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7831 RUSH ROSE DR; ; AS160265
9/26/24, 11:25 AM AS160265 Permit Data City of Carlsbad Sprinkler Permit 7831 RUSH ROSE Job Address: DR Permit Type: SPRINK Parcel No: 2550121900 Lot #: 0 Reference No.: Permit No: AS160265 Status: ISSUED Applied 8/29/2016 Approved: 9/2/2016 Issued: 9/2/2016 PC #: Inspector: Project Title: LA COSTA GLEN-BLDG E BLDG E 3RD FLOOR PIPE REPLACEMENT Applicant: SIMPLEX GRINNELL 3568 RUFFIN ROAD SOUTH SAN DIEGO CA 858-967-5193 Owner: CONTINUING LIFE COMMUNITIES LLC 1940 LEVANTE ST CARLSBAD CA Fees ($) Add'I Fees ($) Total ($) ($) 0 Balance 438 438 0 _ about:blank 1/1 OLWE1HAR! MUflCPAL NATER D:STRCT Are Tcw rt S1ts Service Order# Work Order # EAM# 222t'40 S7 Flow Test Requested By Project Name Le, (,ihz city (o.4SbcLd County S OMWD Personnel Conducting Test YY\ Date 160 Time 13o p,y Address Svp Pressure Zone Zone g-7 Potential Impact To Zone tJ/A Reservoirs Involved tJOr P.R. Stations Involved -- VbIVQ r— Static Pressure (prior to flow test) P.S.I. i 5E Residual Pressure (during flow test) P.S.L. 141 PITOT Residual Pressure 21/2 inch port P.S.I. 1 33 Calculated Flow G.P.M. 177 q Comments Test Results Reviewed By:OW— AS16 1 0265 7831 RUSH ROSE DR OLIVNHAIN MUNICIPAL WATER DISTRICT Service Order Number 222140 CrI-td ........ : OMWDLSMIT:H Assigned To. ............. .Systems Operations Created Date & Time ..: 4/11/2016 12:01 :47 PM Do Not Disconnect..: Scheduled Date.......: 4/11/2016 12:00:00 AM Service Order Type.: Fire Flow Test Service Message.....: Please do fire flow test contact person is Sean Kostka 562-405-3800. skostka@simplexgrinnell.com GPU .........................: W580031 Ux 25S-3- Customer-Account 1025064 100005 Customer Type Residential Account Status Closed Customer Name.......: Omwd Misc Acct Owner APN .................... Primary Cell...............: () - Cycle..................: Handheld Book 001 Home Phone,.............: () - Lid/Cover........... Service Address Box Size ............. San Diego CA 92127 Service Type Dial# MXU# Port # Class # jype Meter# Size Manf seq # Prev Read Prev Date Water' Meter Location: Latitude: Meter Notes: Longitude: Water Meter Location: Latitude: Meter Notes: Longitude: Field Notes Employee Time 1t-.tG LOTh. 6u h,- _________________________ _ _ 4181/0 mike I1w Equipment Exchange Domestic Service Fire Service (if applicable) Exchange Date Old Equipment New Equipment Old Equipment New Equipment Dial U Scrapped nvenory LII Scrapped Inventory Remote/MXU U Scrapped Lj• Inventory [1 Scrapped fl Inventory [J Channel/Port # Pulled Read Pulled Read Remote. Type . . . . Meter U Scrapped [.1 'Inventory fl Scrapped [II Inventory Meter Manufacturer Meter Model New Meter Read Work Completed By .. completed Date: .:Completed Time. . Domestic Meter Read .., Meter Read ''.5/0 Closed By. d T AS16D9 (a 15 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.9 213.7 100.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 213.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 113.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 1 29.0 - - - - 72.2 - - - 2 30.0 - - - - 71.7 - - - 3 33.5 - - - - 70.2 - - - 4 33.5 - - - - 70.2 - - - 5 29.0 - - - - 72.2 - - - 6 30.0 - - - - 71.7 - - - 7 33.5 - - - - 70.2 - - - 8 33.5 - - - - 70.2 9 33.5 - - - - 70.2 - - - 10 33.5 - - - - 70.2 - - - 11 30.0 - - - - 71.7 - - - 12 33.5 - - - - 70.3 - - - 13 33.5 - - - - 70.3 - - - 14 33.5 - - - - 70.6 - - - 15 33.5 - - - - 70.8 - - - 16 33.5 - - - - 72.5 - - 17 33.5 - - - - 72.5 18 33.5 - - - - 72.6 - - - 19 33.5 - - - - 72.6 - - - 20 33.5 - - - - 72.7 - - - 21 33.5 - - - - 73.0 22 33.5 - - - - 74.8 - - - 23 30.0 - - - - 76.4 - - - 24 29.0 - - - - 72.2 - - - 25 30.0 - - - - 71.7 - - - 26 29.0 - - - - 72.2 - - - 27 30.0 - - - - 71.7 - - - 28 29.0 - - - - 72.2 - - 29 30.0 - - - - 71.7 - - - 30 32.0 - - - - 70.9 - - - 31 32.0 - - - - 70.9 - - - 32 32.0 - - - - 70.9 - - - 33 30.0 - - - - 71.7 - - - 34 32.0 - - - - 71.4 - - - 35 32.0 - - - - 72.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Cab 3 - 5 Head Corridor Caic NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 32.0 - - - - 73.0 37 32.0 - - - - 73.1 - - - 38 32.0 - - - - 73.2 39 32.0 - - - - 73.2 40 32.0 - - - - 73.3 41 32.0 - - - - 73.7 - - - 42 32.0 - - - - 75.5 - - - 43 30.0 - - - 76.4 - - - 44 32.0 - - - - 70.8 - - - 45 30.0 - - - - 71.7 - - - 46 32.0 - - - - 71.2 - - - 47 32.0 - - - - 72.6 - - - 48 32.0 - - - - 72.7 - - - 49 32.0 - - - - 72.8 - - - 50 32.0 - - - - 72.9 - - - 51 32.0 - - - - 73.0 - - - 52 32.0 - - - - 73.3 - - - 53 32.0 - - - - 75.0 - - - 54 30.0 - - - - 76.0 - - - 55 32.0 - - - 68.7 - - - 56 30.0 - - - - 71.6 - - - 57 32.0 - - - - 586 - - - 58 29.0 K= 5.60 17.2 23.2 59 32.0 - - - - 24.7 - - - 60 32.0 - - - - 23.4 - - - 61 29.0 K= 5.60 16.2 22.6 62 32.0 - - - - 23.2 - - - 63 29.0 K= 5.60 16.1 22.5 64 32.0 - - - 23.1 - - - 65 32.0 - - - - 23.1 - - - 66 32.0 - - - - 23.2 - - - 67 29.0 K= 5.60 16.2 22.6 68 32.0 - - - - 23.2 - - - 69 29.0 K= 5.60 16.7 22.9 70 32.0 - - - - 24.0 - - - 71 32.0 - - - - 24.2 - - - 72 32.0 - - - - 33.1 - - - 73 32.0 - - - - 73.2 74 30.0 - - - - 75.8 - - - 75 32.0 - - - - 70.9 - - - 76 30.0 - - - - 71.7 - - - 77 32.0 - - - - 71.2 - - - 78 32.0 - - - - 72.6 - - - 79 32.0 - - - - 73.2 - - - 80 32.0 - - - - 74.9 - - - 81 30.0 - - - - 75.8 - - - 82 32.0 - - - - 70.9 - - - 83 30.0 - - - - 71.7 - - - 84 32.0 - - - - 71.1 - - - 85 32.0 - - - - 73.0 - - - 86 32.0 - - - - 74.8 - - - 87 30.0 - - - - 75.8 - - - 88 33.5 - - - - 70.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Cab NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 89 30.0 - - - - 71.7 - - - 90 33.5 - - - - 70.5 - - - 91 33.5 - - - - 72.4 - - - 92 33.5 - - - - 74.2 - - - 93 30.0 - - - - 75.8 - - - 94 30.0 - - - - 76.5 - - - 95 30.0 - - - - 77.8 - - - BOR 0.5 - - - - 94.8 UG3 -3.0 - - - - 96.3 - - - UG2 -3.0 - - - - 96.4 - - - BF2 2.0 - - - - 94.3 BF1 2.0 - - - - 98.3 UG1 -3.0 - - - - 100.5 - - - SRC -3.0 SOURCE 100.5 113.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ., PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 72.2 0.0 0.0 120 FTG ---- FE -0.4 2 30.0 0.0 71.7 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 71.7 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 70.2 0.0 0.000 TL 11.00 FV Pipe: 3 0.0 1.380 FL 2.50 PF 0.0 3 33.5 0.0 70.2 0.0 0.0 120 FTG ---- FE 0.0 4 33.5 0.0 70.2 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 FL 2.21 PF 0.0 4 33.5 0.0 70.2 0.0 0.0 120 FTG ---- FE 0.0 7 33.5 0.0 70.2 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 72.2 0.0 0.0 120 FTG ---- FE -0.4 6 30.0 0.0 71.7 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 FL 4.29 PF 0.0 6 30.0 0.0 71.7 0.0 0.0 120 FTG ET FE -1.5 7 33.5 0.0 70.2 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 FE' 0.0 7 33.5 0.0 70.2 0.0 0.0 120 FTG ---- FE 0.0 8 33.5 0.0 70.2 0.0 0.000 TL 1.75 FV Pipe: 8 0.0 1.380 FL 4.00 PF 0.0 8 33.5 0.0 70.2 0.0 0.0 120 FTG ---- FE 0.0 9 33.5 0.0 70.2 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 FL 0.83 PF 0.0 9 33.5 0.0 70.2 0.0 0.0 120 FTG T FE 0.0 10 33.5 0.0 70.2 0.0 0.000 TL 6.83 PV Pipe: 10 9.6 1.380 FL 3.50 PF 0.1 10 33.5 0.0 70.2 0.0 2.1 120 FTG T PE 1.5 11 30.0 0.0 71.7 0.0 0.009 TL 9.50 PV Pipe: 11 -9.6 1.380 PL 3.17 FE' 0.1 10 33.5 0.0 70.2 0.0 2.1 120 FTG T FE 0.0 12 33.5 0.0 70.3 0.0 0.009 TL 9.17 PV Pipe: 12 -9.6 1.380 FL 4.00 FE' 0.0 12 33.5 0.0 70.3 0.0 2.1 120 FTG ---- FE 0.0 13 33.5 0.0 70.3 0.0 0.009 TL 4.00 PV Pipe: 13 -9.6 1.380 FL 30.25 FE' 0.3 13 33.5 0.0 70.3 0.0 2.1 120 FTG L FE 0.0 14 33.5 0.0 70.6 0.0 0.009 TL 32.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Calc PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 -9.6 1.380 PL 10.42 PF 0.1 14 33.5 0.0 70.6 0.0 2.1 120 FTG T PE 0.0 15 33.5 0.0 70.8 0.0 0.009 TL 16.42 PV Pipe: 15 -9.6 1.380 PL 177.46 PF 1.7 15 33.5 0.0 70.8 0.0 2.1 120 FTG 3ET PE 0.0 16 33.5 0.0 72.5 0.0 0.009 TL 192.46 PV Pipe: 16 -9.6 1.380 PL 6.00 PF 0.1 16 33.5 0.0 72.5 0.0 2.1 120 FTG ---- PE 0.0 17 33.5 0.0 72.5 0.0 0.009 TL 6.00 PV Pipe: 17 -9.6 1.380 PL 6.00 PF 0.1 17 33.5 0.0 72.5 0.0 2.1 120 FTG ---- PE 0.0 18 33.5 0.0 72.6 0.0 0.009 TL 6.00 PV Pipe: 18 -9.6 1.380 PL 6.00 PP 0.1 18 33.5 0.0 72.6 0.0 2.1 120 FTG ---- FE 0.0 19 33.5 0.0 72.6 0.0 0.009 TL 6.00 PV Pipe: 19 -9.6 1.380 PL 6.00 PP 0.1 19 33.5 0.0 72.6 0.0 2.1 120 FTG ---- PE 0.0 20 33.5 0.0 72.7 0.0 0.009 TL 6.00 PV Pipe: 20 -9.6 1.380 PL 26.42 PF 0.3 20 33.5 0.0 72.7 0.0 2.1 120 FTG 2E PE 0.0 21 33.5 0.0 73.0 0.0 0.009 TL 32.42 PV Pipe: 21 -9.6 1.380 PL 189.96 PF 1.8 21 33.5 0.0 73.0 0.0 2.1 120 FTG 4ET PE 0.0 22 33.5 0.0 74.8 0.0 0.009 TL 207.96 PV Pipe: 22 -9.6 1.380 FL 3.50 PP 0.1 22 33.5 0.0 74.8 0.0 2.1 120 FTG T PE 1.5 23 30.0 0.0 76.4 0.0 0.009 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PF 0.0 24 29.0 0.0 72.2 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 71.7 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PP 0.0 25 30.0 0.0 71.7 0.0 0.0 120 FTG ---- PE 0.0 27 30.0 0.0 71.7 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PP 0.0 26 29.0 0.0 72.2 0.0 0.0 120 FTG ---- PE -0.4 27 30.0 0.0 71.7 0.0 0.000 TL 35.00 PV Pipe: 26 0.0 1.380 PL 3.50 PP 0.0 27 30.0 0.0 71.7 0.0 0.0 120 FTG ---- FE 0.0 29 30.0 0.0 71.7 0.0 0.000 TL 3.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 27 0.0 1.049 PL 35.00 PP 0.0 28 29.0 0.0 72.2 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 71.7 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 71.7 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 70.9 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PP 0.0 30 32.0 0.0 70.9 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 70.9 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PP 0.0 31 32.0 0.0 70.9 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 70.9 0.0 0.000 TL 6.96 PV Pipe: 31 10.1 1.380 PL 2.00 PP 0.1 32 32.0 0.0 70.9 0.0 2.2 120 FTG T PE 0.9 33 30.0 0.0 71.7 0.0 0.010 TL 8.00 PV Pipe: 32 -10.1 1.380 PL 47.58 PP 0.5 32 32.0 0.0 70.9 0.0 2.2 120 FTG TL FE 0.0 3,4 32.0 0.0 71.4 0.0 0.010 TL 55.58 PV Pipe: 33 -10.1 1.380 PL 138.50 PP 1.4 34 32.0 0.0 71.4 0.0 2.2 120 FTG 3E PE 0.0 35 32.0 0.0 72.8 0.0 0.010 TL 147.50 PV Pipe: 34 -10.1 1.380 PL 14.00 PP 0.2 35 32.0 0.0 72.8 0.0 2.2 120 FTG E PE 0.0 36 32.0 0.0 73.0 0.0 0.010 TL 17.00 PV Pipe: 35 -10.1 1.380 PL 10.00 PP 0.1 36 32.0 0.0 73.0 0.0 2.2 120 FTG ---- PE 0.0 37 32.0 0.0 73.1 0.0 0.010 TL 10.00 PV Pipe: 36 -10.1 1.380 FL 8.00 PP 0.1 37 32.0 0.0 73.1 0.0 2.2 120 FTG ---- FE 0.0 39 32.0 0.0 73.2 0.0 0.010 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 PP 0.0 38 32.0 0.0 73.2 0.0 0.0 120 FTG ---- PE 0.0 39 32.0 0.0 73.2 0.0 0.000 TL 10.00 PV Pipe: 38 -10.1 1.380 PL 10.00 PF 0.1 39 32.0 0.0 73.2 0.0 2.2 120 FTG ---- PE 0.0 40 32.0 0.0 73.3 0.0 0.010 TL 10.00 PV Pipe: 39 -10.1 1.380 FL 34.67 PP 0.5 40 32.0 0.0 73.3 0.0 2.2 120 FTG 4E FE 0.0 41 32.0 0.0 73.7 0.0 0.010 TL 46.67 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Cab PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 40 -10.1 1.380 PL 175.12 PF 1.8 41 32.0 0.0 73.7 0.0 2.2 120 FTG T PE 0.0 42 32.0 0.0 75.5 0.0 0.010 TL 181.12 PV Pipe: 41 -10.1 1.380 PL 2.00 PF 0.1 42 32.0 0.0 75.5 0.0 2.2 120 FTG T PE 0.9 43 30.0 0.0 76.4 0.0 0.010 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 70.8 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 71.7 0.0 0.000 TL 8.00 PV Pipe: 43 -9.9 1.380 PL 41.25 PF 0.5 45 30.0 0.0 71.7 0.0 2.1 120 FTG TL PE -0.9 46 32.0 0.0 71.2 0.0 0.009 TL 49.25 PV Pipe: 44 -9.9 1.380 PL 145.04 PF 1.4 46 32.0 0.0 71.2 0.0 2.1 120 FTG ---- PE 0.0 47 32.0 0.0 72.6 0.0 0.009 TL 145.04 PV Pipe: 45 -9.9 1.380 PL 10.00 PF 0.1 47 32.0 0.0 72.6 0.0 2.1 120 FTG ---- PE 0.0 48 32.0 0.0 72.7 0.0 0.009 TL 10.00 PV Pipe: 46 -9.9 1.380 PL 8.00 PF 0.1 48 32.0 0.0 72.7 0.0 2.1 120 FTG ---- PE 0.0 49 32.0 0.0 72.8 0.0 0.009 TL 8.00 PV Pipe: 47 -9.9 1.380 PL 10.00 PF 0.1 49 32.0 0.0 72.8 0.0 .2.1 120 FTG ---- PE 0.0 50 32.0 0.0 72.9 0.0 0.009 TL 10.00 PV Pipe: 48 -9.9 1.380 PL 10.00 PF 0.1 50 32.0 0.0 72.9 0.0 2.1 120 FTG ---- PE 0.0 51 32.0 0.0 73.0 0.0 0.009 TL 10.00 PV Pipe: 49 -9.9 1.380 PL 27.96 PF 0.3 51 32.0 0.0 73.0 0.0 2.1 120 FTG 2E PE 0.0 52 32.0 0.0 73.3 0.0 0.009 TL 33.96 PV Pipe: 50 -9.9 1.380 PL 182.33 PF 1.8 52 32.0 0.0 73.3 0.0 2.1 120 FTG T PE 0.0 53 32.0 0.0 75.0 0.0 0.009 TL 188.33 PV Pipe: 51 -9.9 1.380 PL 2.00 PF 0.1 53 32.0 0.0 75.0 0.0 2.1 120 FTG T PE 0.9 54 30.0 0.0 76.0 0.0 0.009 TL 8.00 PV Pipe: 52 -58.9 1.380 PL 2.00 PF 2.0 55 32.0 0.0 68.7 0.0 12.6 120 FTG T PE 0.9 56 30.0 0.0 71.6 0.0 0.252 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3..SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Cab PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 58.9 1.380 PL 38.17 PF 10.1 55 32.0 0.0 68.7 0.0 12.6 120 FTG L PE 0.0 57 32.0 0.0 58.6 0.0 0.252 TL 40.17 PV Pipe: 54 58.9 1.380 PL 134.70 PP 34.0 57 32.0 0.0 58.6 0.0 12.6 120 FTG ---- PE 0.0 59 32.0 0.0 24.7 0.0 0.252 TL 134.70 PV Pipe: 55 -23.2 1.049 PL 51.00 PP 8.8 58 29.0 5.6 17.2 23.2 8.6 120 FTG ---- PE -1.3 59 32.0 0.0 24.7 0.0 0.172 TL 51.00 PV Pipe: 56 35.6 1.380 PL 12.50 PF 1.2 59 32.0 0.0 24.7 0.0 7.6 120 FTG ---- PE 0.0 60 32.0 0.0 23.4 0.0 0.100 TL 12.50 PV Pipe: 57 35.6 1.380 PL 1.83 PF 0.2 60 32.0 0.0 23.4 0.0 7.6 120 FTG ---- PE 0.0 62 32.0 0.0 23.2 0.0 0.100 TL 1.83 PV Pipe: 58 -22.6 1.049 PL 51.00 PP 8.3 61 29.0 5.6 16.2 22.6 8.4 120 FTG ---- PE -1.3 62 32.0 0.0 23.2 0.0 0.163 TL 51.00 PV Pipe: 59 13.1 1.380 PL 9.25 PP 0.1 62 32.0 0.0 23.2 0.0 2.8 120 FTG ---- PE 0.0 64 32.0 0.0 23.1 0.0 0.016 TL 9.25 PV Pipe: 60 -22.5 1.049 PL 51.00 PP 8.3 63 29.0 5.6 16.1 22.5 8.4 120 FTG ---- FE -1.3 64 32.0 0.0 23.1 0.0 0.162 TL 51.00 PV Pipe: 61 -9.4 1.380 PL 0.92 PP 0.0 64 32.0 0.0 23.1 0.0 2.0 120 FTG ---- FE 0.0 65 32.0 0.0 23.1 0.0 0.009 TL 0.92 PV Pipe: 62 -9.4 1.380 PL 12.00 PF 0.1 65 32.0 0.0 23.1 0.0 2.0 120 FTG ---- FE 0.0 66 32.0 0.0 23.2 0.0 0.009 TL 12.00 PV Pipe: 63 -9.4 1.380 PL 1.42 PP 0.0 66 32.0 0.0 23.2 0.0 2.0 120 FTG ---- PE 0.0 68 32.0 0.0 23.2 0.0 0.009 TL 1.42 PV Pipe: 64 -22.6 1.049 FL 51.00 PP 8.3 67 29.0 5.6 16.2 22.6 8.4 120 FTG ---- FE -1.3 68 32.0 0.0 23.2 0.0 0.163 TL 51.00 PV Pipe: 65 -32.0 1.380 PL 9.17 PP 0.7 68 32.0 0.0 23.2 0.0 6.9 120 FTG ---- FE 0.0 70 32.0 0.0 24.0 0.0 0.082 TL 9.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDP JOB TITLE: La Costa Glen Building H Calc 3 - 5 Head Corridor Calc PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 66 -22.9 1.049 PL 51.00 PF 8.5 69 29.0 5.6 16.7 22.9 8.5 120 FTG ---- PE -1.3 70 32.0 0.0 24.0 0.0 0.167 TL 51.00 PV Pipe: 67 -54.9 1.380 PL 1.25 PP 0.3 70 32.0 0.0 24.0 0.0 11.8 120 FTG ---- PE 0.0 71 32.0 0.0 24.2 0.0 0.222 TL 1.25 PV Pipe: 68 -54.9 1.380 PL 30.80 PF 8.8 71 32.0 0.0 24.2 0.0 11.8 120 FTG ET PH 0.0 72 32.0 0.0 33.1 0.0 0.222 TL 39.80 PV Pipe: 69 -54.9 1.380 PL 175.00 PP 40.1 72 32.0 0.0 33.1 0.0 11.8 120 FTG T PE 0.0 73 32.0 0.0 73.2 0.0 0.222 TL 181.00 PV Pipe: 70 -54.9 1.380 PL 2.00 PP 1.8 73 32.0 0.0 73.2 0.0 11.8 120 FTG T PE 0.9 74 30.0 0.0 75.8 0.0 0.222 TL 8.00 PV Pipe: 71 9.8 1.380 PL 2.00 PF 0.1 75 32.0 0.0 70.9 0.0 2.1 120 FTG T PE 0.9 76 30.0 0.0 71.7 0.0 0.009 TL 8.00 PV Pipe: 72 -9.8 1.380 PL 38.25 PP 0.4 75 32.0 0.0 70.9 0.0 2.1 120 FTG L PE 0.0 77 32.0 0.0 71.2 0.0 0.009 TL 40.25 PV Pipe: 73 -9.8 1.380 PL 150.42 PF 1.4 77 32.0 0.0 71.2 0.0 2.1 120 FTG ---- PE 0.0 78 32.0 0.0 72.6 0.0 0.009 TL 150.42 PV Pipe: 74 -9.8 1.380 PL 65.83 PP 0.7 78 32.0 0.0 72.6 0.0 2.1 120 FTG 2E PE 0.0 79 32.0 0.0 73.2 0.0 0.009 TL 71.83 PV Pipe: 75 -9.8 1.380 PL 170.83 PF 1.6 79 32.0 0.0 73.2 0.0 2.1 120 FTG T PE 0.0 80 32.0 0.0 74.9 0.0 0.009 TL 176.83 PV Pipe: 76 -9.8 1.380 PL 2.00 PP 0.1 80 32.0 0.0 74.9 0.0 2.1 120 FTG T PE 0.9 81 30.0 0.0 75.8 0.0 0.009 TL 8.00 PV Pipe: 77 9.8 1.380 PL 2.00 PP 0.1 82 32.0 0.0 70.9 0.0 2.1 120 FTG T PE 0.9 83 30.0 0.0 71.7 0.0 0.009 TL 8.00 PV Pipe: 78 -9.8 1.380 PL 24.58 PF 0.2 82 32.0 0.0 70.9 0.0 2.1 120 FTG L PE 0.0 84 32.0 0.0 71.1 0.0 0.009 TL 26.58 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Calc PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 79 -9.8 1.380 FL 190.50 PF 1.9 84 32.0 0.0 71.1 0.0 2.1 120 FTG 4E PE 0.0 85 32.0 0.0 73.0 0.0 0.009 TL 202.50 PV Pipe: 80 -9.8 1.380 PL 196.21 PF 1.9 85 32.0 0.0 73.0 0.0 2.1 120 FTG T FE 0.0 86 32.0 0.0 74.8 0.0 0.009 TL 202.21 PV Pipe: 81 -9.8 1.380 FL 2.00 PF 0.1 86 32.0 0.0 74.8 0.0 2.1 120 FTG T PE 0.9 87 30.0 0.0 75.8 0.0 0.009 TL 8.00 PV Pipe: 82 9.6 1.380 FL 3.50 PF 0.1 88 33.5 0.0 70.2 0.0 2.1 120 FTG T PE 1.5 89 30.0 0.0 71.7 0.0 0.009 TL 9.50 PV Pipe: 83 -9.6 1.380 PL 33.58 PF 0.3 88 33.5 0.0 70.2 0.0 2.1 120 FTG L FE 0.0 90 33.5 0.0 70.5 0.0 0.009 TL 35.58 PV Pipe: 84 -9.6 1.380 FL 202.38 PF 1.9 90 33.5 0.0 70.5 0.0 2.1 120 FTG 3ET PE 0.0 91 33.5 0.0 72.4 0.0 0.009 TL 217.38 PV Pipe: 85 -9.6 1.380 FL 193.96 PF 1.7 91 33.5 0.0 72.4 0.0 2.1 120 FTG T PE 0.0 92 33.5 0.0 74.2 0.0 0.009 TL 199.96 PV Pipe: 86 -9.6 1.380 FL 3.50 PF 0.1 92 33.5 0.0 74.2 0.0 2.1 120 FTG T PE 1.5 93 30.0 0.0 75.8 0.0 0.009 TL 9.50 FV Pipe: 87 9.6 2.635 FL 3.00 PF 0.0 11 30.0 0.0 71.7 0.0 0.6 120 FTG ---- FE 0.0 33 30.0 0.0 71.7 0.0 0.000 TL 3.00 PV Pipe: 88 19.7 2.635 FL 8.50 PF 0.0 33 30.0 0.0 71.7 0.0 1.2 120 FTG ---- FE 0.0 45 30.0 0.0 71.7 0.0 0.001 TL 8.50 PV Pipe: 89 29.7 2.635 FL 6.92 PF 0.0 45 30.0 0.0 71.7 0.0 1.7 120 FTG ---- FE 0.0 56 30.0 0.0 71.6 0.0 0.003 TL 6.92 PV Pipe: 90 -29.2 2.635 FL 7.42 PF 0.0 56 30.0 0.0 71.6 0.0 1.7 120 FTG ---- FE 0.0 76 30.0 0.0 71.7 0.0 0.003 TL 7.42 PV Pipe: 91 -19.4 2.635 FL 7.00 PF 0.0 76 30.0 0.0 71.7 0.0 1.1 120 FTG ---- FE 0.0 83 30.0 0.0 71.7 0.0 0.001 TL 7.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 10/11/2016RAM PILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDP JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 92 -9.6 2.635 PL 3.92 PP 0.0 83 30.0 0.0 71.7 0.0 0.6 120 FTG ---- PE 0.0 89 30.0 0.0 71.7 0.0 0.000 TL 3.92 PV Pipe: 93 -9.6 2.635 PL 5.54 PP 0.0 23 30.0 0.0 76.4 0.0 0.6 120 FTC ---- PE 0.0 43 30.0 0.0 76.4 0.0 0.000 TL 5.54 PV Pipe: 94 -19.7 2.635 PL 8.96 PF 0.0 43 30.0 0.0 76.4 0.0 1.2 120 FTG T PE 0.0 94 30.0 0.0 76.5 0.0 0.001 TL 25.96 PV Pipe: 95 -9.6 2.635 PL 5.40 PP 0.0 93 30.0 0.0 75.8 0.0 0.6 120 FTG ---- PE 0.0 87 30.0 0.0 75.8 0.0 0.000 TL 5.40 PV Pipe: 96 -19.4 2.635 PL 9.50 PP 0.0 87 30.0 0.0 75.8 0.0 1.1 120 FTG ---- PE 0.0 81 30.0 0.0 75.8 0.0 0.001 TL 9.50 PV Pipe: 97 -29.2 2.635 PL 8.17 PP 0.0 81 30.0 0.0 75.8 0.0 1.7 120 FTC ---- PE 0.0 74 30.0 0.0 75.8 0.0 0.003 TL 8.17 PV Pipe: 98 -84.1 2.635 PL 7.96 PP 0.2 74 30.0 0.0 75.8 0.0 4.9 120 FTC ---- PE 0.0 54 30.0 0.0 76.0 0.0 0.021 TL 7.96 PV Pipe: 99 -94.0 2.635 PL 1.04 PP 0.5 54 30.0 0.0 76.0 0.0 5.5 120 FTG T PE 0.0 94 30.0 0.0 76.5 0.0 0.026 TL 18.04 PV Pipe: 100 -113.8 2.635 PL 20.38 PP 1.3 94 30.0 0.0 76.5 0.0 6.7 120 FTG 2E PE 0.0 95 30.0 0.0 77.8 0.0 0.037 TL 36.38 PV Pipe: 101 -113.8 2.635 PL 75.50 PP 4.2 95 30.0 0.0 77.8 0.0 6.7 120 FTG 5E PE 12.8 BOR 0.5 0.0 94.8 0.0 0.037 TL 115.50 PV Pipe: 102 -113.8 6.280 PL 10.00 PP 0.0 BOR 0.5 0.0 94.8 0.0 1.2 140 FTG E PE 1.5 UG3 -3.0 0.0 96.3 0.0 0.000 TL 32.00 PV Pipe: 103 -113.8 6.080 PL 142.00 PP 0.1 UG3 -3.0 0.0 96.3 0.0 1.3 150 FTG 3E PE 0.0 UG2 -3.0 0.0 96.4 0.0 0.000 TL 208.00 PV Pipe: 104 -113.8 6.280 PL 5.00 PP 0.0 UG2 -3.0 0.0 96.4 0.0 1.2 140 FTG ET PE -2.2 BF2 2.0 0.0 94.3 0.0 0.000 TL 74.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Calc PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 98.3 0.0 4.0 psi, 113.8 gpm BF2 2.0 0.0 94.3 0.0 Pipe: 106 -113.8 6.280 FL 5.00 FE' 0.0 BF1 2.0 0.0 98.3 0.0 1.2 140 FTG 2E FE 2.2 UG1 -3.0 0.0 100.5 0.0 0.000 TL 49.00 PV Pipe: 107 -113.7 6.080 PL 16.00 PF 0.0 UG1 -3.0 0.0 100.5 0.0 1.3 150 FTG TG PE 0.0 SRC -3.0 SRCE 100.5 (N/A) 0.000 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.187 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.6 ft/sec at pipe 53. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.84 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Calc PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 1A 140.0 G A120 0 U G E 100• R E S S 80.0 LI, R E WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm LEGEND 1Availab1e pressure 154.88 psi @ 213.7 gpm- -2 Required pressure 100.48 psi 8 213.7 gpm lA Avail. OnSite Demand Press 154.88 psi @ 113.7 gpm 2A Req. OnSite Demand Press. 100.48 psi 8 113.7 gpm A. Source Supply Curve System Demand Curve Available at Source '1swt p S i 40.0 20.0 B 0.0 -14.7 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) ished Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 10/11/2016RAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Cab 3 - 5 Head Corridor Cab WATER SUPPLY CURVE \\\\\\\\\\\\\\\\\\\\\\\\\\ I 149.0 psi @ 1790 gpm-> * I Flow Test Point 143+ 130+ 117+ P104+ R IX E I S S 91+ U I R I E 78+ P I S I I 65+ 52+ 39+ 26+ LEGEND I X = Required Water Supply 100.48 psi @ 213.7 gpm 13+ I 0 = Available Water Supply 154.88 psi @ 213.7 gpm 7 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.8 268.8 129.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 268.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 168.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 K= 6.90 43.7 45.6 2 30.0 - - - - 73.7 - - - 3 33.5 - - - - 73.2 - - - 4 33.5 - - - - 73.3 - - - 5 29.0 - - - - 75.5 - - - 6 33.5 - - -, - 73.5 - - - 7 33.5 - - - - 73.5 8 33.5 - - - - 73.6 - - - 9 33.5 - - - - 73.9 10 33.5 - - - - 74.6 11 30.0 - - - - 76.3 - - - 12 33.5 - - - - 75.0 13 33.5 - - - - 75.2 - - - 14 33.5 - - - - 76.6 - - - 15 33.5 - - - - 77.3 - - - 16 33.5 - - - - 85.9 - - - 17 33.5 - - - - 86.2 - - - 18 33.5 - - - - 86.5 - - - 19 33.5 - - - - 86.7 - - - 20 33.5 - - - - 87.0 - - - 21 33.5 - - - - 88.4 - - - 22 33.5 - - - - 97.7 - - - 23 30.0 - - - - 99.5 - - - 24 29.0 K= 6.90 38.7 42.9 25 30.0 - - - - 56.9 - - - 26 29.0 K= 6.90 33.6 40.0 27 30.0 - - - - 57.1 - - - 28 29.0 K= 6.90 34.1 40.3 29 30.0 - - - - 57.9 - - - 30 32.0 - - - - 64.5 - - - 31 32.0 - - - - 68.3 - - - 32 32.0 - - - - 72.4 - - - 33 30.0 - - - - 76.3 - - - 34 32.0 - - - - 75.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 83.5 - - - 36 32.0 - - - - 84.4 - - - 37 32.0 - - - - 85.0 - - - 38 32.0 - - - - 85.4 - - - 39 32.0 - - - - 85.4 - - - 40 32.0 - - - - 86.0 - - - 41 32.0 - - - - 88.5 - - - 42 32.0 - - - - 98.4 - - - 43 30.0 - - - - 99.5 - - - 44 32.0 - - - - 75.8 - - - 45 30.0 - - - - 76.7 - - - 46 32.0 - - - - 78.2 - - - 47 32.0 - - - - 85.2 - - - 48 32.0 - - - - 85.7 - - - 49 32.0 - - - - 86.1 - - - 50 32.0 - - - - 86.6 - - - 51 32.0 - - - - 87.1 - - - 52 32.0 - - - - 88.7 - - - 53 32.0 - - - - 97.9 - - - 54 30.0 - - - - 99.0 - - - 55 32.0 - - - - 76.2 - - - 56 30.0 - - - - 76.9 - - - 57 32.0 - - - - 78.2 - - - 58 29.0 - - - - 86.0 - - - 59 32.0 - - - - 84.7 - - - 60 32.0 - - - - 85.3 - - - 61 29.0 - - - - 86.7 - - - 62 32.0 - - - - 85.4 - - - 63 29.0 - - - - 87.1 - - - 64 32.0 - - - - 85.8 - - - 65 32.0 - - - - 85.8 - - - 66 32.0 - - - - 86.4 - - - 67 29.0 - - - - 87.8 - - - 68 32.0 - - - - 86.5 - - - 69 29.0 - - - - 88.2 - - - 70 32.0 - - - - 86.9 - - - 71 32.0 - - - - 87.0 - - - 72 32.0 - - - - 88.9 - - - 73 32.0 - - - - 97.6 - - - 74 30.0 - - - - 98.7 - - - 75 32.0 - - - - 76.3 - - - 76 30.0 - - - - 77.0 - - - 77 32.0 - - - - 78.3 - - - 78 32.0 - - - - 85.5 - - - 79 32.0 - - - - 89.0 - - - 80 32.0 - - - - 97.5 - - - 81 30.0 - - - - 98.6 - - - 82 32.0 - - - - 76.4 - - - 83 30.0 - - - - 77.0 - - - 84 32.0 - - - - 77.7 - - - 85 32.0 - - - - 87.5 - - - 86 32.0 - - - - 97.3 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/11/2016RAM .FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 87 30.0 - - - - 98.5 - - - 88 33.5 - - - - 75.8 89 30.0 - - - - 77.0 - - - 90 33.5 - - - - 77.4 - - - 91 33.5 - - - - 87.5 - - - 92 33.5 - - - - 96.8 - - - 93 30.0 - - - - 98.5 - - - 94 30.0 - - - - 99.7 - - - 95 30.0 - - - - 102.4 - - - BOR 0.5 - - - - 124.0 UG3 -3.0 - - - - 125.5 UG2 -3.0 - - - - 125.7 BF2 2.0 - - - - 123.6 - - - BF1 2.0 - - - - 127.6 UG1 -3.0 - - - - 129.8 - - - SRC -3.0 SOURCE 129.9 168.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/11/2016RAJ4 FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Cab 5 - Res. Heads 20x20 PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 -45.6 1.049 PL 51.00 PF 30.5 1 29.0 6.9 43.7 45.6 16.9 120 FTG ---- PE -0.4 2 30.0 0.0 73.7 0.0 0.598 TL 51.00 PV Pipe: 2 -45.6 1.610 PL 5.00 PF 1.0 2 30.0 0.0 73.7 0.0 7.2 120 FTG 2E FE -1.5 3 33.5 0.0 73.2 0.0 0.074 TL 13.00 PV Pipe: 3 -45.6 1.610 FL 2.50 PF 0.2 3 33.5 0.0 73.2 0.0 7.2 120 FTG ---- PE 0.0 4 33.5 0.0 73.3 0.0 0.074 TL 2.50 PV Pipe: 4 -45.6 1.610 PL 2.21 PF 0.2 4 33.5 0.0 73.3 0.0 7.2 120 FTG ---- PE 0.0 7 33.5 0.0 73.5 0.0 0.074 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 75.5 0.0 0.0 120 FTG ---- PE -1.9 6 33.5 0.0 73.5 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 0.83 PF 0.0 6 33.5 0.0 73.5 0.0 0.0 120 FTG ET PE 0.0 7 33.5 0.0 73.5 0.0 0.000 TL 9.83 PV Pipe: 7 -45.6 1.610 PL 1.75 PF 0.1 7 33.5 0.0 73.5 0.0 7.2 120 FTG ---- PE 0.0 8 33.5 0.0 73.6 0.0 0.074 TL 1.75 PV Pipe: 8 -45.6 1.610 PL 4.00 PF 0.3 8 33.5 0.0 73.6 0.0 7.2 120 FTG ---- PE 0.0 9 33.5 0.0 73.9 0.0 0.074 TL 4.00 PV Pipe: 9 -45.6 1.610 PL 0.83 PF 0.7 9 33.5 0.0 73.9 0.0 7.2 120 FTG T PE 0.0 10 33.5 0.0 74.6 0.0 0.074 TL 8.83 PV Pipe: 10 -22.5 1.610 FL 3.50 PF 0.2 10 33.5 0.0 74.6 0.0 3.5 120 FTG T FE 1.5 11 30.0 0.0 76.3 0.0 0.020 TL 11.50 PV Pipe: 11 -23.1 1.380 PL 3.17 PF 0.4 10 33.5 0.0 74.6 0.0 5.0 120 FTG T FE 0.0 12 33.5 0.0 75.0 0.0 0.045 TL 9.17 PV Pipe: 12 -23.1 1.380 FL 4.00 PF 0.2 12 33.5 0.0 75.0 0.0 5.0 120 FTG ---- FE 0.0 13 33.5 0.0 75.2 0.0 0.045 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -23.1 1.380 FL 30.25 PF 1.4 13 33.5 0.0 75.2 0.0 5.0 120 FTG L PE 0.0 14 33.5 0.0 76.6 0.0 0.045 TL 32.25 PV Pipe: 14 -23.1 1.380 PL 10.42 PF 0.7 14 33.5 0.0 76.6 0.0 5.0 120 FTG T FE 0.0 15 33.5 0.0 77.3 0.0 0.045 TL 16.42 PV Pipe: 15 -23.1 1.380 PL 177.46 PP 8.6 15 33.5 0.0 77.3 0.0 5.0 120 FTG 3ET PE 0.0 16 33.5 0.0 85.9 0.0 0.045 TL 192.46 PV Pipe: 16 -23.1 1.380 PL 6.00 PP 0.3 16 33.5 0.0 85.9 0.0 5.0 120 FTG ---- PE 0.0 17 33.5 0.0 86.2 0.0 0.045 TL 6.00 PV Pipe: 17 -23.1 1.380 PL 6.00 PP 0.3 17 33.5 0.0 86.2 0.0 5.0 120 FTG ---- PE 0.0 18 33.5 0.0 86.5 0.0 0.045 TL 6.00 PV Pipe: 18 -23.1 1.380 FL 6.00 PF 0.3 18 33.5 0.0 86.5 0.0 5.0 120 FTG ---- PE 0.0 19 33.5 0.0 86.7 0.0 0.045 TL 6.00 PV Pipe: 19 -23.1 1.380 PL 6.00 PF 0.3 19 33.5 0.0 86.7 0.0 5.0 120 FTG ---- FE 0.0 20 33.5 0.0 87.0 0.0 0.045 TL 6.00 PV Pipe: 20 -23.1 1.380 PL 26.42 PF 1.4 20 33.5 0.0 87.0 0.0 5.0 120 FTG 2E PE 0.0 21 33.5 0.0 88.4 0.0 0.045 TL 32.42 PV Pipe: 21 -23.1 1.380 FL 189.96 PF 9.3 21 33.5 0.0 88.4 0.0 5.0 120 FTG 4ET FE 0.0 22 33.5 0.0 97.7 0.0 0.045 TL 207.96 PV Pipe: 22 -23.1 1.610 FL 3.50 PP 0.2 22 33.5 0.0 97.7 0.0 3.6 120 FTG T FE 1.5 23 30.0 0.0 99.5 0.0 0.021 TL 11.50 PV Pipe: 23 -42.9 1.049 PL 35.00 PP 18.7 24 29.0 6.9 38.7 42.9 15.9 120 FTG ---- PE -0.4 25 30.0 0.0 56.9 0.0 0.534 TL 35.00 PV Pipe: 24 -42.9 1.610 FL 2.75 PF 0.2 25 30.0 0.0 56.9 0.0 6.8 120 FTG ---- FE 0.0 27 30.0 0.0 57.1 0.0 0.066 TL 2.75 PV Pipe: 25 -40.0 1.049 FL 51.00 PF 23.9 26 29.0 6.9 33.6 40.0 14.8 120 FTG ---- PE -0.4 27 30.0 0.0 57.1 0.0 0.469 TL 51.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/11/2016RAM FILES\HRS SYSTENS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 -82.9 1.610 PL 3.50 PF 0.8 27 30.0 0.0 57.1 0.0 13.1 120 FTG ---- FE 0.0 29 30.0 0.0 57.9 0.0 0.224 TL 3.50 PV Pipe: 27 -40.3 1.049 PL 51.00 PF 24.2 28 29.0 6.9 34.1 40.3 15.0 120 FTG ---- PE -0.4 29 30.0 0.0 57.9 0.0 0.475 TL 51.00 PV Pipe: 28 -123.2 1.610 PL 8.12 PF 7.5 29 30.0 0.0 57.9 0.0 19.4 120 FTG 2E PE -0.9 30 32.0 0.0 64.5 0.0 0.467 TL 16.12 PV Pipe: 29 -123.2 1.610 PL 8.00 PF 3.7 30 32.0 0.0 64.5 0.0 19.4 120 FTG ---- FE 0.0 31 32.0 0.0 68.3 0.0 0.467 TL 8.00 PV Pipe: 30 -123.2 1.610 PL 0.96 PF 4.2 31 32.0 0.0 68.3 0.0 19.4 120 FTG T PE 0.0 32 32.0 0.0 72.4 0.0 0.467 TL 8.96 PV Pipe: 31 -97.5 1.610 FL 2.00 PF 3.0 32 32.0 0.0 72.4 0.0 15.4 120 FTG T PE 0.9 33 30.0 0.0 76.3 0.0 0.303 TL 10.00 PV Pipe: 32 -25.7 1.380 FL 47.58 PF 3.0 32 32.0 0.0 72.4 0.0 5.5 120 FTG TL PE 0.0 34 32.0 0.0 75.5 0.0 0.054 TL 55.58 PV Pipe: 33 -25.7 1.380 FL 138.50 FE' 8.0 34 32.0 0.0 75.5 0.0 5.5 120 FTG 3E FE 0.0 35 32.0 0.0 83.5 0.0 0.054 TL 147.50 PV Pipe: 34 -25.7 1.380 FL 14.00 PF 0.9 35 32.0 0.0 83.5 0.0 5.5 120 FTG E PE 0.0 36 32.0 0.0 84.4 0.0 0.054 TL 17.00 PV Pipe: 35 -25.7 1.380 FL 10.00 PF 0.5 36 32.0 0.0 84.4 0.0 5.5 120 FTG ---- FE 0.0 37 32.0 0.0 85.0 0.0 0.054 TL 10.00 PV Pipe: 36 -25.7 1.380 FL 8.00 PF 0.4 37 32.0 0.0 85.0 0.0 5.5 120 FTG ---- PE 0.0 39 32.0 0.0 85.4 0.0 0.054 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 FE' 0.0 38 32.0 0.0 85.4 0.0 0.0 120 FTG ---- PE 0.0 39 32.0 0.0 85.4 0.0 0.000 TL 10.00 PV Pipe: 38 -25.7 1.380 FL 10.00 PF 0.5 39 32.0 0.0 85.4 0.0 5.5 120 FTG ---- FE 0.0 40 32.0 0.0 86.0 0.0 0.054 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) H(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -25.7 1.380 PL 34.67 PF 2.5 40 32.0 0.0 86.0 0.0 5.5 120 FTG 4E PE 0.0 41 32.0 0.0 88.5 0.0 0.054 TL 46.67 PV Pipe: 40 -25.7 1.380 PL 175.12 PF 9.9 41 32.0 0.0 88.5 0.0 5.5 120 FTG T PE 0.0 42 32.0 0.0 98.4 0.0 0.054 TL 181.12 PV Pipe: 41 -25.7 1.610 PL 2.00 PF 0.3 42 32.0 0.0 98.4 0.0 4.1 120 FTG T PE 0.9 43 30.0 0.0 99.5 0.0 0.026 TL 10.00 PV Pipe: 42 0.0 1.610 PL 2.00 PF 0.0 44 32.0 0.0 75.8 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 76.7 0.0 0.000 TL 10.00 PV Pipe: 43 -24.1 1.380 PL 41.25 PF 2.4 45 30.0 0.0 76.7 0.0 5.2 120 FTG TL PE -0.9 46 32.0 0.0 78.2 0.0 0.048 TL 49.25 PV Pipe: 44 -24.1 1.380 PL 145.04 PF 7.0 46 32.0 0.0 78.2 0.0 5.2 120 FTG ---- PE 0.0 47 32.0 0.0 85.2 0.0 0.048 TL 145.04 PV Pipe: 45 -24.1 1.380 PL 10.00 PP 0.5 47 32.0 0.0 85.2 0.0 5.2 120 FTG ---- PE 0.0 48 32.0 0.0 85.7 0.0 0.048 TL 10.00 PV Pipe: 46 -24.1 1.380 PL 8.00 PP 0.4 48 32.0 0.0 85.7 0.0 5.2 120 FTG ---- PE 0.0 49 32.0 0.0 86.1 0.0 0.048 TL 8.00 PV Pipe: 47 -24.1 1.380 PL 10.00 PP 0.5 49 32.0 0.0 86.1 0.0 5.2 120 FTG ---- PE 0.0 50 32.0 0.0 86.6 0.0 0.048 TL 10.00 PV Pipe: 48 -24.1 1.380 PL 10.00 PP 0.5 50 32.0 0.0 86.6 0.0 5.2 120 FTG ---- PE 0.0 51 32.0 0.0 87.1 0.0 0.048 TL 10.00 PV Pipe: 49 -24.1 1.380 PL 27.96 PF 1.6 51 32.0 0.0 87.1 0.0 5.2 120 FTG 2E PE 0.0 52 32.0 0.0 88.7 0.0 0.048 TL 33.96 PV Pipe: 50 -24.1 1.380 PL 182.33 PF 9.1 52 32.0 0.0 88.7 0.0 5.2 120 FTG T PE 0.0 53 32.0 0.0 97.9 0.0 0.048 TL 188.33 PV Pipe: 51 -24.1 1.610 PL 2.00 FE' 0.2 53 32.0 0.0 97.9 0.0 3.8 120 FTG T FE 0.9 54 30.0 0.0 99.0 0.0 0.023 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/11/2016RAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 24.1 1.610 PL 2.00 PP 0.2 55 32.0 0.0 76.2 0.0 3.8 120 FTG T PE 0.9 56 30.0 0.0 76.9 0.0 0.023 TL 10.00 PV Pipe: 53 -24.1 1.380 PL 38.17 PF 1.9 55 32.0 0.0 76.2 0.0 5.2 120 FTG L PE 0.0 57 32.0 0.0 78.2 0.0 0.048 TL 40.17 PV Pipe: 54 -24.1 1.380 PL 134.70 PP 6.5 57 32.0 0.0 78.2 0.0 5.2 120 FTG ---- PE 0.0 59 32.0 0.0 84.7 0.0 0.048 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 86.0 0.0 0.0 120 FTG ---- FE -1.3 59 32.0 0.0 84.7 0.0 0.000 TL 35.00 PV Pipe: 56 -24.1 1.380 FL 12.50 PP 0.6 59 32.0 0.0 84.7 0.0 5.2 120 FTC ---- FE 0.0 60 32.0 0.0 85.3 0.0 0.048 TL 12.50 PV Pipe: 57 -24.1 1.380 PL 1.83 PP 0.1 60 32.0 0.0 85.3 0.0 5.2 120 FTG ---- PE 0.0 62 32.0 0.0 85.4 0.0 0.048 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PP 0.0 61 29.0 0.0 86.7 0.0 0.0 120 FTG ---- PE -1.3 62 32.0 0.0 85.4 0.0 0.000 TL 35.00 PV Pipe: 59 -24.1 1.380 PL 9.25 PP 0.4 62 32.0 0.0 85.4 0.0 5.2 120 FTG ---- FE 0.0 64 32.0 0.0 85.8 0.0 0.048 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PF 0.0 63 29.0 0.0 87.1 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 85.8 0.0 0.000 TL 35.00 PV Pipe: 61 -24.1 1.380 PL 0.92 PF 0.0 64 32.0 0.0 85.8 0.0 5.2 120 FTG ---- PE 0.0 65 32.0 0.0 85.8 0.0 0.048 TL 0.92 PV Pipe: 62 -24.1 1.380 FL 12.00 PF 0.6 65 32.0 0.0 85.8 0.0 5.2 120 FTG ---- FE 0.0 66 32.0 0.0 86.4 0.0 0.048 TL 12.00 PV Pipe: 63 -24.1 1.380 PL 1.42 PP 0.1 66 32.0 0.0 86.4 0.0 5.2 120 FTG ---- FE 0.0 68 32.0 0.0 86.5 0.0 0.048 TL 1.42 PV Pipe: 64 0.0 1.049 FL 35.00 PP 0.0 67 29.0 0.0 87.8 0.0 0.0 120 FTG ---- FE -1.3 68 32.0 0.0 86.5 0.0 0.000 TL 35.00 PV ci SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Cab 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -24.1 1.380 PL 9.17 PF 0.4 68 32.0 0.0 86.5 0.0 5.2 120 FTG ---- PE 0.0 70 32.0 0.0 86.9 0.0 0.048 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 88.2 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 86.9 0.0 0.000 TL 35.00 PV Pipe: 67 -24.1 1.380 PL 1.25 PF 0.1 70 32.0 0.0 86.9 0.0 5.2 120 FTG ---- PE 0.0 71 32.0 0.0 87.0 0.0 0.048 TL 1.25 PV Pipe: 68 -24.1 1.380 PL 30.80 PF 1.9 71 32.0 0.0 87.0 0.0 5.2 120 FTG ET PE 0.0 72 32.0 0.0 88.9 0.0 0.048 TL 39.80 PV Pipe: 69 -24.1 1.380 PL 175.00 PF 8.7 72 32.0 0.0 88.9 0.0 5.2 120 FTG T PE 0.0 73 32.0 0.0 97.6 0.0 0.048 TL 181.00 PV Pipe: 70 -24.1 1.610 PL 2.00 PF 0.2 73 32.0 0.0 97.6 0.0 3.8 120 FTG T PE 0.9 74 30.0 0.0 98.7 0.0 0.023 TL 10.00 PV Pipe: 71 24.1 1.610 PL 2.00 PF 0.2 75 32.0 0.0 76.3 0.0 3.8 120 FTG T PE 0.9 76 30.0 0.0 77.0 0.0 0.023 TL 10.00 PV Pipe: 72 -24.1 1.380 PL 38.25 PF 1.9 75 32.0 0.0 76.3 0.0 5.2 120 FTG L PE 0.0 77 32.0 0.0 78.3 0.0 0.048 TL 40.25 PV Pipe: 73 -24.1 1.380 PL 150.42 PF 7.2 77 32.0 0.0 78.3 0.0 5.2 120 FTG ---- PE 0.0 78 32.0 0.0 85.5 0.0 0.048 TL 150.42 By Pipe: 74 -24.1 1.380 PL 65.83 PF 3.5 78 32.0 0.0 85.5 0.0 5.2 120 FTG 2E PE 0.0 79 32.0 0.0 89.0 0.0 0.048 TL 71.83 PV Pipe: 75 -24.1 1.380 PL 170.83 PF 8.5 79 32.0 0.0 89.0 0.0 5.2 120 FTG T PE 0.0 80 32.0 0.0 97.5 0.0 0.048 TL 176.83 PV Pipe: 76 -24.1 1.610 PL 2.00 PF 0.2 80 32.0 0.0 97.5 0.0 3.8 120 FTG T PE 0.9 81 30.0 0.0 98.6 0.0 0.023 TL 10.00 PV Pipe: 77 24.1 1.610 PL 2.00 PF 0.2 82 32.0 0.0 76.4 0.0 3.8 120 FTG T PE 0.9 83 30.0 0.0 77.0 0.0 0.023 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic S - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -24.1 1.380 PL 24.58 PF 1.3 82 32.0 0.0 76.4 0.0 5.2 120 FTG L PE 0.0 84 32.0 0.0 77.7 0.0 0.048 TL 26.58 PV Pipe: 79 -24.1 1.380 PL 190.50 PF 9.8 84 32.0 0.0 77.7 0.0 5.2 120 FTG 4E PE 0.0 85 32.0 0.0 87.5 0.0 0.048 TL 202.50 PV Pipe: 80 -24.1 1.380 PL 196.21 PF 9.8 85 32.0 0.0 87.5 0.0 5.2 120 FTG T PE 0.0 86 32.0 0.0 97.3 0.0 0.048 TL 202.21 PV Pipe: 81 -24.1 1.380 PL 2.00 PF 0.4 86 32.0 0.0 97.3 0.0 5.2 120 FTG T PE 0.9 87 30.0 0.0 98.5 0.0 0.048 TL 8.00 PV Pipe: 82 23.6 1.610 PL 3.50 PF 0.3 88 33.5 0.0 75.8 0.0 3.7 120 FTG T PE 1.5 89 30.0 0.0 77.0 0.0 0.022 TL 11.50 PV Pipe: 83 -23.6 1.380 PL 33.58 PF 1.6 88 33.5 0.0 75.8 0.0 5.1 120 FTG L PE 0.0 90 33.5 0.0 77.4 0.0 0.046 TL 35.58 PV Pipe: 84 -23.6 1.380 PL 202.38 PF 10.1 90 33.5 0.0 77.4 0.0 5.1 120 FTG 3ET PE 0.0 91 33.5 0.0 87.5 0.0 0.046 TL 217.38 PV Pipe: 85 -23.6 1.380 PL 193.96 PF 9.3 91 33.5 0.0 87.5 0.0 5.1 120 FTG T PE 0.0 92 33.5 0.0 96.8 0.0 0.046 TL 199.96 PV Pipe: 86 -23.6 1.610 PL 3.50 PF 0.3 92 33.5 0.0 96.8 0.0 3.7 120 FTG T PE 1.5 93 30.0 0.0 98.5 0.0 0.022 TL 11.50 PV Pipe: 87 -22.5 2.635 PL 3.00 PF 0.0 11 30.0 0.0 76.3 0.0 1.3 120 FTG ---- PE 0.0 33 30.0 0.0 76.3 0.0 0.002 TL 3.00 PV Pipe: 88 -120.0 2.635 PL 8.50 PF 0.3 33 30.0 0.0 76.3 0.0 7.1 120 FTG ---- PE 0.0 45 30.0 0.0 76.7 0.0 0.040 TL 8.50 PV Pipe: 89 -95.8 2.635 PL 6.92 PF 0.2 45 30.0 0.0 76.7 0.0 5.6 120 FTG ---- PE 0.0 56 30.0 0.0 76.9 0.0 0.027 TL 6.92 PV Pipe: 90 -71.8 2.635 PL 7.42 PF 0.1 56 30.0 0.0 76.9 0.0 4.2 120 FTG ---- PE 0.0 76 30.0 0.0 77.0 0.0 0.016 TL 7.42 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 1 -47.7 2.635 FL 7.00 PF 0.1 76 30.0 0.0 77.0 0.0 2.8 120 FTG ---- PE 0.0 83 30.0 0.0 77.0 0.0 0.007 TL 7.00 FV Pipe: 92 -23.6 2.635 PL 3.02 PF 0.0 83 30.0 0.0 77.0 0.0 1.4 120 FTG ---- FE 0.0 89 30.0 0.0 77.0 0.0 0.002 TL 3.92 PV Pipe: 93 -23.1 2.635 PL 5.54 PF 0.0 23 30.0 0.0 99.5 0.0 1.4 120 FTG ---- FE 0.0 43 30.0 0.0 99.5 0.0 0.002 TL 5.54 PV Pipe: 94 -48.8 2.635 FL 8.96 PF 0.2 43 30.0 0.0 99.5 0.0 2.9 120 FTG T PE 0.0 94 30.0 0.0 99.7 0.0 0.008 TL 25.96 PV Pipe: 95 -23.6 2..635 FL 5.40 PF 0.0 93 30.0 0.0 98.5 0.0 1.4 120 FTG ---- FE 0.0 87 30.0 0.0 98.5 0.0 0.002 TL 5.40 PV Pipe: 96 -47.7 2.635 FL 9.50 PF 0.1 87 30.0 0.0 98.5 0.0 2.8 120 FTG ---- FE 0.0 81 30.0 0.0 98.6 0.0 0.007 TL 9.50 PV Pipe: 97 -71.8 2.635 PL 8.17 FE' 0.1 81 30.0 0.0 98.6 0.0 4.2 120 FTG ---- FE 0.0 74 30.0 0.0 98.7 0.0 0.016 TL 8.17 PV Pipe: 98 -95.8 2.635 FL 7.96 PF 0.2 74 30.0 0.0 98.7 0.0 5.6 120 FTG ---- PE 0.0 54 30.0 0.0 99.0 0.0 0.027 TL 7.96 PV Pipe: 99 -120.0 2.635 FL 1.04 PF 0.7 54 30.0 0.0 99.0 0.0 7.1 120 FTG T FE 0.0 94 30.0 0.0 99.7 0.0 0.040 TL 18.04 PV Pipe: 100 -168.8 2.635 FL 20.38 PF 2.8 94 30.0 0.0 99.7 0.0 9.9 120 FTG 2E FE 0.0 95 30.0 0.0 102.4 0.0 0.076 TL 36.38 PV Pipe: 101 -168.8 2.635 FL 75.50 PF 8.8 95 30.0 0.0 102.4 0.0 9.9 120 FTG 5E FE 12.8 BOR 0.5 0.0 124.0 0.0 0.076 TL 115.50 PV Pipe: 102 -168.8 6.280 FL 10.00 FE' 0.0 BOR 0.5 0.0 124.0 0.0 1.7 140 FTG E FE 1.5 UG3 -3.0 0.0 125.5 0.0 0.001 TL 32.00 PV Pipe: 103 -168.8 6.080 FL 142.00 PF 0.2 UG3 -3.0 0.0 125.5 0.0 1.9 150 FTG 3E FE 0.0 UG2 -3.0 0.0 125.7 0.0 0.001 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -168.8 6.280 PL 5.00 PF 0.1 UG2 -3.0 0.0 125.7 0.0 1.7 140 FTG ET FE -2.2 BF2 2.0 0.0 123.6 0.0 0.001 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 127.6 0.0 4.0 psi, 168.8 gpm BF2 2.0 0.0 123.6 0.0 Pipe: 106 -168.8 6.280 PL 5.00 PF 0.0 BF1 2.0 0.0 127.6 0.0 1.7 140 FTG 2E PE 2.2 UG1 -3.0 0.0 129.8 0.0 0.001 TL 49.00 PV Pipe: 107 -168.8 6.080 PL 16.00 FE 0.1 UG1 -3.0 0.0 129.8 0.0 1.9 150 FTG TQ FE 0.0 SRC -3.0 SRCE 129.9 (N/A) 0.001 TL 67.00 PV NOTES (HASS) Calculations were performed by the MASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.137 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 19.4 ft/sec at pipe 30. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.80 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 11½ WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm LEGEND 1 =Availab1e pressure 154.82 psi 8 268.8 gpm- 2 Required pressure 129.86 psi 8 268.8 gpm lA Avail. OnSite Demand Press 154.82 psi 8 168.8 gpm 2A Req. OnSite Demand Press. 129.86 psi 8 168.8 gpm A. Source Supply Curve System Demand Curve Available at Source 140.0 21½ G A U120. 0 G E P100 . 0 R E S S 80.0 U R E p S 40.0 20.0 B 0.0 -14.7 400 600 800 1000 1200 1400 FLOW (GPM) thed Lines indicate extrapolated values from Test Results 1600 1800 2000 - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 10/11/2016RAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 WATER SUPPLY CURVE I \\\\\\\\\\\\\\\\\\\\\\\\\\ 149.0 psi 8 1790 gpm-> * I Flow Test Point 143+ 130+ X 117+ P104+ R I E I S I S 91+ U I R E 78+ P S I I 65+ 52+ 39+ 26+ LEGEND 'p I X = Required Water Supply 129.86 psi @ 268.8 gpm 13+ I 0 = Available Water Supply I 154.82 psi 8 268.8 gpm 'p +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.7 352.7 93.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 352.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 252.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 23.4 - - - 2 30.0 - - - - 23.0 - - - 3 33.5 - - - - 21.5 - - - 4 33.5 - - - - 21.5 - - - 5 29.0 - - - - 23.4 - - - 6 30.0 - - - - 23.0 - - - 7 33.5 - - - - 21.5 8 33.5 - - - - 21.5 - - - 9 33.5 - - - - 21.5 10 33.5 - - - - 21.5 - - - 11 30.0 - - - - 22.5 - - - 12 33.5 - - - - 21.9 - - - 13 33.5 - - - - 22.1 14 33.5 - - - - 23.8 - - - 15 33.5 - - - - 24.6 - - - 16 33.5 - - - - 34.3 - - - 17 33.5 - - - - 34.6 - - - 18 33.5 - - - - 34.9 - - - 19 33.5 - - - - 35.2 - - - 20 33.5 - - - - 35.5 21 33.5 - - - - 37.2 - - - 22 33.5 - - - - 47.7 - - - 23 30.0 - - - - 49.7 - - - 24 29.0 - - - - 22.4 - - - 25 30.0 - - - - 22.0 - - - 26 29.0 - - - - 22.4 - - - 27 30.0 - - - - 22.0 - - - 28 29.0 - - - - 22.4 - - - 29 30.0 - - - - 22.0 - - - 30 32.0 - - - - 21.1 - - - 31 32.0 - - - - 21.1 - - - 32 32.0 - - - - 21.1 - - - 33 30.0 - - - - 22.5 - - - 34 32.0 - - - - 17.6 - - - 35 32.0 - - - - 8.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 32.0 K= 5.60 7.3 15.2 37 32.0 K= 5.60 7.2 15.0 38 32.0 K= 5.60 7.0 14.8 39 32.0 K= 5.60 7.2 15.0 40 32.0 K= 5.60 8.0 15.8 41 32.0 - - - - 16.1 - - - 42 32.0 - - - - 47.5 - - - 43 30.0 - - - 49.7 - - - 44 32.0 - - - - 21.6 - - - 45 30.0 - - - - 22.5 - - - 46 32.0 - - - - 18.1 - - - 47 32.0 K= 5.60 7.6 15.4 48 32.0 K= 5.60 7.4 15.2 49 32.0 K= 5.60 7.4 15.2 50 32.0 K= 5.60 7.6 15.5 51 32.0 K= 5.60 8.4 16.2 52 32.0 - - - - 14.2 - - - 53 32.0 - - - - 46.4 - - - 54 30.0 - - - - 48.6 - - - 55 32.0 - - - 21.2 - - - 56 30.0 - - - - 22.5 - - - 57 32.0 - - - - 18.8 - - - 58 29.0 - - - - 12.3 - - - 59 32.0 - - - - 11.0 - - - 60 32.0 K= 5.60 10.3 18.0 61 29.0 - - - - 11.6 - - - 62 32.0 - - - - 10.3 - - - 63 29.0 - - - - 11.5 - - - 64 32.0 - - - - 10.2 - - - 65 32.0 K= 5.60 10.2 17.9 66 32.0 K= 5.60 10.3 18.0 67 29.0 - - - - 11.7 - - - 68 32.0 - - - - 10.4 - - - 69 29.0 - - - - 12.3 - - - 70 32.0 -- - - - 11.0 - - - 71 32.0 K= 5.60 11.0 18.6 72 32.0 - - - - 17.4 - - - 73 32.0 - - - - 46.1 - - - 74 30.0 - - - - 48.2 - - - 75 32.0 - - - - 21.8 - - - 76 30.0 - - - - 22.6 - - - 77 32.0 - - - - 22.0 - - - 78 32.0 K= 5.60 22.9 26.8 79 32.0 - - - - 29.7 - - - 80 32.0 - - - 46.4 - - - 81 30.0 - - - - 48.0 - - - 82 32.0 - - - - 22.2 - - - 83 30.0 - - - - 22.6 - - - 84 32.0 - - - - 23.7 - - - 85 32.0 - - - - 35.2 - - - 86 32.0 - - - - 46.6 - - - 87 30.0 - - - - 48.0 - - - 88 33.5 - - - - 21.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 89 30.0 - - - - 22.7 - - - 90 33.5 - - - - 23.6 - - - 91 33.5 - - - - 35.2 - - - 92 33.5 - - - - 45.9 - - - 93 30.0 - - - - 48.0 - - - 94 30.0 - - - - 50.1 - - - 95 30.0 - - - - 56.0 - - - BOR 0.5 - - - - 87.2 UG3 -3.0 - - - - 88.8 - - - UG2 -3.0 - - - - 89.2 - - - BF2 2.0 - - - - 87.1 - - - BF1 2.0 - - - - 91.1 - - - UG1 -3.0 - - - - 93.4 - - - SRC -3.0 SOURCE 93.5 252.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 23.4 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 23.0 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 23.0 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 21.5 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 0.0 21.5 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 PL 2.21 PF 0.0 4 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 7 33.5 0.0 21.5 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 23.4 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 23.0 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 PF 0.0 6 30.0 0.0 23.0 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 21.5 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 PF 0.0 7 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 8 33.5 0.0 21.5 0.0 0.000 TL 1.75 PV Pipe: 8 0.0 1.380 PL 4.00 PF 0.0 8 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 9 33.5 0.0 21.5 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 PL 0.83 PF 0.0 9 33.5 0.0 21.5 0.0 0.0 120 FTG T PE 0.0 10 33.5 0.0 21.5 0.0 0.000 TL 6.83 PV Pipe: 10 24.7 1.380 PL 3.50 PF 0.5 10 33.5 0.0 21.5 0.0 5.3 120 FTG T PE 1.5 11 30.0 0.0 22.5 0.0 0.051 TL 9.50 PV Pipe: 11 -24.7 1.380 PL 3.17 PF 0.5 10 33.5 0.0 21.5 0.0 5.3 120 FTG T PE 0.0 12 33.5 0.0 21.9 0.0 0.051 TL 9.17 PV Pipe: 12 -24.7 1.380 PL 4.00 PF 0.2 12 33.5 0.0 21.9 0.0 5.3 120 FTG ---- PE 0.0 13 33.5 0.0 22.1 0.0 0.051 TL 4.00 PV Pipe: 13 -24.7 1.380 PL 30.25 PF 1.6 13 33.5 0.0 22.1 0.0 5.3 120 FTG L PE 0.0 14 33.5 0.0 23.8 0.0 0.051 TL 32.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 -24.7 1.380 PL 10.42 PP 0.8 14 33.5 0.0 23.8 0.0 5.3 120 FTG T PE 0.0 15 33.5 0.0 24.6 0.0 0.051 TL 16.42 PV Pipe: 15 -24.7 1.380 PL 177.46 PP 9.7 15 33.5 0.0 24.6 0.0 5.3 120 FTG 3ET PE 0.0 16 33.5 0.0 34.3 0.0 0.051 TL 192.46 PV Pipe: 16 -24.7 1.380 PL 6.00 PP 0.3 16 33.5 0.0 34.3 0.0 5.3 120 FTG ---- PE 0.0 17 33.5 0.0 34.6 0.0 0.051 TL 6.00 PV Pipe: 17 -24.7 1.380 PL 6.00 PP 0.3 17 33.5 0.0 34.6 0.0 5.3 120 FTG ---- PE 0.0 18 33.5 0.0 34.9 0.0 0.051 TL 6.00 PV Pipe: 18 -24.7 1.380 PL 6.00 PP 0.3 18 33.5 0.0 34.9 0.0 5.3 120 FTG ---- PE 0.0 19 33.5 0.0 35.2 0.0 0.051 TL 6.00 PV Pipe: 19 -24.7 1.380 PL 6.00 PP 0.3 19 33.5 0.0 35.2 0.0 5.3 120 FTG ---- PE 0.0 20 33.5 0.0 35.5 0.0 0.051 TL 6.00 PV Pipe: 20 -24.7 1.380 PL 26.42 PF 1.6 20 33.5 0.0 35.5 0.0 5.3 120 FTG 2E PE 0.0 21 33.5 0.0 37.2 0.0 0.051 TL 32.42 PV Pipe: 21 -24.7 1.380 PL 189.96 PF 10.5 21 33.5 0.0 37.2 0.0 5.3 120 FTG 4ET PE 0.0 22 33.5 0.0 47.7 0.0 0.051 TL 207.96 PV Pipe: 22 -24.7 1.380 PL 3.50 PP 0.5 22 33.5 0.0 47.7 0.0 5.3 120 FTG T PE 1.5 23 30.0 0.0 49.7 0.0 0.051 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PP 0.0 24 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PP 0.0 25 30.0 0.0 22.0 0.0 0.0 120 FTG ---- PE 0.0 27 30.0 0.0 22.0 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PF 0.0 26 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 27 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 26 0.0 1.380 PL 3.50 PF 0.0 27 30.0 0.0 22.0 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 22.0 0.0 0.000 TL 3.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 27 0.0 1.049 PL 35.00 PF 0.0 28 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 22.0 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 21.1 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PF 0.0 30 32.0 0.0 21.1 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 21.1 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PF 0.0 31 32.0 0.0 21.1 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 21.1 0.0 0.000 TL 6.96 PV Pipe: 31 -27.7 1.380 PL 2.00 PF 0.5 32 32.0 0.0 21.1 0.0 6.0 120 FTG T PE 0.9 33 30.0 0.0 22.5 0.0 0.063 TL 8.00 PV Pipe: 32 27.7 1.380 PL 47.58 PF 3.5 32 32.0 0.0 21.1 0.0 6.0 120 FTG TL PE 0.0 34 32.0 0.0 17.6 0.0 0.063 TL 55.58 PV Pipe: 33 27.7 1.380 PL 138.50 PF 9.2 34 32.0 0.0 17.6 0.0 6.0 120 FTG 3E PE 0.0 35 32.0 0.0 8.4 0.0 0.063 TL 147.50 PV Pipe: 34 27.7 1.380 PL 14.00 PF 1.1 35 32.0 0.0 8.4 0.0 6.0 120 FTG E PE 0.0 36 32.0 5.6 7.3 15.2 0.063 TL 17.00 By Pipe: 35 12.6 1.380 PL 10.00 PF 0.1 36 32.0 5.6 7.3 15.2 2.7 120 FTG ---- BE 0.0 37 32.0 5.6 7.2 15.0 0.015 TL 10.00 By Pipe: 36 -2.4 1.380 PL 8.00 PF 0.0 37 32.0 5.6 7.2 15.0 0.5 120 FTG ---- PE 0.0 39 32.0 5.6 7.2 15.0 0.001 TL 8.00 PV Pipe: 37 -14.8 1.380 PL 10.00 PF 0.2 38 32.0 5.6 7.0 14.8 3.2 120 FTG ---- BE 0.0 39 32.0 5.6 7.2 15.0 0.020 TL 10.00 By Pipe: 38 -32.2 1.380 PL 10.00 PF 0.8 39 32.0 5.6 7.2 15.0 6.9 120 FTG ---- PE 0.0 40 32.0 5.6 8.0 15.8 0.083 TL 10.00 PV Pipe: 39 -48.1 1.380 PL 34.67 PF 8.1 40 32.0 5.6 8.0 15.8 10.3 120 FTG 4E BE 0.0 41 32.0 0.0 16.1 0.0 0.173 TL 46.67 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 40 -48.1 1.380 PL 175.12 PF 31.4 41 32.0 0.0 16.1 0.0 10.3 120 FTG T PE 0.0 42 32.0 0.0 47.5 0.0 0.173 TL 181.12 PV Pipe: 41 -48.1 1.380 PL 2.00 PF 1.4 42 32.0 0.0 47.5 0.0 10.3 120 FTG T PE 0.9 43 30.0 0.0 49.7 0.0 0.173 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 21.6 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 22.5 0.0 0.000 TL 8.00 PV Pipe: 43 29.9 1.380 PL 41.25 PF 3.6 45 30.0 0.0 22.5 0.0 6.4 120 FTG TL PE -0.9 46 32.0 0.0 18.1 0.0 0.072 TL 49.25 PV Pipe: 44 29.9 1.380 PL 145.04 PF 10.5 46 32.0 0.0 18.1 0.0 6.4 120 FTG ---- PE 0.0 47 32.0 5.6 7.6 15.4 0.072 TL 145.04 PV Pipe: 45 14.5 1.380 PL 10.00 PF 0.2 47 32.0 5.6 7.6 15.4 3.1 120 FTG ---- PE 0.0 48 32.0 5.6 7.4 15.2 0.019 TL 10.00 PV Pipe: 46 -0.7 1.380 PL 8.00 PF 0.0 48 32.0 5.6 7.4 15.2 0.2 120 FTG ---- PE 0.0 49 32.0 5.6 7.4 15.2 0.000 TL 8.00 PV Pipe: 47 -16.0 1.380 PL 10.00 PF 0.2 49 32.0 5.6 7.4 15.2 3.4 120 FTG ---- PE 0.0 50 32.0 5.6 7.6 15.5 0.023 TL 10.00 PV Pipe: 48 -31.4 1.380 PL 10.00 PF 0.8 50 32.0 5.6 7.6 15.5 6.7 120 FTG ---- PE 0.0 51 32.0 5.6 8.4 16.2 0.079 TL 10.00 PV Pipe: 49 -47.7 1.380 PL 27.96 PF 5.8 51 32.0 5.6 8.4 16.2 10.2 120 FTG 2E PE 0.0 52 32.0 0.0 14.2 0.0 0.171 TL 33.96 PV Pipe: 50 -47.7 1.380 PL 182.33 PF 32.2 52 32.0 0.0 14.2 0.0 10.2 120 FTG T PE 0.0 53 32.0 0.0 46.4 0.0 0.171 TL 188.33 PV Pipe: 51 -47.7 1.380 PL 2.00 PF 1.4 53 32.0 0.0 46.4 0.0 10.2 120 FTG T PE 0.9 54 30.0 0.0 48.6 0.0 0.171 TL 8.00 PV Pipe: 52 -26.6 1.380 PL 2.00 PF 0.5 55 32.0 0.0 21.2 0.0 5.7 120 FTG T PE 0.9 56 30.0 0.0 22.5 0.0 0.058 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 26.6 1.380 PL 38.17 PF 2.3 55 32.0 0.0 21.2 0.0 5.7 120 FTG L PE 0.0 57 32.0 0.0 18.8 0.0 0.058 TL 40.17 PV Pipe: 54 26.6 1.380 PL 134.70 PF 7.8 57 32.0 0.0 18.8 0.0 5.7 120 FTG ---- PE 0.0 59 32.0 0.0 11.0 0.0 0.058 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 12.3 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 11.0 0.0 0.000 TL 35.00 PV Pipe: 56 26.6 1.380 PL 12.50 PF 0.7 59 32.0 0.0 11.0 0.0 5.7 120 FTG ---- PE 0.0 60 32.0 5.6 10.3 18.0 0.058 TL 12.50 PV Pipe: 57 8.6 1.380 PL 1.83 PF 0.0 60 32.0 5.6 10.3 18.0 1.9 120 FTG ---- PE 0.0 62 32.0 0.0 10.3 0.0 0.007 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PF 0.0 61 29.0 0.0 11.6 0.0 0.0 120 FTG ---- PE -1.3 62 32.0 0.0 10.3 0.0 0.000 TL 35.00 PV Pipe: 59 8.6 1.380 PL 9.25 PF 0.1 62 32.0 0.0 10.3 0.0 1.9 120 FTG ---- PE 0.0 64 32.0 0.0 10.2 0.0 0.007 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PF 0.0 63 29.0 0.0 11.5 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 10.2 0.0 0.000 TL 35.00 PV Pipe: 61 8.6 1.380 FL 0.92 PF 0.0 64 32.0 0.0 10.2 0.0 1.9 120 FTG ---- PE 0.0 65 32.0 5.6 10.2 17.9 0.007 TL 0.92 PV Pipe: 62 -9.3 1.380 PL 12.00 FE' 0.1 65 32.0 5.6 10.2 17.9 2.0 120 FTG ---- PE 0.0 66 32.0 5.6 10.3 18.0 0.008 TL 12.00 PV Pipe: 63 -27.2 1.380 PL 1.42 PF 0.1 66 32.0 5.6 10.3 18.0 5.8 120 FTG ---- FE 0.0 68 32.0 0.0 10.4 0.0 0.061 TL 1.42 PV Pipe: 64 0.0 1.049 FL 35.00 PF 0.0 67 29.0 0.0 11.7 0.0 0.0 120 FTG ---- PE -1.3 68 32.0 0.0 10.4 0.0 0.000 TL 35.00 PV Pipe: 65 -27.2 1.380 PL 9.17 PF 0.6 68 32.0 0.0 10.4 0.0 5.8 120 FTG ---- PE 0.0 70 32.0 0.0 11.0 0.0 0.061 TL 9.17 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) I-iW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 12.3 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 11.0 0.0 0.000 TL 35.00 PV Pipe: 67 -27.2 1.380 PL 1.25 PF 0.1 70 32.0 0.0 11.0 0.0 5.8 120 FTG ---- FE 0.0 71 32.0 5.6 11.0 18.6 0.061 TL 1.25 PV Pipe: 68 -45.8 1.380 PL 30.80 PF 6.3 71 32.0 5.6 11.0 18.6 9.8 120 FTG ET PE 0.0 72 32.0 0.0 17.4 0.0 0.159 TL 39.80 PV Pipe: 69 -45.8 1.380 PL 175.00 PP 28.7 72 32.0 0.0 17.4 0.0 9.8 120 FTG T PE 0.0 73 32.0 0.0 46.1 0.0 0.159 TL 181.00 PV Pipe: 70 -45.8 1.380 PL 2.00 PP 1.3 73 32.0 0.0 46.1 0.0 9.8 120 FTG T PE 0.9 74 30.0 0.0 48.2 0.0 0.159 TL 8.00 PV Pipe: 71 7.8 1.380 FL 2.00 PP 0.0 75 32.0 0.0 21.8 0.0 1.7 120 FTG T PE 0.9 76 30.0 0.0 22.6 0.0 0.006 TL 8.00 PV Pipe: 72 -7.8 1.380 FL 38.25 PP 0.2 75 32.0 0.0 21.8 0.0 1.7 120 FTG L PE 0.0 77 32.0 0.0 22.0 0.0 0.006 TL 40.25 PV Pipe: 73 -7.8 1.380 PL 150.42 PP 0.9 77 32.0 0.0 22.0 0.0 1.7 120 FTG ---- PE 0.0 78 32.0 5.6 22.9 26.8 0.006 TL 150.42 PV Pipe: 74 -34.6 1.380 PL 65.83 PF 6.8 78 32.0 5.6 22.9 26.8 7.4 120 FTG 2E PE 0.0 79 32.0 0.0 29.7 0.0 0.095 TL 71.83 PV Pipe: 75 -34.6 1.380 FL 170.83 PF 16.7 79 32.0 0.0 29.7 0.0 7.4 120 FTG T PE 0.0 80 32.0 0.0 46.4 0.0 0.095 TL 176.83 PV Pipe: 76 -34.6 1.380 PL 2.00 PP 0.8 80 32.0 0.0 46.4 0.0 7.4 120 FTG T FE 0.9 81 30.0 0.0 48.0 0.0 0.095 TL 8.00 PV Pipe: 77 26.3 1.380 PL 2.00 PF 0.5 82 32.0 0.0 22.2 0.0 5.6 120 FTG T PE 0.9 83 30.0 0.0 22.6 0.0 0.057 TL 8.00 PV Pipe: 78 -26.3 1.380 PL 24.58 PF 1.5 82 32.0 0.0 22.2 0.0 5.6 120 FTG L FE 0.0 84 32.0 0.0 23.7 0.0 0.057 TL 26.58 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 79 -26.3 1.380 PL 190.50 PF 11.5 84 32.0 0.0 23.7 0.0 5.6 120 FTG 4E PE 0.0 85 32.0 0.0 35.2 0.0 0.057 TL 202.50 PV Pipe: 80 -26.3 1.380 PL 196.21 PF 11.4 85 32.0 0.0 35.2 0.0 5.6 120 FTG T PE 0.0 86 32.0 0.0 46.6 0.0 0.057 TL 202.21 PV Pipe: 81 -26.3 1.380 FL 2.00 PF 0.5 86 32.0 0.0 46.6 0.0 5.6 120 FTG T FE 0.9 87 30.0 0.0 48.0 0.0 0.057 TL 8.00 PV Pipe: 82 25.5 1.380 FL 3.50 PF 0.5 88 33.5 0.0 21.7 0.0 5.5 120 FTG T PE 1.5 89 30.0 0.0 22.7 0.0 0.054 TL 9.50 PV Pipe: 83 -25.5 1.380 PL 33.58 PF 1.9 88 33.5 0.0 21.7 0.0 5.5 120 FTG L PE 0.0 90 33.5 0.0 23.6 0.0 0.054 TL 35.58 PV Pipe: 84 -25.5 1.380 FL 202.38 PF 11.7 90 33.5 0.0 23.6 0.0 5.5 120 FTG 3ET FE 0.0 91 33.5 0.0 35.2 0.0 0.054 TL 217.38 PV Pipe: 85 -25.5 1.380 FL 193.96 PF 10.7 91 33.5 0.0 35.2 0.0 5.5 120 FTG T PE 0.0 92 33.5 0.0 45.9 0.0 0.054 TL 199.96 PV Pipe: 86 -25.5 1.380 FL 3.50 PP 0.5 92 33.5 0.0 45.9 0.0 5.5 120 FTG T FE 1.5 93 30.0 0.0 48.0 0.0 0.054 TL 9.50 PV Pipe: 87 24.7 2.635 FL 3.00 PP 0.0 11 30.0 0.0 22.5 0.0 1.5 120 FTG ---- PE 0.0 33 30.0 0.0 22.5 0.0 0.002 TL 3.00 PV Pipe: 88 -3.0 2.635 PL 8.50 PP 0.0 33 30.0 0.0 22.5 0.0 0.2 120 FTG ---- PE 0.0 45 30.0 0.0 22.5 0.0 0.000 TL 8.50 PV Pipe: 89 -33.0 2.635 FL 6.92 PP 0.0 45 30.0 0.0 22.5 0.0 1.9 120 FTG ---- PE 0.0 56 30.0 0.0 22.5 0.0 0.004 TL 6.92 PV Pipe: 90 -59.6 2.635 FL 7.42 PP 0.1 56 30.0 0.0 22.5 0.0 3.5 120 FTG ---- FE 0.0 76 30.0 0.0 22.6 0.0 0.011 TL 7.42 PV Pipe: 91 -51.7 2.635 FL 7.00 PP 0.1 76 30.0 0.0 22.6 0.0 3.0 120 FTG ---- FE 0.0 83 30.0 0.0 22.6 0.0 0.009 TL 7.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 92 -25.5 2.635 PL 3.92 PP 0.0 83 30.0 0.0 22.6 0.0 1.5 120 FTG ---- PE 0.0 89 30.0 0.0 22.7 0.0 0.002 TL 3.92 PV Pipe: 93 -24.7 2.635 PL 5.54 PP 0.0 23 30.0 0.0 49.7 0.0 1.5 120 FTG ---- PE 0.0 43 30.0 0.0 49.7 0.0 0.002 TL 5.54 PV Pipe: 94 -72.8 2.635 PL 8.96 PP 0.4 43 30.0 0.0 49.7 0.0 4.3 120 FTG T PE 0.0 94 30.0 0.0 50.1 0.0 0.016 TL 25.96 PV Pipe: 95 -25.5 2.635 PL 5.40 PP 0.0 93 30.0 0.0 48.0 0.0 1.5 120 FTG ---- PE 0.0 87 30.0 0.0 48.0 0.0 0.002 TL 5.40 PV Pipe: 96 -51.7 2.635 PL 9.50 PP 0.1 87 30.0 0.0 48.0 0.0 3.0 120 FTG ---- PE 0.0 81 30.0 0.0 48.0 0.0 0.009 TL 9.50 PV Pipe: 97 -86.4 2.635 PL 8.17 PP 0.2 81 30.0 0.0 48.0 0.0 5.1 120 FTG ---- PE 0.0 74 30.0 0.0 48.2 0.0 0.022 TL 8.17 PV Pipe: 98 -132.2 2.635 PL 7.96 PP 0.4 74 30.0 0.0 48.2 0.0 7.8 120 FTG ---- PE 0.0 54 30.0 0.0 48.6 0.0 0.048 TL 7.96 PV Pipe: 99 -179.9 2.635 PL 1.04 PP 1.5 54 30.0 0.0 48.6 0.0 10.6 120 FTG T PE 0.0 94 30.0 0.0 50.1 0.0 0.085 TL 18.04 PV Pipe: 100 -252.7 2.635 PL 20.38 PP 5.8 94 30.0 0.0 50.1 0.0 14.9 120 FTG 2E PE 0.0 95 30.0 0.0 56.0 0.0 0.160 TL 36.38 PV Pipe: 101 -252.7 2.635 PL 75.50 PP 18.5 95 30.0 0.0 56.0 0.0 14.9 120 FTG SE PE 12.8 BOR 0.5 0.0 87.2 0.0 0.160 TL 115.50 PV Pipe: 102 -252.7 6.280 PL 10.00 PP 0.1 BOR 0.5 0.0 87.2 0.0 2.6 140 FTG E PE 1.5 UG3 -3.0 0.0 88.8 0.0 0.002 TL 32.00 PV Pipe: 103 -252.7 6.080 PL 142.00 PP 0.4 UG3 -3.0 0.0 88.8 0.0 2.8 150 FTG 3E PE 0.0 UG2 -3.0 0.0 89.2 0.0 0.002 TL 208.00 PV Pipe: 104 -252.7 6.280 PL 5.00 PP 0.1 UG2 -3.0 0.0 89.2 0.0 2.6 140 FTG ET PE -2.2 BF2 2.0 0.0 87.1 0.0 0.002 TL 74.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 91.1 0.0 4.0 psi, 252.7 gpm BF2 2.0 0.0 87.1 0.0 Pipe: 106 -252.7 6.280 PL 5.00 PF 0.1 BF1 2.0 0.0 91.1 0.0 2.6 140 FTG 2E PE 2.2 UGl -3.0 0.0 93.4 0.0 0.002 TL 49.00 PV Pipe: 107 -252.7 6.080 PL 16.00 PF 0.1 UG1 -3.0 0.0 93.4 0.0 2.8 150 FTG TG PE 0.0 SRC -3.0 SRCE 93.5 (N/A) 0.002 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.169 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.9 ft/sec at pipe 100. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.54 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AimChk DPViv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 140.0 120.0 P100.0 R E S S 80.0 U R E p S i 40.0 20.0 -14.- WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) ished Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights WATER SUPPLY CURVE I \\\\\\\\\\\\\\\\\\\\\\\\\\ I 149.0 psi @ 1790 gpm-> * I Flow Test Point 143+ 130+ 117+ P104+ R E I S IX S 91+ U I R I E 78+ P I S I I 65+ 52+ 39+ 26+ LEGEND I, I X = Required Water Supply I 93.52 psi @ 352.7 gpm 13+ I 0 = Available Water Supply 154.70 psi @ 352.7 gpm +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Cab 2 - SDI ATTIC HEADS WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.9 226.1 123.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 226.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 126.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 91.2 - - - 2 30.0 - - - - 90.8 - - - 3 33.5 - - - - 89.3 - - - 4 33.5 - - - - 89.3 - - - 5 29.0 - - - - 91.2 - - - 6 30.0 - - - - 90.8 - - - 7 33.5 - - - - 89.3 - - - 8 33.5 - - - - 89.3 - - - 9 33.5 - - - - 89.3 - - - 10 33.5 - - - - 89.3 - - - 11 30.0 - - - - 93.4 - - - 12 33.5 - - - - 86.8 - - - 13 33.5 - - - - 85.7 14 33.5 - - - - 77.0 - - - 15 33.5 - - - - 72.6 - - - 16 33.5 K= 5.60 20.6 25.4 17 33.5 K= 5.60 20.0 25.0 18 33.5 K= 5.60 19.9 25.0 19 33.5 K= 5.60 20.0 25.1 20 33.5 K= 5.60 20.8 25.5 21 33.5 - - - - 30.6 - - - 22 33.5 - - - - 93.4 - - - 23 30.0 - - - - 97.8 - - - 24 29.0 - - - - 93.9 - - - 25 30.0 - - - - 93.5 - - - 26 29.0 - - - - 93.9 - - - 27 30.0 - - - - 93.5 - - - 28 29.0 - - - - 93.9 - - - 29 30.0 - - - - 93.5 - - - 30 32.0 - - - - 92.6 - - - 31 32.0 - - - - 92.6 - - - 32 32.0 - - - - 92.6 - - - 33 30.0 - - - - 93.4 - - - 34 32.0 - - - - 93.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 94.5 36 32.0 - - - - 94.6 - - - 37 32.0 - - - - 94.7 - - - 38 32.0 - - - - 94.8 - - - 39 32.0 - - - - 94.8 - - - 40 32.0 - - - - 94.9 - - - 41 32.0 - - - - 95.3 - - - 42 32.0 - - - - 96.9 - - - 43 30.0 - - - - 97.9 - - - 44 32.0 - - - - 92.6 - - - 45 30.0 - - - - 93.5 - - - 46 32.0 - - - - 93.1 - - - 47 32.0 - - - - 94.6 - - - 48 32.0 - - - - 94.7 - - - 49 32.0 - - - - 94.8 - - - 50 32.0 - - - - 94.9 - - - 51 32.0 - - - - 95.0 - - - 52 32.0 - - - - 95.3 - - - 53 32.0 - - - - 97.2 54 30.0 - - - - 98.2 - - - 55 32.0 - - - - 92.7 - - - 56 30.0 - - - - 93.5 - - - 57 32.0 - - - - 93.1 - - - 58 29.0 - - - - 95.8 - - - 59 32.0 - - - - 94.5 - - - 60 32.0 - - - - 94.6 - - - 61 29.0 - - - 95.9 - - - 62 32.0 - - - - 94.6 - - - 63 29.0 - - - - 96.0 - - - 64 32.0 - - - - 94.7 - - - 65 32.0 - - - - 94.7 - - - 66 32.0 - - - - 94.9 - - - 67 29.0 - - - - 96.2 - - 68 32.0 - - - - 94.9 - - - 69 29.0 - - - - 96.3 - - - 70 32.0 - - - - 95.0 - - - 71 32.0 - - - - 95.0 - - - 72 32.0 - - - - 95.4 - - - 73 32.0 - - - - 97.2 - - - 74 30.0 - - - - 98.1 - - - 75 32.0 - - - - 92.8 - - - 76 30.0 - - - - 93.5 - - - 77 32.0 - - - - 93.2 - - - 78 32.0 - - - - 94.7 - - - 79 32.0 - - - - 95.4 - - - 80 32.0 - - - - 97.2 - - - 81 30.0 - - - - 98.1 - - - 82 32.0 - - - - 92.8 - - - 83 30.0 - - - - 93.6 - - - 84 32.0 - - - - 93.0 - - - 85 32.0 - - - - 95.1 - - - 86 32.0 - - - - 97.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 87 30.0 - - - - 98.1 - - - 88 33.5 - - - - 92.1 - - - 89 30.0 - - - - 93.6 - - - 90 33.5 - - - - •92.5 91 33.5 - - - - 94.6 - - - 92 33.5 - - - - 96.5 - - - 93 30.0 - - - - 98.1 - - - 94 30.0 - - - - 98.3 95 30.0 - - - - 99.9 BOR 0.5 - - - - 117.8 - - - UG3 -3.0 - - - - 119.3 - - - UG2 -3.0 - - - - 119.4 - - - BF2 2.0 - - - - 117.3 - - - BF1 2.0 - - - - 121.3 - - - UG1 -3.0 - - - - 123.5 - - - SRC -3.0 SOURCE 123.5 126.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SDI ATTIC HEADS PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PP 0.0 1 29.0 0.0 91.2 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 90.8 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 90.8 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 89.3 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PP 0.0 3 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 0.0 89.3 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 PL 2.21 PF 0.0 4 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 7 33.5 0.0 89.3 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 91.2 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 90.8 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 PP 0.0 6 30.0 0.0 90.8 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 89.3 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 PP 0.0 7 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 8 33.5 0.0 89.3 0.0 0.000 TL 1.75 PV Pipe: 8 0.0 1.380 PL 4.00 PP 0.0 8 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 9 33.5 0.0 89.3 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 PL 0.83 PP 0.0 9 33.5 0.0 89.3 0.0 0.0 120 FTG T PE 0.0 10 33.5 0.0 89.3 0.0 0.000 TL 6.83 PV Pipe: 10 -61.1 1.380 PL 3.50 PP 2.6 10 33.5 0.0 89.3 0.0 13.1 120 FTG T PE 1.5 11 30.0 0.0 93.4 0.0 0.270 TL 9.50 PV Pipe: 11 61.1 1.380 PL 3.17 PF 2.5 10 33.5 0.0 89.3 0.0 13.1 120 FTG T PE 0.0 12 33.5 0.0 86.8 0.0 0.270 TL 9.17 PV Pipe: 12 61.1 1.380 PL 4.00 PP 1.1 12 33.5 0.0 86.8 0.0 13.1 120 FTG ---- PE 0.0 13 33.5 0.0 85.7 0.0 0.270 TL 4.00 PV LI SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SD.F JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 61.1 1.380 PL 30.25 PF 8.7 13 33.5 0.0 85.7 0.0 13.1 120 FTG L PE 0.0 14 33.5 0.0 77.0 0.0 0.270 TL 32.25 PV Pipe: 14 61.1 1.380 PL 10.42 PF 4.4 14 33.5 0.0 77.0 0.0 13.1 120 FTG T PE 0.0 15 33.5 0.0 72.6 0.0 0.270 TL 16.42 PV Pipe: 15 61.1 1.380 PL 177.46 PF 52.0 15 33.5 0.0 72.6 0.0 13.1 120 FTG 3ET PE 0.0 16 33.5 5.6 20.6 25.4 0.270 TL 192.46 PV Pipe: 16 35.7 1.380 PL 6.00 PF 0.6 16 33.5 5.6 20.6 25.4 7.7 120 FTG ---- PE 0.0 17 33.5 5.6 20.0 25.0 0.100 TL 6.00 PV Pipe: 17 10.7 1.380 PL 6.00 PF 0.1 17 33.5 5.6 20.0 25.0 2.3 120 FTG ---- PE 0.0 18 33.5 5.6 19.9 25.0 0.011 TL 6.00 PV Pipe: 18 -14.3 1.380 FL 6.00 PF 0.1 18 33.5 5.6 19.9 25.0 3.1 120 FTG ---- PE 0.0 19 33.5 5.6 20.0 25.1 0.019 TL 6.00 PV Pipe: 19 -39.4 1.380 FL 6.00 PF 0.7 19 33.5 5.6 20.0 25.1 8.5 120 FTG ---- FE 0.0 20 33.5 5.6 20.8 25.5 0.120 TL 6.00 PV Pipe: 20 -64.9 1.380 PL 26.42 PF 9.8 20 33.5 5.6 20.8 25.5 13.9 120 FTG 2E FE 0.0 21 33.5 0.0 30.6 0.0 0.302 TL 32.42 PV Pipe: 21 -64.9 1.380 FL 189.96 PF 62.9 21 33.5 0.0 30.6 0.0 13.9 120 FTG 4ET PE 0.0 22 33.5 0.0 93.4 0.0 0302 TL 207.96 PV Pipe: 22 -64.9 1.380 PL 3.50 PF 2.9 22 33.5 0.0 93.4 0.0 13.9 120 FTG T FE 1.5 23 30.0 0.0 97.8 0.0 0.302 TL 9.50 By Pipe: 23 0.0 1.049 FL 35.00 PF 0.0 24 29.0 0.0 93.9 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 FL 2.75 PF 0.0 25 30.0 0.0 93.5 0.0 0.0 120 FTG ---- PE 0.0 27 30.0 0.0 93.5 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 FL 35.00 FE' 0.0 26 29.0 0.0 93.9 0.0 0.0 120 FTG ---- FE -0.4 27 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.380 PL 3.50 PF 0.0 27 30.0 0.0 93.5 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 93.5 0.0 0.000 TL 3.50 PV Pipe: 27 0.0 1.049 PL 35.00 PF 0.0 28 29.0 0.0 93.9 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 93.5 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 92.6 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PF 0.0 30 32.0 0.0 92.6 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 92.6 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 SF 0.0 31 32.0 0.0 92.6 0.0 0.0 120 FTG T SE 0.0 32 32.0 0.0 92.6 0.0 0.000 TL 6.96 PV Pipe: 31 9.8 1.380 PL 2.00 PF 0.1 32 32.0 0.0 92.6 0.0 2.1 120 FTG T PE 0.9 33 30.0 0.0 93.4 0.0 0.009 TL 8.00 PV Pipe: 32 -9.8 1.380 PL 47.58 PF 0.5 32 32.0 0.0 92.6 0.0 2.1 120 FTG TL PE 0.0 34 32.0 0.0 93.1 0.0 0.009 TL 55.58 PV Pipe: 33 -9.8 1.380 PL 138.50 PF 1.3 34 32.0 0.0 93.1 0.0 2.1 120 FTG 3E PE 0.0 35 32.0 0.0 94.5 0.0 0.009 TL 147.50 PV Pipe: 34 -9.8 1.380 PL 14.00 PF 0.2 35 32.0 0.0 94.5 0.0 2.1 120 FTG E PE 0.0 36 32.0 0.0 94.6 0.0 0.009 TL 17.00 PV Pipe: 35 -9.8 1.380 PL 10.00 SF 0.1 36 32.0 0.0 94.6 0.0 2.1 120 FTG ---- PE 0.0 37 32.0 0.0 94.7 0.0 0.009 TL 10.00 PV Pipe: 36 -9.8 1.380 PL 8.00 PF 0.1 37 32.0 0.0 94.7 0.0 2.1 120 FTG ---- PE 0.0 39 32.0 0.0 94.8 0.0 0.009 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 PF 0.0 38 32.0 0.0 94.8 0.0 0.0 120 FTG ---- PE 0.0 39 32.0 0.0 94.8 0.0 0.000 TL 10.00 PV Pipe: 38 -9.8 1.380 PL 10.00 SF 0.1 39 32.0 0.0 94.8 0.0 2.1 120 FTG ---- PE 0.0 40 32.0 0.0 94.9 0.0 0.009 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAJ4 FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -9.8 1.380 PL 34.67 PF 0.4 40 32.0 0.0 94.9 0.0 2.1 120 FTG 4E PE 0.0 41 32.0 0.0 95.3 0.0 0.009 TL 46.67 PV Pipe: 40 -9.8 1.380 PL 175.12 PF 1.6 41 32.0 0.0 95.3 0.0 2.1 120 FTG T PE 0.0 42 32.0 0.0 96.9 0.0 0.009 TL 181.12 PV Pipe: 41 -9.8 1.380 PL 2.00 PF 0.1 42 32.0 0.0 96.9 0.0 2.1 120 FTG T PE 0.9 43 30.0 0.0 97.9 0.0 0.009 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 92.6 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 93.5 0.0 0.000 TL 8.00 PV Pipe: 43 -10.4 1.380 PL 41.25 PF 0.5 45 30.0 0.0 93.5 0.0 2.2 120 FTG TL PE -0.9 46 32.0 0.0 93.1 0.0 0.010 TL 49.25 PV Pipe: 44 -10.4 1.380 PL 145.04 PF 1.5 46 32.0 0.0 93.1 0.0 2.2 120 FTG ---- PE 0.0 47 32.0 0.0 94.6 0.0 0.010 TL 145.04 PV Pipe: 45 -10.4 1.380 PL 10.00 PF 0.1 47 32.0 0.0 94.6 0.0 2.2 120 FTG ---- PE 0.0 48 32.0 0.0 94.7 0.0 0.010 TL 10.00 PV Pipe: 46 -10.4 1.380 PL 8.00 PF 0.1 48 32.0 0.0 94.7 0.0 2.2 120 FTG ---- PE 0.0 49 32.0 0.0 94.8 0.0 0.010 TL 8.00 PV Pipe: 47 -10.4 1.380 PL 10.00 PP 0.1 49 32.0 0.0 94.8 0.0 2.2 120 FTG ---- PE 0.0 50 32.0 0.0 94.9 0.0 0.010 TL 10.00 PV Pipe: 48 -10.4 1.380 PL 10.00 PP 0.1 50 32.0 0.0 94.9 0.0 2.2 120 FTG ---- PE 0.0 51 32.0 0.0 95.0 0.0 0.010 TL 10.00 PV Pipe: 49 -10.4 1.380 PL 27.96 PP 0.3 51 32.0 0.0 95.0 0.0 2.2 120 FTG 2E PE 0.0 52 32.0 0.0 95.3 0.0 0.010 TL 33.96 PV Pipe: 50 -10.4 1.380 PL 182.33 PF 1.9 52 32.0 0.0 95.3 0.0 2.2 120 FTG T PE 0.0 53 32.0 0.0 97.2 0.0 0.010 TL 188.33 PV Pipe: 51 -10.4 1.380 PL 2.00 PF 0.1 53 32.0 0.0 97.2 0.0 2.2 120 FTG T PE 0.9 54 30.0 0.0 98.2 0.0 0.010 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SY.STEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 10.3 1.380 PL 2.00 PF 0.1 55 32.0 0.0 92.7 0.0 2.2 120 FTG T FE 0.9 56 30.0 0.0 93.5 0.0 0.010 TL 8.00 PV Pipe: 53 -10.3 1.380 PL 38.17 PF 0.4 55 32.0 0.0 92.7 0.0 2.2 120 FTG L PE 0.0 57 32.0 0.0 93.1 0.0 0.010 TL 40.17 PV Pipe: 54 -10.3 1.380 PL 134.70 PF 1.3 57 32.0 0.0 93.1 0.0 2.2 120 FTG ---- FE 0.0 59 32.0 0.0 94.5 0.0 0.010 TL 134.70 PV Pipe: 55 0.0 1.049 FL 35.00 PF 0.0 58 29.0 0.0 95.8 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 94.5 0.0 0.000 TL 35.00 PV Pipe: 56 -10.3 1.380 PL 12.50 PF 0.1 59 32.0 0.0 94.5 0.0 2.2 120 FTG ---- PE 0.0 60 32.0 0.0 94.6 0.0 0.010 TL 12.50 PV Pipe: 57 -10.3 1.380 PL 1.83 PF 0.0 60 32.0 0.0 94.6 0.0 2.2 120 FTG ---- PE 0.0 62 32.0 0.0 94.6 0.0 0.010 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PF 0.0 61 29.0 0.0 95.9 0.0 0.0 120 FTG ---- PE -1.3 62 32.0 0.0 94.6 0.0 0.000 TL 35.00 PV Pipe: 59 -10.3 1.380 FL 9.25 PF 0.1 62 32.0 0.0 94.6 0.0 2.2 120 FTG ---- PE 0.0 64 32.0 0.0 94.7 0.0 0.010 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PF 0.0 63 29.0 0.0 96.0 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 94.7 0.0 0.000 TL 35.00 PV Pipe: 61 -10.3 1.380 PL 0.92 PF 0.0 64 32.0 0.0 94.7 0.0 2.2 120 FTG ---- FE 0.0 65 32.0 0.0 94.7 0.0 0.010 TL 0.92 PV Pipe: 62 -10.3 1.380 FL 12.00 PF 0.1 65 32.0 0.0 94.7 0.0 2.2 120 FTG ---- PE 0.0 66 32.0 0.0 94.9 0.0 0.010 TL 12.00 PV Pipe: 63 -10.3 1.380 FL 1.42 PF 0.0 66 32.0 0.0 94.9 0.0 2.2 120 FTG ---- PE 0.0 68 32.0 0.0 94.9 0.0 0.010 TL 1.42 PV Pipe: 64 0.0 1.049 PL 35.00 PF 0.0 67 29.0 0.0 96.2 0.0 0.0 120 FTG ---- PE -1.3 68 32.0 0.0 94.9 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDP JOB TITLE: La Costa Glen Building P Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -10.3 1.380 PL 9.17 PF 0.1 68 32.0 0.0 94.9 0.0 2.2 120 FTG ---- PE 0.0 70 32.0 0.0 95.0 0.0 0.010 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PP 0.0 69 29.0 0.0 96.3 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 95.0 0.0 0.000 TL 35.00 PV Pipe: 67 -10.3 1.380 PL 1.25 PF 0.0 70 32.0 0.0 95.0 0.0 2.2 120 FTG ---- PE 0.0 71 32.0 0.0 95.0 0.0 0.010 TL 1.25 PV Pipe: 68 -10.3 1.380 PL 30.80 PP 0.4 71 32.0 0.0 95.0 0.0 2.2 120 FTG ET PE 0.0 72 32.0 0.0 95.4 0.0 0.010 TL 39.80 PV Pipe: 69 -10.3 1.380 PL 175.00 PP 1.8 72 32.0 0.0 95.4 0.0 2.2 120 FTG T PE 0.0 73 32.0 0.0 97.2 0.0 0.010 TL 181.00 PV Pipe: 70 -10.3 1.380 PL 2.00 PP 0.1 73 32.0 0.0 97.2 0.0 2.2 120 FTG T PE 0.9 74 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 71 10.3 1.380 PL 2.00 PF 0.1 75 32.0 0.0 92.8 0.0 2.2 120 FTG T PE 0.9 76 30.0 0.0 93.5 0.0 0.010 TL 8.00 PV Pipe: 72 -10.3 1.380 PL 38.25 PP 0.4 75 32.0 0.0 92.8 0.0 2.2 120 FTG L PE 0.0 77 32.0 0.0 93.2 0.0 0.010 TL 40.25 PV Pipe: 73 -10.3 1.380 PL 150.42 PP 1.5 77 32.0 0.0 93.2 0.0 2.2 120 FTG ---- PE 0.0 78 32.0 0.0 94.7 0.0 0.010 TL 150.42 PV Pipe: 74 -10.3 1.380 PL 65.83 PP 0.7 78 32.0 0.0 94.7 0.0 2.2 120 FTG 2E PE 0.0 79 32.0 0.0 95.4 0.0 0.010 TL 71.83 PV Pipe: 75 -10.3 1.380 PL 170.83 PP 1.8 79 32.0 0.0 95.4 0.0 2.2 120 FTG T PE 0.0 80 32.0 0.0 97.2 0.0 0.010 TL 176.83 PV Pipe: 76 -10.3 1.380 PL 2.00 PP 0.1 80 32.0 0.0 97.2 0.0 2.2 120 FTG T PE 0.9 81 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 77 10.4 1.380 PL 2.00 PP 0.1 82 32.0 0.0 92.8 0.0 2.2 120 FTG T PE 0.9 83 30.0 0.0 93.6 0.0 0.010 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Cab 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -10.4 1.380 PL 24.58 PF 0.3 82 32.0 0.0 92.8 0.0 2.2 120 FTG L PE 0.0 84 32.0 0.0 93.0 0.0 0.010 TL 26.58 PV Pipe: 79 -10.4 1.380 FL 190.50 PF 2.0 84 32.0 0.0 93.0 0.0 2.2 120 FTG 4E PE 0.0 85 32.0 0.0 95.1 0.0 0.010 TL 202.50 PV Pipe: 80 -10.4 1.380 PL 196.21 PF 2.0 85 32.0 0.0 95.1 0.0 2.2 120 FTG T FE 0.0 86 32.0 0.0 97.1 0.0 0.010 TL 202.21 PV Pipe: 81 -10.4 1.380 PL 2.00 PF 0.1 86 32.0 0.0 97.1 0.0 2.2 120 FTG T FE 0.9 87 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 82 10.1 1.380 PL 3.50 PF 0.1 88 33.5 0.0 92.1 0.0 2.2 120 FTG T PE 1.5 89 30.0 0.0 93.6 0.0 0.010 TL 9.50 PV Pipe: 83 -10.1 1.380 PL 33.58 PF 0.3 88 33.5 0.0 92.1 0.0 2.2 120 FTG L FE 0.0 90 33.5 0.0 92.5 0.0 0.010 TL 35.58 PV Pipe: 84 -10.1 1.380 PL 202.38 PF 2.1 90 33.5 0.0 92.5 0.0 2.2 120 FTG 3ET FE 0.0 91 33.5 0.0 94.6 0.0 0.010 TL 217.38 PV Pipe: 85 -10.1 1.380 PL 193.96 PF 1.9 91 33.5 0.0 94.6 0.0 2.2 120 FTG T FE 0.0 92 33.5 0.0 96.5 0.0 0.010 TL 199.96 PV Pipe: 86 -10.1 1.380 PL 3.50 PF 0.1 92 33.5 0.0 96.5 0.0 2.2 120 FTG T FE 1.5 93 30.0 0.0 98.1 0.0 0.010 TL 9.50 PV Pipe: 87 -61.1 2.635 FL 3.00 PF 0.0 11 30.0 0.0 93.4 0.0 3.6 120 FTG ---- PE 0.0 33 30.0 0.0 93.4 0.0 0.012 TL 3.00 PV Pipe: 88 -51.3 2.635 PL 8.50 PF '0.1 33 30.0 0.0 93.4 0.0 3.0 120 FTG ---- FE 0.0 45 30.0 0.0 93.5 0.0 0.008 TL 8.50 PV Pipe: 89 -41.0 2.635 FL 6.92 PF 0.0 45 30.0 0.0 93.5 0.0 2.4 120 FTG ---- FE 0.0 56 30.0 0.0 93.5 0.0 0.006 TL 6.92 PV Pipe: 90 -30.7 2.635 PL 7.42 PF 0.0 56 30.0 0.0 93.5 0.0 1.8 120 FTG ---- PE 0.0 76 30.0 0.0 93.5 0.0 0.003 TL 7.42 PV II SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (ET) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -20.4 2.635 PL 7.00 FE 0.0 76 30.0 0.0 93.5 0.0 1.2 120 FTG ---- FE 0.0 83 30.0 0.0 93.6 0.0 0.002 TL 7.00 PV Pipe: 92 -10.1 2.635 PL 3.92 FE 0.0 83 30.0 0.0 93.6 0.0 0.6 120 FTG ---- FE 0.0 89 30.0 0.0 93.6 0.0 0.000 TL 3.92 PV Pipe: 93 -64.9 2.635 PL 5.54 PF 0.1 23 30.0 0.0 97.8 0.0 3.8 120 FTG ---- FE 0.0 43 30.0 0.0 97.9 0.0 0.013 TL 5.54 PV Pipe: 94 -74.7 2.635 PL 8.96 PF 0.4 43 30.0 0.0 97.9 0.0 4.4 120 FTG T PE 0.0 94 30.0 0.0 98.3 0.0 0.017 TL 25.96 PV Pipe: 95 -10.1 2.635 PL 5.40 FE 0.0 93 30.0 0.0 98.1 0.0 0.6 120 FTG ---- FE 0.0 87 30.0 0.0 98.1 0.0 0.000 TL 5.40 PV Pipe: 96 -20.4 2.635 PL 9.50 FE 0.0 87 30.0 0.0 98.1 0.0 1.2 120 FTG ---- FE 0.0 81 30.0 0.0 98.1 0.0 0.002 TL 9.50 PV Pipe: 97 -30.7 2.635 PL 8.17 FE 0.0 81 30.0 0.0 98.1 0.0 1.8 120 FTG ---- FE 0.0 74 30.0 0.0 98.1 0.0 0.003 TL 8.17 PV Pipe: 98 -41.0 2.635 FL 7.96 FE 0.0 74 30.0 0.0 98.1 0.0 2.4 120 FTG ---- PE 0.0 54 30.0 0.0 98.2 0.0 0.006 TL 7.96 PV Pipe: 99 -51.3 2.635 PL 1.04 FE 0.2 54 30.0 0.0 98.2 0.0 3.0 120 FTG T PE 0.0 94 30.0 0.0 98.3 0.0 0.008 TL 18.04 PV Pipe: 100 -126.0 2.635 FL 20.38 FE 1.6 94 30.0 0.0 98.3 0.0 7.4 120 FTG 25 FE 0.0 95 30.0 0.0 99.9 0.0 0.044 TL 36.38 PV Pipe: 101 -126.0 2.635 PL 75.50 FE 5.1 95 30.0 0.0 99.9 0.0 7.4 120 FTG 5E FE 12.8 BOR 0.5 0.0 117.8 0.0 0.044 TL 115.50 PV Pipe: 102 -126.0 6.280 FL 10.00 PF 0.0 BOR 0.5 0.0 117.8 0.0 1.3 140 FTG E FE 1.5 UG3 -3.0 0.0 119.3 0.0 0.000 TL 32.00 PV Pipe: 103 -126.0 6.080 FL 142.00 PF 0.1 UG3 -3.0 0.0 119.3 0.0 1.4 150 FTG 3E FE 0.0 UG2 -3.0 0.0 119.4 0.0 0.000 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -126.0 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 119.4 0.0 1.3 140 FTG ET FE -2.2 BF2 2.0 0.0 117.3 0.0 0.000 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE SF1 2.0 0.0 121.3 0.0 4.0 psi, 126.0 gpm BF2 2.0 0.0 117.3 0.0 Pipe: 106 -126.0 6.280 PL 5.00 PF 0.0 BF1 2.0 0.0 121.3 0.0 1.3 140 FTG 2E FE 2.2 UG1 -3.0 0.0 123.5 0.0 0.000 TL 49.00 PV Pipe: 107 -126.1 6.080 PL 16.00 PF 0.0 UG1 -3.0 0.0 123.5 0.0 1.4 150 FTG TG PE 0.0 SRC -3.0 SRCE 123.5 (N/A) 0.000 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by I-IRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.114 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 13.9 ft/sec at pipe 22. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.85 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP LI SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PAGE: A MATERIAL: S40 HC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 400 600 800 1000 1200 1400 1600 1800 2000 140.0 G A U120.0 G E P100. 0 R E S S 80.0 U R E OW p S 40.0 20.0 [SW -14 WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm FLOW (GPM) ;hed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS WATER SUPPLY CURVE 156*0\\\\\\\\\\\\\\\\\\\\\\\\\ I \\\\\\\\\\\\\\\\\\\\\\\\\\ I 149.0 psi @ 1790 gpm-> * I Flow Test Point 143+ 130+ Ix 117+ P104+ R I E I S I 5 91+ U I R I E 78+ P I S I I 65+ 52+ 39+ 26+ LEGEND I X = Required Water Supply I 123.54 psi @ 226.1 gpm 13+ I 0 = Available Water Supply I 154.87 psi @ 226.1 gpm 7 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.9 229.3 71.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 229.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 129.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 21.9 - - - 2 30.0 - - - - 21.4 - - - 3 33.5 - - - - 19.9 - - - 4 33.5 K= 5.60 19.9 25.0 5 29.0 - - - - 22.0 - - - 6 30.0 - - - - 21.6 - - - 7 33.5 - - - - 20.0 - - - 8 33.5 K= 5.60 20.1 25.1 9 33.5 K= 5.60 20.9 25.6 10 33.5 - - - - 23.6 11 30.0 - - - - 32.4 - - - 12 33.5 K= 5.60 22.9 26.8 13 33.5 K= 5.60 22.9 26.8 14 33.5 - - - - 24.3 - - - 15 33.5 - - - - 24.9 - - - 16 33.5 - - - - 33.0 - - - 17 33.5 - - - - 33.3 - - - 18 33.5 - - - - 33.5 - - - 19 33.5 - - - - 33.8 - - - 20 33.5 - - - - 34.0 - - - 21 33.5 - - - - 35.4 - - - 22 33.5 - - - - 44.1 - - - 23 30.0 - - - 46.0 - - - 24 29.0 - - - - 33.1 - - - 25 30.0 - - - - 32.7 - - - 26 29.0 - - - - 33.1 - - - 27 30.0 - - - - 32.7 - - - 28 29.0 - - - - 33.1 - - - 29 30.0 - - - - 32.7 - - - 30 32.0 - - - - 31.8 - - - 31 32.0 - - - - 31.8 - - - 32 32.0 - - - - 31.8 - - - 33 30.0 - - - - 32.5 - - - 34 32.0 - - - - 33.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 37.4 - - - 36 32.0 - - - - 37.9 - - - 37 32.0 - - - - 38.2 - - - 38 32.0 - - - - 38.4 - - - 39 32.0 - - - - 38.4 - - 40 32.0 - - - - 38.7 - - - 41 32.0 - - - - 39.9 - - - 42 32.0 - - - - 44.9 - - - 43 30.0 - - - - 46.0 - - - 44 32.0 - - - - 31.8 - - - 45 30.0 - - - - 32.7 - - - 46 32.0 - - - - 33.2 - - - 47 32.0 - - - - 37.3 - - - 48 32.0 - - - - 37.6 - - - 49 32.0 - - - - 37.8 - - - 50 32.0 - - - - 38.1 51 32.0 - - - - 38.4 - - - 52 32.0 - - - - 39.3 - - 53 32.0 - - - - 44.6 - - - 54 30.0 - - - - 45.7 - - - 55 32.0 - - - - 32.1 - - - 56 30.0 - - - - 32.8 - - - 57 32.0 - - - - 33.3 - - - 58 29.0 - - - - 38.3 - - - 59 32.0 - - - - 37.0 - - - 60 32.0 - - - - 37.4 - - - 61 29.0 - - - - 38.7 - - - 62 32.0 - - - - 37.4 - - - 63 29.0 - - - - 39.0 - - - 64 32.0 - - - - 37.7 - - - 65 32.0 - - - - 37.7 66 32.0 - - - - 38.0 - - - 67 29.0 - - - - 39.4 - - - 68 32.0 - - - - 38.1 - - - 69 29.0 - - - - 39.6 - - - 70 32.0 - - - - 38.3 - - - 71 32.0 - - - - 38.4 - - - 72 32.0 - - - - 39.5 - - - 73 32.0 - - - - 44.5 - - - 74 30.0 - - - - 45.6 - - - 75 32.0 - - - - 32.2 - - - 76 30.0 - - - - 32.9 - - - 77 32.0 - - - - 33.3 - - - 78 32.0 - - - - 37.5 - - - 79 32.0 - - - - 39.5 - - - 80 32.0 - - - - 44.4 - - - 81 30.0 - - - - 45.5 - - - 82 32.0 - - - - 32.2 - - - 83 30.0 - - - - 32.9 - - - 84 32.0 - - - - 33.0 - - - 85 32.0 - - - - 38.7 86 32.0 - - - - 44.4 - - - cl SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 87 30.0 - - - - 45.5 - - - 88 33.5 - - - - 31.6 - - - 89 30.0 - - - - 32.9 - - - 90 33.5 - - - - 32.6 91 33.5 - - - - 38.4. - - - 92 33.5 - - - - 43.7 - - - 93 30.0 - - - - 45.5 - - - 94 30.0 - - - - 46.1 - - - 95 30.0 - - - - 47.8 - - - BOR 0.5 - - - - 66.0 UG3 -3.0 - - - - 67.5 UG2 -3.0 - - - - 67.6 BF2 2.0 - - - - 65.5 BF1 2.0 - - - - 69.5 - - - UGl -3.0 - - - - 71.7 - - - SRC -3.0 SOURCE 71.7 129.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 21.9 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 '0.0 21.4 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 21.4 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 19.9 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 19.9 0.0 0.0 120 FTG ---- PH 0.0 4 33.5 5.6 19.9 25.0 0.000 TL 2.50 PV Pipe: 4 -25.0 1.380 PL 2.21 PF 0.1 4 33.5 5.6 19.9 25.0 5.4 120 FTG ---- PE 0.0 7 33.5 0.0 20.0 0.0 0.052 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 22.0 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 21.6 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 FL 4.29 PF 0.0 6 30.0 0.0 21.6 0.0 0.0 120 FTG ET PH -1.5 7 33.5 0.0 20.0 0.0 0.000 TL 13.29 PV Pipe: 7 -25.0 1.380 PL 1.75 PF 0.1 7 33.5 0.0 20.0 0.0 5.4 120 FTG ---- PE 0.0 8 33.5 5.6 20.1 25.1 0.052 TL 1.75 PV Pipe: 8 -50.1 1.380 FL 4.00 PF 0.7 8 33.5 5.6 20.1 25.1 10.8 120 FTG ---- PE 0.0 9 33.5 5.6 20.9 25.6 0.187 TL 4.00 PV Pipe: 9 -75.7 1.380 FL 0.83 PF 2.7 9 33.5 5.6 20.9 25.6 16.2 120 FTG T FE 0.0 10 33.5 0.0 23.6 0.0 0.402 TL 6.83 PV Pipe: 10 -107.0 1.380 FL 3.50 PF 7.2 10 33.5 0.0 23.6 0.0 23.0 120 FTG T FE 1.5 11 30.0 0.0 32.4 0.0 0.762 TL 9.50 PV Pipe: 11 31.3 1.380 FL 3.17 PF 0.7 10 33.5 0.0 23.6 0.0 6.7 120 FTG T FE 0.0 12 33.5 5.6 22.9 26.8 0.078 TL 9.17 PV Pipe: 12 4.5 1.380 FL 4.00 PF 0.0 12 33.5 5.6 22.9 26.8 1.0 120 FTG ---- PE 0.0 13 33.5 5.6 22.9 26.8 0.002 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SDI Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -22.3 1.380 PL 30.25 PP 1.4 13 33.5 5.6 22.9 26.8 4.8 120 FTG L PP 0.0 14 33.5 0.0 24.3 0.0 0.042 TL 32.25 PV Pipe: 14 -22.3 1.380 PL 10.42 PP 0.7 14 33.5 0.0 24.3 0.0 4.8 120 FTG T PP 0.0 15 33.5 0.0 24.9 0.0 0.042 TL 16.42 PV Pipe: 15 -22.3 1.380 PL 177.46 PF 8.1 15 33.5 0.0 24.9 0.0 4.8 120 FTG 3ET PE 0.0 16 33.5 0.0 33.0 0.0 0.042 TL 192.46 PV Pipe: 16 -22.3 1.380 PL 6.00 PP 0.3 16 33.5 0.0 33.0 0.0 4.8 120 FTG ---- PE 0.0 17 33.5 0.0 33.3 0.0 0.042 TL 6.00 PV Pipe: 17 -22.3 1.380 PL 6.00 PP 0.3 17 33.5 0.0 33.3 0.0 4.8 120 FTG ---- PE 0.0 18 33.5 0.0 33.5 0.0 0.042 TL 6.00 PV Pipe: 18 -22.3 1.380 PL 6.00 PP 0.3 18 33.5 0.0 33.5 0.0 4.8 120 FTG ---- PE 0.0 19 33.5 0.0 33.8 0.0 0.042 TL 6.00 PV Pipe: 19 -22.3 1.380 PL 6.00 PF 0.3 19 33.5 0.0 33.8 0.0 4.8 120 FTG ---- PE 0.0 20 33.5 0.0 34.0 0.0 0.042 TL 6.00 PV Pipe: 20 -22.3 1.380 PL 26.42 PF 1.4 20 33.5 0.0 34.0 0.0 4.8 120 FTG 2E PE 0.0 21 33.5 0.0 35.4 0.0 0.042 TL 32.42 PV Pipe: 21 -22.3 1.380 PL 189.96 PP 8.7 21 33.5 0.0 35.4 0.0 4.8 120 FTG 4ET PE 0.0 22 33.5 0.0 44.1 0.0 0.042 TL 207.96 PV Pipe: 22 -22.3 1.380 PL 3.50 PF 0.4 22 33.5 0.0 44.1 0.0 4.8 120 FTG T PE 1.5 23 30.0 0.0 46.0 0.0 0.042 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PF 0.0 24 29.0 0.0 33.1 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PF 0.0 25 30.0 0.0 32.7 0.0 0.0 120 FTG ---- PE 0.0 27 30.0 0.0 32.7 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PF 0.0 26 29.0 0.0 33.1 0.0 0.0 120 FTG ---- PE -0.4 27 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.380 PL 3.50 PP 0.0 27 30.0 0.0 32.7 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 32.7 0.0 0.000 TL 3.50 PV Pipe: 27 0.0 1.049 PL 35.00 PP 0.0 28 29.0 0.0 33.1 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 32.7 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 31.8 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PF 0.0 30 32.0 0.0 31.8 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 31.8 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PF 0.0 31 32.0 0.0 31.8 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 31.8 0.0 0.000 TL 6.96 PV Pipe: 31 17.8 1.380 PL 2.00 PP 0.2 32 32.0 0.0 31.8 0.0 3.8 120 FTG T PE 0.9 33 30.0 0.0 32.5 0.0 0.027 TL 8.00 PV Pipe: 32 -17.8 1.380 PL 47.58 PP 1.5 32 32.0 0.0 31.8 0.0 3.8 120 FTG TL PE 0.0 34 32.0 0.0 33.4 0.0 0.027 TL 55.58 PV Pipe: 33 -17.8 1.380 PL 138.50 PP 4.1 34 32.0 0.0 33.4 0.0 3.8 120 FTG 3E PE 0.0 35 32.0 0.0 37.4 0.0 0.027 TL 147.50 PV Pipe: 34 -17.8 1.380 PL 14.00 PP 0.5 35 32.0 0.0 37.4 0.0 3.8 120 FTG E PE 0.0 36 32.0 0.0 37.9 0.0 0.027 TL 17.00 PV Pipe: 35 -17.8 1.380 PL 10.00 PF 0.3 36 32.0 0.0 37.9 0.0 3.8 120 FTG ---- PE 0.0 37 32.0 0.0 38.2 0.0 0.027 TL 10.00 PV Pipe: 36 -17.8 1.380 PL 8.00 PF 0.2 37 32.0 0.0 38.2 0.0 3.8 120 FTG ---- PE 0.0 39 32.0 0.0 38.4 0.0 0.027 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 PF 0.0 38 32.0 0.0 38.4 0.0 0.0 120 FTG ---- PE 0.0 39 32.0 0.0 38.4 0.0 0.000 TL 10.00 PV Pipe: 38 -17.8 1.380 PL 10.00 PP 0.3 39 32.0 0.0 38.4 0.0 3.8 120 FTG ---- PE 0.0 40 32.0 0.0 38.7 0.0 0.027 TL 10.00 PV D SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -17.8 1.380 PL 34.67 FE' 1.3 40 32.0 0.0 38.7 0.0 3.8 120 FTG 4E PE 0.0 41 32.0 0.0 39.9 0.0 0.027 TL 46.67 PV Pipe: 40 -17.8 1.380 FL 175.12 PF 5.0 41 32.0 0.0 39.9 0.0 3.8 120 FTG T PE 0.0 42 32.0 0.0 44.9 0.0 0.027 TL 181.12 PV Pipe: 41 -17.8 1.380 PL 2.00 FE' 0.2 42 32.0 0.0 44.9 0.0 3.8 120 FTG T PE 0.9 43 30.0 0.0 46.0 0.0 0.027 TL 8.00 PV Pipe: 42 0.0 1.380 FL 2.30 PF 0.0 44 32.0 0.0 31.8 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 32.7 0.0 0.000 TL 8.00 PV Pipe: 43 -18.0 1.380 FL 41.25 FE' 1.4 45 30.0 0.0 32.7 0.0 3.9 120 FTG TL FE -0.9 46 32.0 0.0 33.2 0.0 0.028 TL 49.25 PV Pipe: 44 -18.0 1.380 PL 145.04 FE' 4.1 46 32.0 0.0 33.2 0.0 3.9 120 FTG ---- PE 0.0 47 32.0 0.0 37.3 0.0 0.028 TL 145.04 PV Pipe: 45 -18.0 1.380 FL 10.00 PF 0.3 47 32.0 0.0 37.3 0.0 3.9 120 FTG ---- PE 0.0 48 32.0 0.0 37.6 0.0 0.028 TL 10.00 PV Pipe: 46 -18.0 1.380 FL 8.00 FE' 0.2 48 32.0 0.0 37.6 0.0 3.9 120 FTG ---- PE 0.0 49 32.0 0.0 37.8 0.0 0.028 TL 8.00 PV Pipe: 47 -18.0 1.380 PL 10.00 PF 0.3 49 32.0 0.0 37.8 0.0 3.9 120 FTG ---- PE 0.0 50 32.0 0.0 38.1 0.0 0.028 TL 10.00 PV Pipe: 48 -18.0 1.380 FL 10.00 P8' 0.3 50 32.0 0.0 38.1 0.0 3.9 120 FTG ---- PE 0.0 51 32.0 0.0 38.4 0.0 0.028 TL 10.00 PV Pipe: 49 -18.0 1.380 PL 27.96 P8' 1.0 51 32.0 0.0 38.4 0.0 3.9 120 FTG 2E PE 0.0 52 32.0 0.0 39.3 0.0 0.028 TL 33.96 PV Pipe: 50 -18.0 1.380 FL 182.33 FE' 5.3 52 32.0 0.0 39.3 0.0 3.9 120 FTG T FE 0.0 53 32.0 0.0 44.6 0.0 0.028 TL 188.33 PV Pipe: 51 -18.0 1.380 FL 2.00 PF 0.2 53 32.0 0.0 44.6 0.0 3.9 120 FTG T PE 0.9 54 30.0 0.0 45.7 0.0 0.028 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 17.9 1.380 PL 2.00 PF 0.2 55 32.0 0.0 32.1 0.0 3.8 120 FTG T PE 0.9 56 30.0 0.0 32.8 0.0 0.028 TL 8.00 PV Pipe: 53 -17.9 1.380 PL 38.17 PP 1.1 55 32.0 0..0 32.1 0.0 3.8 120 FTG L PE 0.0 57 32.0 0.0 33.3 0.0 0.028 TL 40.17 PV Pipe: 54 -17.9 1.380 PL 134.70 PF 3.7 57 32.0 0.0 33.3 0.0 3.8 120 FTG ---- PE 0.0 59 32.0 0.0 37.0 0.0 0.028 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 38.3 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 37.0 0.0 0.000 TL 35.00 PV Pipe: 56 -17.9 1.380 PL 12.50 PP 0.3 59 32.0 0.0 37.0 0.0 3.8 120 FTG ---- PE 0.0 60 32.0 0.0 37.4 0.0 0.028 TL 12.50 PV Pipe: 57 -17.9 1.380 PL 1.83 PP 0.1 60 32.0 0.0 37.4 0.0 3.8 120 FTG ---- PE 0.0 62 32.0 0.0 37.4 0.0 0.028 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PF 0.0 61 29.0 0.0 38.7 0.0 0.0 120 FTG ---- PE -1.3 62 32.0 0.0 37.4 0.0 0.000 TL 35.00 PV Pipe: 59 -17.9 1.380 PL 9.25 PP 0.3 62 32.0 0.0 37.4 0.0 3.8 120 FTG ---- PE 0.0 64 32.0 0.0 37.7 0.0 0.028 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PP 0.0 63 29.0 0.0 39.0 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 37.7 0.0 0.000 TL 35.00 PV Pipe: 61 -17.9 1.380 PL 0.92 PP 0.0 64 32.0 0.0 37.7 0.0 3.8 120 FTG ---- PE 0.0 65 32.0 0.0 37.7 0.0 0.028 TL 0.92 PV Pipe: 62 -17.9 1.380 PL 12.00 PP 0.3 65 32.0 0.0 37.7 0.0 3.8 120 FTG ---- PE 0.0 66 32.0 0.0 38.0 0.0 0.028 TL 12.00 PV Pipe: 63 -17.9 1.380 PL 1.42 PP 0.0 66 32.0 0.0 38.0 0.0 3.8 120 FTG ---- PE 0.0 68 32.0 0.0 38.1 0.0 0.028 TL 1.42 PV Pipe: 64 0.0 1.049 PL 35.00 PP 0.0 67 29.0 0.0 39.4 0.0 0.0 120 FTG ---- PE -1.3 68 32.0 0.0 38.1 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -17.9 1.380 PL 9.17 PF 0.3 68 32.0 0.0 38.1 0.0 3.8 120 FTG ---- PE 0.0 70 32.0 0.0 '38.3 0.0 0.028 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 39.6 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 38.3 0.0 0.000 TL 35.00 PV Pipe: 67 -17.9 1.380 PL 1.25 PF 0.0 70 32.0 0.0 38.3 0.0 3.8 120 FTG ---- PE 0.0 71 32.0 0.0 38.4 0.0 0.028 TL 1.25 PV Pipe: 68 -17.9 1.380 PL 30.80 PF 1.1 71 32.0 0.0 38.4 0.0 3.8 120 FTG ET PE 0.0 72 32.0 0.0 39.5 0.0 0.028 TL 39.80 PV Pipe: 69 -17.9 1.380 PL 175.00 PF 5.0 72 32.0 0.0 39.5 0.0 3.8 120 FTG T PE 0.0 73 32.0 0.0 44.5 0.0 0.028 TL 181.00 PV Pipe: 70 -17.9 1.380 PL 2.00 PF 0.2 73 32.0 0.0 44.5 0.0 3.8 120 FTG T PE 0.9 74 30.0 0.0 45.6 0.0 0.028 TL 8.00 PV Pipe: 71 17.9 1.380 PL 2.00 PF 0.2 75 32.0 0.0 32.2 0.0 3.8 120 FTG T PE 0.9 76 30.0 0.0 32.9 0.0 0.028 TL 8.00 PV Pipe: 72 -17.9 1.380 PL 38.25 PF 1.1 75 32.0 0.0 32.2 0.0 3.8 120 FTG L PE 0.0 77 32.0 0.0 33.3 0.0 0.028 TL 40.25 PV Pipe: 73 -17.9 1.380 PL 150.42 PF 4.2 77 32.0 0.0 33.3 0.0 3.8 120 FTG ---- PE 0.0 78 32.0 0.0 37.5 0.0 0.028 TL 150.42 PV Pipe: 74 -17.9 1.380 PL 65.83 PF 2.0 78 32.0 0.0 37.5 0.0 3.8 120 FTG 2E PE 0.0 79 32.0 0.0 39.5 0.0 0.028 TL 71.83 PV Pipe: 75 -17.9 1.380 PL 170.83 PF 4.9 79 32.0 0.0 39.5 0.0 3.8 120 FTG T PE 0.0 80 32.0 0.0 44.4 0.0 0.028 TL 176.83 PV Pipe: 76 -17.9 1.380 PL 2.00 PF 0.2 80 32.0 0.0 44.4 0.0 3.8 120 FTG T PE 0.9 81 30.0 0.0 45.5 0.0 0.028 TL 8.00 PV Pipe: 77 18.0 1.380 PL 2.00 PF 0.2 82 32.0 0.0 32.2 0.0 3.9 120 FTG T PE 0.9 83 30.0 0.0 32.9 0.0 0.028 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDP JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -18.0 1.380 PL 24.58 PP 0.7 82 32.0 0.0 32.2 0.0 3.9 120 FTG L FE 0.0 84 32.0 0.0 33.0 0.0 0.028 TL 26.58 PV Pipe: 79 -18.0 1.380 PL 190.50 PP 5.7 84 32.0 0.0 33.0 0.0 3.9 120 FTG 4E PE 0.0 85 32.0 0.0 38.7 0.0 0.028 TL 202.50 PV Pipe: 80 -18.0 1.380 PL 196.21 PP 5.7 85 32.0 0.0 38.7 0.0 3.9 120 FTG T FE 0.0 86 32.0 0.0 44.4 0.0 0.028 TL 202.21 PV Pipe: 81 -18.0 1.380 PL 2.00 PP 0.2 86 32.0 0.0 44.4 0.0 3.9 120 FTG T FE 0.9 87 30.0 0.0 45.5 0.0 0.028 TL 8.00 PV Pipe: 82 17.5 1.380 PL 3.50 PP 0.3 88 33.5 0.0 31.6 0.0 3.7 120 FTG T PE 1.5 89 30.0 0.0 32.9 0.0 0.027 TL 9.50 PV Pipe: 83 -17.5 1.380 PL 33.58 PP 0.9 88 33.5 0.0 31.6 0.0 3.7 120 FTG L PE 0.0 90 33.5 0.0 32.6 0.0 0.027 TL 35.58 PV Pipe: 84 -17.5 1.380 PL 202.38 PP 5.8 90 33.5 0.0 32.6 0.0 3.7 120 FTG 3ET FE 0.0 91 33.5 0.0 38.4 0.0 0.027 TL 217.38 PV Pipe: 85 -17.5 1.380 PL 193.96 PP 5.3 91 33.5 0.0 38.4 0.0 3.7 120 FTG T PE 0.0 92 33.5 0.0 43.7 0.0 0.027 TL 199.96 PV Pipe: 86 -17.5 1.380 PL 3.50 PP 0.3 92 33.5 0.0 43.7 0.0 3.7 120 FTG T FE 1.5 93 30.0 0.0 45.5 0.0 0.027 TL 9.50 PV Pipe: 87 -107.0 2.635 FL 3.00 PP 0.1 11 30.0 0.0 32.4 0.0 6.3 120 FTG ---- FE 0.0 33 30.0 0.0 32.5 0.0 0.033 TL 3.00 PV Pipe: 88 -89.3 2.635 PL 8.50 PP 0.2 33 30.0 0.0 32.5 0.0 5.3 120 FTG ---- FE 0.0 45 30.0 0.0 32.7 0.0 0.023 TL 8.50 PV Pipe: 89 -71.2 2.635 FL 6.92 PP 0.1 45 30.0 0.0 32.7 0.0 4.2 120 FTG ---- FE 0.0 56 30.0 0.0 32.8 0.0 0.015 TL 6.92 PV Pipe: 90 -53.4 2.635 PL 7.42 PP 0.1 56 30.0 0.0 32.8 0.0 3.1 120 FTG ---- FE 0.0 76 30.0 0.0 32.9 0.0 0.009 TL 7.42 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) •LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -35.5 2.635 PL 7.00 PF 0.0 76 30.0 0.0 32.9 0.0 2.1 120 FTG ---- PE 0.0 83 30.0 0.0 32.9 0.0 0.004 TL 7.00 PV Pipe: 92 -17.5 2.635 PL 3.92 PF 0.0 83 30.0 0.0 32.9 0.0 1.0 120 FTG ---- PE 0.0 89 30.0 0.0 32.9 0.0 0.001 TL 3.92 PV Pipe: 93 -22.3 2.635 PL 5.54 PF 0.0 23 30.0 0.0 46.0 0.0 1.3 120 FTG ---- PE 0.0 43 30.0 0.0 46.0 0.0 0.002 TL 5.54 PV Pipe: 94 -40.1 2.635 PL 8.96 PF 0.1 43 30.0 0.0 46.0 0.0 2.4 120 FTG T PE 0.0 94 30.0 0.0 46.1 0.0 0.005 TL 25.96 PV Pipe: 95 -17.5 2.635 PL 5.40 PF 0.0 93 30.0 0.0 45.5 0.0 1.0 120 FTG ---- PE 0.0 87 30.0 0.0 45.5 0.0 0.001 TL 5.40 PV Pipe: 96 -35.5 2.635 PL 9.50 PF 0.0 87 30.0 0.0 45.5 0.0 2.1 120 FTG ---- PE 0.0 81 30.0 0.0 45.5 0.0 0.004 TL 9.50 PV Pipe: 97 -53.4 2.635 PL 8.17 PF 0.1 81 30.0 0.0 45.5 0.0 3.1 120 FTG ---- PE 0.0 74 30.0 0.0 45.6 0.0 0.009 TL 8.17 PV Pipe: 98 -71.2 2.635 PL 7.96 PF 0.1 74 30.0 0.0 45.6 0.0 4.2 120 FTG ---- PE 0.0 54 30.0 0.0 45.7 0.0 0.015 TL 7.96 PV Pipe: 99 -89.3 2.635 PL 1.04 PF 0.4 54 30.0 0.0 45.7 0.0 5.3 120 FTG T PE 0.0 94 30.0 0.0 46.1 0.0 0.023 TL 18.04 PV Pipe: 100 -129.3 2.635 PL 20.38 PF 1.7 94 30.0 0.0 46.1 0.0 7.6 120 FTG .2E PE 0.0 95 30.0 0.0 47.8 0.0 0.046 TL 36.38 PV Pipe: 101 -129.3 2.635 PL 75.50 PF 5.4 95 30.0 0.0 47.8 0.0 7.6 120 FTG SE PE 12.8 BOR 0.5 0.0 66.0 0.0 0.046 TL 115.50 PV Pipe: 102 -129.3 6.280 PL 10.00 PF 0.0 BOR 0.5 0.0 66.0 0.0 1.3 140 FTG E PE 1.5 UG3 -3.0 0.0 67.5 0.0 0.001 TL 32.00 PV Pipe: 103 -129.3 6.080 PL 142.00 PF 0.1 UG3 -3.0 0.0 67.5 0.0 1.4 150 FTG 3E PE 0.0 UG2 -3.0 0.0 67.6 0.0 0.001 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -129.3 6.280 PL 5.00 PP 0.0 UG2 -3.0 0.0 67.6 0.0 1.3 140 FTG ET PE -2.2 BF2 2.0 0.0 65.5 0.0 0.001 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE BFl 2.0 0.0 69.5 0.0 4.0 psi, 129.3 gpm BF2 2.0 0.0 65.5 0.0 Pipe: 106 -129.3 6.280 PL 5.00 PP 0.0 EF1 2.0 0.0 69.5 0.0 1.3 140 FTG 2E PE 2.2 UG1 -3.0 0.0 71.7 0.0 0.001 TL 49.00 PV Pipe: 107 -129.3 6.080 PL 16.00 PP 0.0 UG1 -3.0 0.0 71.7 0.0 1.4 150 FTG TG PE 0.0 SRC -3.0 SRCE 71.7 (N/A) 0.001 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.114 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 23.0 ft/sec at pipe 10. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.76 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP $ , , SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PAGE: A MATERIAL: S40 HC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 400 600 800 1000 1200 1400 1600 1800 2000 140.0 G A U120 G E P100.0 R E S S 80.0 U R E 1w. p 5 i 40.0 20.0 -14 WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm FLOW (GPM) thed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads WATER SUPPLY CURVE 156* 0\ \\ \ \ \ \ \ \ \ \\ \ \ \\ \ \ \\\ \\\\ I 149.0 psi @ 1790 gpm-> * I Flow Test Point 143+ 130+ 117+ P104+ R I E I S S 91+ U I R I E I 78+ P IX S I I 65+ 52+ 39+ 26+ LEGEND I X = Required Water Supply I 71.69 psi @ 229.3 gpm 13+ I 0 = Available Water Supply 154.87 psi @ 229.3 gpm I, +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) tqca Fire Protection Products Worldwide I www.tyco-fire.com Contacts Title RAPID RESPONSE Series LFII Re sidential Sprin- klers 69 K-factor, Pendent/Recessed Pendent/Con- cealed, NFPA 13 Optimized Wet Pipe Systems General Description The TYCO RAPID RESPONSE Series LFII Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers (TY4234) are decorative, fast response, frangible bulb sprin- klers designed for use in residential occupancies such as homes, apart- ments, dormitories, and hotels. When enhanced flow characteristics for resi- dential portions of any occupancy per NFPA 13 is the major consideration, the Series LFII (TY4234) should be the first choice. When higher flow demands are required for residential sprinklers used in an NFPA 13 design, the large 6.9 K-factor of the Series LFII (TY4234) is an attractive choice. Although mostly intended where residential sprinklers are to be used in an NFPA 13 design, the Series LFII (TY4234) can also be used in wet pipe residential sprin- kler systems for one- and two-family dwellings and mobile homes per NFPA 13D, and wet pipe residential sprinkler systems for residential occupancies up to and including four stories in height per NFPA 13R. The recessed version of the sprinkler is intended for use in areas with fin- ished ceilings. It employs a two-piece Style 30 Recessed Escutcheon. The Recessed Escutcheon provides 1/4 inch (6,4 mm) of recessed adjustment or up to 1/2 inch (12,7 mm) of total adjustment from the flush mounting surface position. The adjustment pro- vided by the Recessed Escutcheon or Concealed Cover Plate provides a IMPORTANT Always refer to Technical Data Sheet TFP700 for the "INSTALLER WARNING" that provides cautions with respect to handling and instal- lation of sprinkler systems and com- ponents. Improper handling and installation can permanently damage a sprinkler system or its compo- nents and cause the sprinkler to fail to operate in a fire situation or cause it to operate prematurely. Page 1 of 8 measure of flexibility with regard to which the length of fixed pipe drops to the sprinklers must be cut. The concealed version utilizes a cover plate assembly that conceals the sprin- kler operating components above the ceiling. The separable two-piece design of the Cover Plate and Support Cup Assemblies allows installation of the sprinklers and pressure testing of the fire protection system prior to the installation of the ceiling or application of a finish coating. Also, the separable "push-on and thread-off" two-piece design of the concealed version provides for 1/2 inch (12,7 mm ) of vertical adjustment. The Series LFII Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers have been designed with heat sensitivity and water distri- bution characteristics proven to help in the control of residential fires and to improve the chance for occupants to escape or be evacuated. The Series LFII Residential Concealed Pendent Sprinklers (TY4234) are shipped with a Disposable Protective Cap. The Protective Cap is temporar- ily removed for installation, and it must be replaced to protect the sprinkler while the ceiling is being installed o; finished. The tip of the Protective çp can also be used to mark the cter of the ceiling hole into plaster lbard, ceiling tiles, etc. by gently pushi(g the ceiling product against the Ptotec-tive Cap--When ceiling installafton is complete, the Protective Cap mut be removed and the Cover Plate Assethly installed. The Protective Cap must removed to ensure proper performance of the sprinklers. NOTICE The Series LFII (TY4234) Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers described herein must be installed and maintained in compliance with this document and with the applica- ble standards of the National Fire Pro- tection Association, in addition to the standards of any authorities having jurisdiction. Failure to do so may impair the performance of these devices. JANUARY 2016 The owner is responsible for maintain- ing their fire protection system and devices in proper operating condition. The installing contractor or sprinkler manufacturer should be contacted with any questions. TFP4O8 Components: 1 - Frame 2 - Button 3 - Sealing Assembly 1 4 - Bulb 5 Compression 2 Screw 6 - Deflector* 7 - Ejection Spring 4 * Temperature 5 rating is indicated on 6 Deflector. 1/2" (127 mm) NOMINAL MAKE-IN 7 TFP4OS Page 2 of 8 ESCUTCHEON PLATE SEATING 2-7/8" DIA._________ NPT SURFACE (73,0 mm) __ LJEIli 2-1/4 (57,2 " mm) (38,1 mm) WRENCH RECESSED I 1-1/2' I / STYLE 30 I I I FLATS ESCUTCHEON I CROSS SECTION PENDENT RECESSED PENDENT FIGURE 1 RAPID RESPONSE SERIES LFII RESIDENTIAL PENDENT AND RECESSED PENDENT SPRINKLERS (TY4234) 2-7/8 DIA. ( 73,0 mm) 1/2 (12,7 mm) 1/2±1/8 (12,7±3,2 mm) 2-1/4" DIA. 1/4" (6,4 mm) I (57,2 mm) FACE OF SPRINKLER MOUNTINGI I FITTING - /7r PLATE !L 4i:MOUNTING / SURFACE 1/8" (3,2 mm) ////L CLOSURE 1-3/8'(34 1-1/8" -3/8"(34 1-1/8(28,6mm) TY4234 (28,6 mm) FIGURE 2 STYLE 30 RECESSED ESCUTCHEON FOR USE WITH THE RAPID RESPONSE SERIES LFII RESIDENTIAL PENDENT SPRINKLER (TY4234) / WRENCH RECESS (END "B" USED e1_ D FOR TY4234) FIGURE 3 W-TYPE 6 SPRINKLER WRENCH WRENCH RECESS PUSH WRENCH IN TO ENSURE ENGAGEMENT WITH SPRINKLER WRENCHING AREA FIGURE W-TYPE 7 RECESSED SPRINKLER WRENCH SPRINKLER- SUPPORT CUP ASSEMB / COVER PLATE RETAINEI TFP4O8 Page 3 of 8 SUPPORT I CUP WITH SPRINKLER I Q_D ROLL FORMED STRAP (SEE THREADS INSTALLATION LIII1- SECTION) SPRINKLER/SUPPORT CUP ASSEMBLY THREAD INTO I I RETAINER SUPPORT CUP II '- WITH THREAD UNTIL MOUNTING 101 TABS SURFACE IS II FLUSH WITH. ii EJECTION CEILING D SPRING SOLDER COVER TABS (3) \ PLATE COVER PLATE/RETAINER ASSEMBLY FIGURE 5 RAPID RESPONSE SERIES LFII RESIDENTIAL CONCEALED PENDENT SPRINKLER (TY4234) (SHOWN WITH SPRINKLER STRAP) L...___ 2-1/2 DIA. (63,5 mm) 3/4" NPT 1/2 (12,7 mm) FACE OF THREADED SPRINKLER ADJUSTMENT FITTING !__-' 3/32 GAP 1 1-1/8±1/4' I (2,4 mm) F- (28,6 mm ±6,4 mm) MOUNTING SURFACE COVER- SPRINKLER- i J II / RETAINER SUPPORT CUP (25,4 mm) \. \J 7/8' (22,2 mm) ASSEMBLY ASSEMBLY 7" \ 3-5/16 DIA. PROTECTIVE (84,1 mm) TIP CAP FIGURE 6 DOMED CONCEALED COVER FOR USE WITH THE RAPID RESPONSE SERIES LFII RESIDENTIAL CONCEALED PENDENT SPRINKLER (TY4234) (SHOWN WITH PROTECTIVE CAP) OPERATED SPRINKLER TFP4OS Page 4 of 8 WET PIPE SYSTEM Minimum Flow and Residual Pressure(b, c) Max. Pendent and Recessed Pendent Coverage Maximum Ordinary Temp. Rating Intermediate Temp. Rating Area (a) Spacing Ft. (m) Minimum Ft. x Ft. 155°F (68°C) 175°F (79°C) Deflector to Installation Spacing (m x m) I Ceiling Type Ft. Flow Pressure Flow Pressure (m) GPM PSI GPM PSI (L/min) (bar) (L/min) (bar) 12x12 12 19 7.6 19 7.6 Smooth (3,7 x 3,7) (3,7) (71,9) (0,52) (71,9) (0,52) Ceilings 1-1/4 to 4 inches 14x14 14 19 7.6 19 7.6 (4,3x4,3) (4,3) (71,9) (0,52) (71,9) (0,52) Beamed Ceilings per Recessed using Style 30 16x16 16 19 7.6 19 7.6 NFPA 13D, Escutcheon or 8 (4,9 x 4,9) (4,9) (71,9) (0,52) (71,9) (052) 13R, or 13 Pendent and non-recessed per NFPA 13D, (2,4) 18x18 18 19 7.6 19 7.6 Recessed 13R,or13 (5,5x5,5) (5.5) (71,9) (0,52) (71,9) (0,52) Pendent 1-1/4to1-3/4 inches below bottom of 20 X 20 20 22 10.2 22 10.2 (6,1 X 6,1) (6,1) (83,3) (0,70) (83,3) (0,70) beam. For coverage area dimensions less than or between those indicated, use the minimum required flow for the next highest coverage area for which hydraulic design criteria are stated. Requirement is based on minimum flow in GPM (LPM) from each sprinkler. The associated residual pressures are calculated using the nominal K-factor. Refer to Hydraulic Design under the Design Criteria section. For NFPA 13 residential applications, the greater of 0.1 gpmlft2 over the design area or the flow in accordance with the criteria in this table must be used. TABLE A WET PIPE SYSTEM SERIES LFII RESIDENTIAL PENDENT AND RECESSED PENDENT SPRINKLERS (TY4234) NFPA 13D, 13R AND 13 HYDRAULIC DESIGN CRITERIA Sprinkler Identification Number (SIN) TY4234 Technical Data Approvals UL and C-UL Listed Certified to all requirements of NSF/ANSI 61 NYC Approved under MEA 44-03-E-2. FM Approved (Pendent and Recessed Pendent Only) The Series LFll Concealed Pendent Sprinklers are only listed and approved with the Series LFll Concealed Cover Plates having a factory applied finish. (Refer to the Design Criteria section for details on these approvals.) Maximum Working Pressure 175 psi (12,1 bar) Discharge Coefficient K=6.9 GPM/psi1l2 (99,4 LPM/bart/2) Pipe Thread Connection: 3/4 NPT Sprinkler Temperature Rating Pendent and Recessed Pendent: 155°F (68°C) or 175°F (79°C) Concealed Pendent: 155°F (68°C) w/139°F (59°C) Cover Plate 175°F (79°C) w/139°F (59°C) Cover Plate* *Suitable for use with maximum 100°F (38°C) ceiling temperature. Finishes Sprinkler: Natural Brass, Pure or Signal White, or Chrome Plated Recessed Escutcheon: Brass, Pure or Signal White, or Chrome Concealed Cover Plate: Refer to Ordering Procedure section. Physical Characteristics Frame .............................Brass Button ...........................Copper Sealing Assembly. . Beryllium Nickel w/TEFLON Bulb ....................... ...3mm Glass Compression Screw .................Bronze Deflector ..........................Bronze Ejection Spring ..............Stainless Steel Support Cup ........................Steel Cover Plate .........................Brass Retainer............................Brass Cover Plate Ejection Spring Stainless Steel Operation For pendent and recessed pendent sprinklers, the glass bulb contains a fluid that expands when exposed to heat. When the rated temperature is reached, the fluid expands sufficiently to shatter the glass bulb allowing the sprinkler to activate and flow water. For the concealed pendent sprinkler, the cover plate which is soldered to the support cup at three places, first falls away when exposed to heat from a fire. The sprinkler then operates similar to pendent and recessed pendent sprin- klers described above. TFP4O8 Page 5 of 8 WET PIPE SYSTEM Minimum Flow and Residual Pressure(b, c) Max. Concealed Pendent Coverage Maximum Ordinary Temp. Rating Intermediate Temp. Rating Area (a) Spacing Ft (m) Deflector to Installation Minimum Spacing Ft. x Ft. 155°F (68°C) 175°F (79°C) Ceiling Type Ft. (m x m) (m) Flow Pressure Flow Pressure GPM PSI GPM PSI (L/min) (bar) I (L/min) (bar) 12x12 12 19 7.6 19 7.6 Smooth (3,7 X 3,7) (3,7) (71,9) (0,52) (71,9) (0,52) Ceilings 3/8 to 7/8 14x14 14 19 7.6 19 7.6 inches. (4,3x4,3) (4,3) (71,9) (0,52) (71,9) (0,52) Beamed Ceilings per NFPA 13D, Concealed 8 16 x 16 16 19 7.6 19 7.6 (4,9 x 4,9) (4,9) (71,9) (0,52) (71,9) (0,52) 13R, or 13 installed in (2,4) 18 x 18 18 21 9.3 21 9.3 beam (5,5x5,5) (5,5) (79,5) (0,64) (79,5) (0,64) 3/8to7/8 inches below 20 x 20 20 24 12.1 24 12.1 bottom of (6,1 x 6,1) (6,1) (90,8) (0,83) (90,8) (0,83) beam For coverage area dimensions less than or between those indicated, use the minimum required flow for the next highest coverage area for which hydraulic design criteria are stated. Requirement is based on minimum flow in GPM (LPM) from each sprinkler. The associated residual pressures are calculated using the nominal K-factor. Refer to Hydraulic Design under the Design criteria section. c, For NFPA 13 residential applications, the greater of 0.1 gpm/ft2 over the design area or the flow in accordance with the criteria in this table must be used. TABLE B WET PIPE SYSTEM SERIES LFII RESIDENTIAL CONCEALED PENDENT SPRINKLERS (TY4234) NFPA 13D, 13R AND 13 HYDRAULIC DESIGN CRITERIA Design Criteria UL AND C-UL LISTING CRITERIA The TYCO RAPID RESPONSE Series LFII Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers (TY4234) are UL and C-UL Listed for installation in accordance with the following criteria. Residential Sprinkler Design Guide When conditions exist that are outside the scope of the provided criteria, refer to the Residential Sprinkler Design Guide TFP490 for the manufactur- er's recommendations that may be acceptable to the local authority having jurisdiction. System Type Only wet pipe systems may be utilized. Ceiling Types Smooth flat horizontal, or beamed, or sloped, in accordance with the 2013 Edition of NFPA 13D, 13R, or 13 as applicable. Hydraulic Design (NFPA 13D and 13R) The minimum required sprinkler flow rate for systems designed to NFPA 13D or NFPA 13R are given in Tables A and B as a function of temperature rating and the maximum allowable cov- erage areas. The sprinkler flow rate is the minimum required discharge from each of the total number of "design sprinklers" as specified in NFPA 13D or NFPA 13R. Hydraulic Design (NFPA 13) For systems designed to NFPA 13, the number of design sprinklers is to be the four most hydraulically demanding sprinklers. The minimum required dis- charge from each of the four sprinklers is to be the greater of the following: The flow rates given in Tables A and B for NFPA 13D and 13R as a func- tion of temperature rating and the maximum allowable coverage area A minimum discharge of 0.1 gpm/ft2. over the "design area" comprised of the four most hydraulically demand- ing sprinklers for the actual coverage areas being protected by the four sprinklers Example No. 1: A corridor being pro- tected is 8 ft. wide; consequently, an actual coverage area of 8 ft. x 20 ft. is being contemplated. Based on using the LFII (TY4234) Residential Pendent Sprinkler, the flow rate provided in Table A and B for a 20 ft. x 20 ft. cover- age area is 22 GPM. However based on minimum discharge of 0.1 gpm/ft2. the flow rate would be 16 GPM. In this case a minimum flow rate of 22 GPM for this design sprinkler must be utilized. Example No. 2: A long narrow room being protected is 12 ft. wide; con- sequently, an actual coverage area of 12 ft. x 20 ft. is being contemplated. Based on using the LFII (TY4234) Residential Pendent Sprinkler, the flow rate provided in Table A for a 20 ft. x 20 ft. coverage area is 22 GPM. However based on minimum discharge of 0.1 gpm/ft2. the flow rate would be 24 GPM. In this case a minimum flow rate of 24 GPM for this design sprinkler must be utilized. Obstruction to Water Distribution Sprinklers are to be located in accor- dance with the obstruction rules of NFPA 13D, 13R, and 13 as applica- ble for residential sprinklers as well as- with the obstruction criteria described within the TYCO Technical Data Sheet TFP49O. Operational Sensitivity Sprinklers are to be installed with a deflector-to-ceiling distance of 1-1/4 to 4 inches or in the recessed position using only the Style 30 escutcheon as shown in Figure 2. For concealed pendent sprinkler installations, the sprinklers relative to the ceiling mounting surface are to be installed per Figure 6. The concealed pendent sprinkler must not be used in applications where the air pressure above the ceiling is greater TFP4O8 Page 6 of 8 WET PIPE SYSTEM Minimum Flow and Residual Pressure(b, C) Max. Ordinary Temp. Rating 155°F (68°C) Intermediate Temp. Rating 175°F (79°C) Deflector to Ceiling Installation Type (bar) Minimum Spacing Ft. (m) Coverage Area (a) Ft. x Ft. (m x m) Maximum Spacing FL (m) Flow GPM (L/min) Pressure PSI (bar) Flow GPM (L/min) Pressure PSI 12x12 (3,7 x 3,7) 12 (3,7) 20 (75,7) 8.4 (0,58) 20 (75,7) 8.4 (0,58) Smooth 14 x 14 (4,3 x 4,3) 14 (4,3) 20 (75,7) 8.4 (0,58) 20 (75,7) 8.4 (0158) Ceilings 1-1/4 to 4 inches Beamed Ceilings 1-1/4 to 1-3/4 inches below bottom of Recessed using Style 30 Escutcheon or non-recessed 8 (2,4) 16x16 (4,9 x 4,9) 16 (4,9) 20 (75.7) 8.4 (0,58) 20 (75,7) 8.4 (0758) 18 x 18 (5,5 x 5,5) 18 (5,5) 20 (75,7) 8.4 (0,58) 20 (75,7) 8.4 (0,58) beam. 20x20 (6,1 x 6,1) 20 (6,1) 23 (87,1) 11.1 (0,76) 23 (87,1) 11.1 (0,76) For coverage area dimensions less than or between those indicated, use the minimum required flow for the next highest coverage area for which hydraulic design criteria are stated. Requirement is based on minimum flow in GPM (LPM) from each sprinkler. The associated residual pressures are calculated using the nominal K-factor. Refer to Hydraulic Design under the Design Criteria section. For FM residential applications, the greater of 0.1 gpm/ft2 over the design area (i.e., 5xL) or the flow in accordance with the criteria in this table must be used. TABLE C FM APPROVAL WET PIPE SYSTEM SERIES LFII RESIDENTIAL PENDENT AND RECESSED PENDENT SPRINKLERS (TY4234) - HYDRAULIC DESIGN CRITERIA than that below. Down drafts through the Support Cup could delay sprinkler operation in a fire situation. Sprinkler Spacing The minimum spacing between sprin- klers is 8 feet (2,4 m). The maximum spacing between sprinklers cannot exceed the length of the coverage area (Ref. Tables A and B) being hydrauli- cally calculated (e.g., maximum 12 feet for a 12 ft. x 12 ft. coverage area, or 20 feet for a 20 ft. x 20 ft. coverage area). FM APPROVAL CRITERIA The Series LFII (TY4234) Residen- tial Pendent and Recessed Pendent Sprinklers are FM Approved for installation in accordance with the applicable Factory Mutual Loss Pre- vention Data Sheet FM 2-5. Criteria provided by FM may differ from UL and/or NFPA, therefore the designer should review and become familiar with Factory Mutival requirements before proceeding with design. The following information pertaining to System Type, Hydraulic Design, and Sprinkler spacing are provided for ref- erence and are not intended to provide complete installation criteria as provide in the applicable Factory Mutual Loss Prevention Data Sheet. Residential Sprinkler Design Guide When conditions exist that are outside the scope of the provided criteria, refer to the Residential Sprinkler Design Guide TFP490 for the manufactur- er's recommendations that may be acceptable to the local authority having jurisdiction. System Type Only wet pipe systems may be utilized. Hydraulic Design The number of design sprinklers is to be the greater of the four most hydrau- lically demanding sprinklers, or 1500 sq. ft. as per FM Data Sheet 2-5. The minimum required discharge from each of the four sprinklers is to be the greater of the following: The flow rates given in Table C as a function of the maximum allowable coverage area A minimum discharge of 0.1 gpm/ft2. over the "design area" comprised of the four most hydraulically demand- ing sprinklers for the actual coverage areas being protected by the four sprinklers Example No. 1: A corridor being pro- tected is 10 ft. wide; consequently, an actual coverage area of 10 ft. x 20 ft. is being contemplated. Based on using the LFII (TY4234) Residential Pendent Sprinkler, the flow rate provided in Table C for a 20 ft. x 20 ft. coverage area is 23 GPM. However, based on minimum discharge of 0.1 gpm/ft2, the flow rate would be 20 GPM. In this case, a minimum flow rate of 23 GPM for this design sprinkler must be utilized. Example No. 2: A long narrow room being protected is 12 ft. wide; con- sequently, an actual coverage area of 12 ft. x 20 ft. is being contemplated. Based on using the LFII (TY4234) Resi- dential Pendent Sprinkler, the flow rate provided in Table C for a 20 ft. x 20 ft. coverage area is 23 GPM. However, based on minimum discharge of 0.1 gpm/ft2, the flow rate would be 24 GPM. In this case, a minimum flow rate of 24 GPM for this design sprin- kler must be utilized. (In no case shall the design pressure be less than 7 psi.) Sprinkler Spacing The minimum spacing between sprin- klers is 8 feet (2,4 m). The maximum spacing between sprinklers cannot exceed the length of the coverage area (Ref. Table C) being hydraulically calcu- lated (e.g., maximum 12 feet for a 12 ft. x 12 ft. coverage area, or 20 feet for a 20 ft. x 20 ft. coverage area). TFP4OS Page 7 of 8 Installation The TYCO RAPID RESPONSE Series LFII Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers (TY4234) must be installed in accordance with this section. General Instructions Do not install any bulb type sprinkler if the bulb is cracked or there is a loss of liquid from the bulb. With the sprin- kler held horizontally, a small air bubble should be present. The diameter of the air bubble is approximately 1/16 inch (1,6 mm). A leak-tight 3/4 inch NPT sprinkler joint should be obtained by applying a minimum to maximum torque of 10 to 20 ft-lbs. (13,4 to 26,8 Nm). Higher levels of torque may distort the sprin- kler inlet with consequent leakage or impairment of the sprinkler. Do not attempt to compensate for insufficient adjustment in an Escutch- eon Plate by under or over-tightening the Sprinkler. Re-adjust the position of the sprinkler fitting to suit. Series LFII Residential Pendent Sprinklers The Series LFII Residential Pendent Sprinklers must be installed in accordance with the Steps 1 P through 3P. Step 1P. Install pendent sprinklers in the pendent position with the deflector parallel to the ceiling. Step 2P. With pipe thread sealant applied to the pipe threads, hand- tighten the sprinkler into the sprinkler fitting. The sprinkler has been provided with a Sprinkler Strap similar to that shown in Figure 5 for the concealed sprinkler assembly. Refer to NFPA 13 for guid- ance regarding removal of protective straps and caps. As long as the Sprin- kler Strap remains in place, the system is considered to be "Out Of Service". Step 3P. Tighten the sprinkler into the sprinkler fitting using only the W-Type 6 Sprinkler Wrench (Figure 3). With ref- erence to Figure 1, apply the W-Type 6 Sprinkler Wrench to the wrench flats. Refer to Technical Data Sheet TFP700 regarding instructions for the removal of the Sprinkler Strap. Series LFII Residential Recessed Pendent Sprinklers The Series LFII Residential Recessed Pendent Sprinklers must be installed in accordance with Steps 1R through 4R. Step 1R. Install recessed pendent sprinklers in the pendent position with the deflector parallel to the ceiling. Step 2R. After installing the Style 30 Mounting Plate over the sprinkler threads and with pipe thread sealant applied to the pipe threads, hand- tighten the sprinkler into the sprinkler fitting. The recessed sprinkler has been pro- vided with a Sprinkler Strap similar to that shown in Figure 5 for the con- cealed sprinkler assembly. Refer to NFPA 13 for guidance regarding removal of protective straps and caps. As long as the Sprinkler Strap remains in place, the system is considered to be "Out Of Service". Step 3R. Tighten the sprinkler into the sprinkler fitting using only the W-Type 7 Recessed Sprinkler Wrench (Figure 4). With reference to Figure 1, apply the W-Type 7 Recessed Sprinkler Wrench to the sprinkler wrench flats. Step 4R. After the ceiling has been installed or the finish coat has been applied, slide on the Style 30 Closure over the Series LFII Sprinkler and push the Closure over the Mounting Plate until its flange comes in contact with the ceiling. Refer to Technical Data Sheet TFP700 regarding instructions for the removal of the Sprinkler Strap. Series LFII Residential Concealed Pendent Sprinklers The Series LFII Residential Concealed Pendent Sprinklers must be installed in accordance with Steps 1C through 6C. Step 1C. Install the sprinkler in the pendent position and with the center- line of the sprinkler perpendicular to the mounting surface. Step 2C. Remove the Protective Cap. Refer to NFPA 13 for guidance regard- ing removal of protective straps and caps Step 3C. With pipe thread sealant applied to the pipe threads, and using the W-Type 7 Wrench shown in Figure 4, install and tighten the Sprin- kler/Support Cup Assembly into the fitting. The W-Type 7 Wrench will accept a 1/2 inch ratchet drive. Step 4C. Replace the Protective Cap by pushing it upwards until it bottoms out against the Support Cup. The Pro- tective Cap helps prevent damage to the Deflector and Arms during ceiling installation and/or during application of the finish coating of the ceiling. It may also be used to locate the center of the clearance hole by gently pushing the ceiling material against the center point of the Cap. As long as the Sprinkler Strap (Fig. 5) or the Protective Cap (Fig. 6) remains in place, the system is considered to be "Out Of Service". Step 5C. After the ceiling has been completed with the 2-1/2 inch (63 mm) diameter clearance hole and in preparation for installing the Cover Plate/Retainer Assembly, remove and discard the Protective Cap and the Sprinkler Strap. Refer to Technical Data Sheet TFP700 regarding instructions for the removal of the Sprinkler Strap. Step 6C. Push the Cover Plate/Retainer Assembly into the Support Cup, and as necessary, make the final adjustment of the Cover Plate with respect to the ceiling by turning the Cover Plate/ Retainer Assembly clockwise until its flange just comes in contact with the ceiling. If it becomes necessary to remove the Cover Plate, it can be removed by unscrewing in a counter-clockwise direction. If the Cover Plate/Retainer Assembly cannot be engaged with the Support Cup or the Cover Plate/Retainer Assembly cannot be engaged suffi- ciently to contact the ceiling, the Sprin- kler Fitting must be repositioned. TFP4O8 Page 8 of 8 Care and Maintenance The TYCO RAPID RESPONSE Series LFll Residential Pendent, Recessed Pendent, and Concealed Pendent Sprinklers (1Y4234) must be main- tained and serviced in accordance with this section. Before closing a fire protection system main control valve for maintenance work on the fire protection system that it controls, obtain permission to shut down the affected fire protec- tion system from the proper authorities and notify all personnel who may be affected by this action. Absence of a Cover Plate can delay the sprinkler operation in a fire situation. The owner must assure that the sprin- klers are not used for hanging any objects and that the sprinklers are only cleaned by means of gently dusting with a feather duster; otherwise, non- operation in the event of a fire or inad- vertent operation may result. When properly installed, there is a nominal 3/32 inch (2,4 mm) air gap between the lip of the Cover Plate and the ceiling, as shown in Figure 6. This air gap is necessary for proper oper- ation of the sprinkler by allowing heat flow from a fire to pass below and above the Cover Plate to help assure appropriate release of the Cover Plate in a fire situation. If the ceiling needs repainting after sprinkler installation, exercise care to ensure that the new paint does not seal off any of the air gap. Failure to do so may impair sprin- kler operation. Factory painted Cover Plates must not be repainted. They should be replaced, if necessary, by factory painted units. Non-factory applied paint may adversely delay or prevent sprinkler operation in the event of a fire. Do not pull the Cover Plate relative to the Retainer. Separation may result. Sprinklers which are found to be leaking or exhibiting visible signs of corrosion must be replaced. Automatic sprinklers must never be painted, plated, coated, or other- wise altered after leaving the factory. Modified sprinklers must be replaced. Sprinklers that have been exposed to corrosive products of combustion, but have not operated, should be replaced if they cannot be completely cleaned by wiping the sprinkler with a cloth or by brushing it with a soft bristle brush. Care must be exercised to avoid damage to the sprinklers - before, during, and after installation. Sprin- klers damaged by dropping, striking, wrench twist/slippage, or the like, must be replaced. Also, replace any sprin- kler that has a cracked bulb or that has lost liquid from its bulb. (Ref. Installa- tion Section.) The owner is responsible for the inspection, testing, and maintenance of their fire protection system and devices in compliance with this document, as well as with the applicable standards of the National Fire Protection Asso- ciation (e.g., NFPA 25), in addition to the standards of any other authorities having jurisdiction. Contact the install- ing contractor or sprinkler manufac- turer regarding any questions. Automatic sprinkler systems are rec- ommended to be inspected, tested, and maintained by a qualified Inspec- tion Service in accordance with local requirements and/or national codes. Limited Warranty For warranty terms and conditions, visit www.tyco-fire.com. Ordering Procedure Contact your local distributor for avail- ability. When placing an order, indicate the full product name and Part Number (P/N). For pendent sprinkler, order pendent sprinkler assembly plus sprinkler wrench. For recessed pendent sprinkler, order pendent sprinkler assembly plus sep- arately ordered recessed escutcheon plus sprinkler wrench. —s--For concealed pendent sprinkler, order concealed pendent sprinkler assembly plus separately ordered cover plate assembly plus sprinkler wrench. Pendent Sprinkler Assembly Specify: Series LFll (TY4234), K=6.9, Residential Pendent Sprinkler, (specify) temperature rating, (specify) finish, P/N (specify): 155°F (68°C) Natural Brass ................. 51-069-1 -155 Pure White (RAL9010) (a) 51-069-3-155 Signal White (RAL9003) ......... 51 -069-4-155 Chrome Plated ................51-069-9-155 175°F (79°C) Natural Brass .................51-069-1-175 Pure White (RAL9010) (a) 51-069-3-175 Signal White (RAL9003) ....... ..51-069-4-175 Chrome Plated ................51 -069-9-175 (a) Eastern Hemisphere sales only. Concealed Pendent Sprinkler Assembly: Specify: Series LFII (TY4234), K=6.9, Residential Concealed Pendent Sprin- kler, (specify) temperature rating without Cover Plate Assembly, P/N (specify): 155°F (68°C)..................51-068-1-155 175°F(79°C) ..................51 -068-1-175 Separately Ordered Recessed Escutcheon: Specify: Style 30 Recessed Escutch- eon with (specify*) finish, P/N (specify*) *Refer to Technical Data Sheet TFP770. Separately Ordered Cover Plate Assembly: Specify: 139°F (58°C), Cover Plate Assembly having a (specify) finish for the Series LFll (TY4234), K=6.9, Resi- dential Concealed Pendent Sprinkler, P/N (specify): Grey White (RAL9002)..........56-873-0-135 Pure White (HAL 9010) (a) 56-873-3-135 Signal White (HAL 9003) ........56-873-4-135 Chrome......................56-873-9-135 Custom .....................56-873-X-135 (a) Eastern Hemisphere sales only. Separately Ordered Sprinkler Wrench: Specify: W-Type 6 Sprinkler Wrench, P/N 56-000-6-387 (For pendent sprinklers) Specify: W-Type 7 Sprinkler Wrench, P/N 56-850-4-001 (For recessed pendent sprinklers and concealed pendent sprinklers) GLOBAL HEADQUARTERS 11400 Pennbrook Parkway, Lansdale, PA 19446 I Telephone +1-215-362-0700 Copyright © 2016 Tyco Fire Products, LP. All rights reserved. tyco TEFLON is trademark of The DuPont Corporation Fire Protection Products ltqc MEN I Worldwide www.tyco-fire.com Contacts Series RFII - 56 K-factor "Ro al Flush Il" Concealed Pendent Sprinklers Quick Standard Response, Standard Coverage General Description The TYCO Series RFII 5.6 K-factor, "Royal Flush II" Concealed Pendent Sprinklers Quick Response (3-mm bulb) and Standard Response (5-mm bulb), are decorative sprinklers featur- ing a flat cover plate designed to con- ceal the sprinkler. These sprinklers are optimal for architecturally sensitive ar- eas such as hotel lobbies, office build- ings, churches, and restaurants. Each sprinkler includes a Cover Plate! Retainer Assembly and a Sprinkler! Support Cup Assembly. The separa- ble, two-piece assembly design pro- vides the following benefits: Allows installation of the sprinklers and pressure testing of the fire pro- tection system prior to installation of a suspended ceiling or applica- tion of the finish coating to a fixed ceiling. Permits the removal of suspended ceiling panels for access to building service equipment without having to first shut down the fire protection system and remove sprinklers. Provides for 1/2 inch (12,7 mm) of vertical adjustment to allow a mea- sure of flexibility in determining the length of fixed piping to cut for the sprinkler drops. The Series RFII Sprinklers are shipped with a Disposable Protective Cap. The Protective Cap is temporarily removed during installation and replaced to help protect the sprinkler during ceiling in- IMPORTANT Always refer to Technical Data Sheet TFP700 for the "INSTALLER WARNING" that provides cautions with respect to handling and instal- lation of sprinkler systems and com- ponents. Improper handling and in- stallation can permanently damage a sprinkler system or its components and cause the sprinkler to fall to operate in a fire situation or cause it to operate prematurely. Page 1 of 4 stallation or finish. The tip of the Pro- tective Cap can be used to mark the center of the ceiling hole into plaster board or ceiling tiles by gently push- ing the ceiling product against the Pro- tective Cap. When ceiling installation is complete, the Protective Cap is re- moved and the Cover Plate/Retainer Assembly is installed. As an option, the Series RFll Standard Response (5-mm bulb) "Royal Flush II" Concealed Pendent Sprinklers can be fitted with a silicone Air and Dust Seal. (Refer to Figure 5.) The Air and Dust Seal is intended for sensitive areas where it is desirable to prevent air and dust from the area above the ceiling to pass through the cover plate. The Series RFll Concealed Pendent Sprinklers described herein must be installed and maintained in compli- ance with this document and with the applicable standards of the National Fire Protection Association, in addi- tion to the standards of any author? - ties having jurisdiction. Failure to do so may impair the performance of these devices. The owner is responsible for maintain- ing their fire protection system and de- vices in proper operating condition. The installing contractor or sprinkler manufacturer should be contacted with any questions. Sprinkler Identification Numb r SIN) TY3531 - 3 mm bulb Technical Data Sprinkler Approvals Approvals apply only to the service conditions indicated in the Design Cri- teria section. MARCH 2013 TY3531 (3-mm Bulb) is UL Listed, C-UL Listed, VdS Approved (Certif- icate No. G4090007), and NYC Ap- proved (MEA 353-01-E) as Quick Response. TY3531 (3-mm Bulb) is FM and LPCB Approved (Ref. No. 094a/10) Approved as Standard Response. Factory Mutual and LPCB do not approve any concealed sprinklers for quick response. 1Y3551 (5-mm Bulb) is UL Listed, C-UL Listed, FM Approved, LPCB Approved (Ref. No. 094a!9), and NYC Approved (MEA 353-01-E) as Standard Response. Approvals for Air and Dust Seal UL and C-UL Listed for use with the RFll Standard Response Concealed Sprinkler (TY3551). Maximum Working Pressure Maximum 250 psi (17,3 bar) by UL, C-UL, and NYC Maximum 175 psi (12,1 bar) by FM, VdS, and LPCB Temperature Rating 155°F (68°C) Sprinkler with 139°F (59°C) Plate 200°F (93°C) Sprinkler with 165°F (74°C) Plate Discharge Coefficient K= 5.6 GPM/psi112 (80,6 LPM/bar112) Adjustment 1/2 inch (12,7 mm) Finishes See the Ordering Procedure section. TFPISI TFPI.81 Page 2 of 4 Physical Characteristics Frame ...................Bronze Support Cup..............Chrome Plated Steel Guide Pins .........Stainless Steel Deflector.................Bronze Compression Screw.........Brass Bulb ......................Glass Cap.............Bronze or Copper Sealing Assembly.........Beryllium Nickel w/ TEFLON Cover Plate................Brass Retainer ..................Brass Ejection Spring......Stainless Steel Design Criteria The TYCO Series RFII 5.6 K-factor, "Royal Flush II" Concealed Pendent Sprinklers are intended for fire protec- tion systems designed in accordance with the standard installation rules rec- ognized by the applicable Listing or Approval agency; for example, UL List- ing is based on NFPA 13 and VdS Ap- proval is based on the CEA 4001. For more information on LPCB and VdS Approvals, contact Tyco Fire Pro- tection Products at the following office: Enschede, Netherlands Telephone: 31-53-428-4444 Fax: 31-53-428-3377 The Series RFII Concealed Pendent Sprinklers are only listed and approved with the Series RFII Concealed Cover Plates having a factory applied finish. Do not use the Series RFII in applica- tions where the air pressure above the ceiling is greater than that be- low. Down drafts through the Sprin- kler/Support Cup Assembly can delay sprinkler operation in a fire situation. Operation When exposed to heat from a fire, the Cover Plate, normally soldered to the Retainer at three points, falls away to expose the Sprinkler/Support Cup Assembly. The Deflector - supported by the Guide Pins - then drops down to its operational position. The glass bulb contains a fluid that ex- pands when exposed to heat. When the rated temperature is reached, the fluid expands sufficiently to shatter the glass bulb, activating the sprinkler and allowing water to flow. 1/2 NPT FRAME SUPPOR CUP WITI ROLL FORIV THREADS GUIDE PINS (2) Installation The TYCO Series RFII 5.6 K-factor, "Royal Flush II" Concealed Pendent Sprinklers must be installed in accor- dance with this section. General Instructions Do not install any bulb-type sprinkler if the bulb is cracked or there is a loss of liquid from the bulb. With the sprin- kler held horizontally, a small air bub- ble should be present. The diameter of the air bubble is approximately 1/16 inch (1,6 mm) for the 155°F (68°C) and 3/32 inch (2,4 mm) for the 200°F (93°C) temperature ratings. A leak-tight 1/2 inch NPT sprinkler joint should be obtained by applying a min- imum to maximum torque of 7 to 14 ft.-Ibs. (9,5 to 19,0 Nm). Higher levels of torque can distort the sprinkler In- let with consequent leakage or impair- ment of the sprinkler. Do not attempt to, compensate for in- sufficient adjustment in the Sprinkler by under- or over-tightening the Sprin- kler/Support Cup Assembly. Re-adjust the position of the sprinkler fitting to suit. Step 1. Install the sprinkler only in the pendent position with the center-line of the sprinkler perpendicular to the mounting surface. Step 2. Remove the Protective Cap. Step 3. With pipe thread sealant ap- plied to the pipe threads, hand-tighten the sprinkler into the sprinkler fitting. Step 4. Wrench-tighten the sprinkler using only the RFII Sprinkler Wrench. (Refer to Figure 3.) Apply the RFII Sprinkler Wrench to the Sprinkler as shown in Figure 3. Step 5. Replace the Protective Cap by pushing it upwards until it bottoms out against the Support Cup. (Refer to Figure 4.) The Protective Cap helps prevent damage to the Deflector and DEFLECTOR II SPRINKLER/SUPPORT CUP ASSEMBLY LECTOR ROPPED POSITION) EALING SEMBLY CAP BULB PRESSION CREW THREAD INTO fl RETAINER SUPPORT Ii WITH THREAD CUP UNTIL 0 0 'ti_— DIMPLES MOUNTING SURFACE IS EJECTION FLUSH WITH SPRING CEILING SOLDER COVER TABS (3) COVER PLATE/RETAINER PLATE ASSEMBLY FIGURE 1 MODEL RFII CONCEALED SPRINKLER ASSEMBLY T_7~ 3/16" to 11/16" (4,8 to 17,5 mm) REFERENCE COVER PLATE PROFILE DEPTH DIMENSION B I I V MANUFACTURER DEFLECTOR COVER PLATE PRESET GAP IN DROPPED RETAINER 3/32 (2,4 mm) POSITION ASSEMBLY COVER PLATE DIAMETER DIMENSION A 3-1/4 inches (82,6 mm) C: 2-3/8 to 2-5/8 inches (60,3 to 66,7 mm) 3/16 inches (4,8 mm) D: 1-3/4 to 2-1/4 inches (44,5 to 57,2 mm) FIGURE 2 SERIES CONCEALED SPRINKLER INSTALLATION DIMENSIONS TFPI8I Page 3 of 4 FACE OF SPRINKLER FITTING SPRINKLER SUPPORT CUP ASSEMBLY 1/2 (12,7 mm) THREADED D ADJUSTMENT FACE OF CEILING, RETAINING RING MOUNTING SURFACE CLEARANCE HOLE - DIAMETER - DIMENSION C Arms during ceiling installation and/or finish. You can also use the Protective Cap to locate the center of the clear- ance hole by gently pushing the ceiling material up against the center point of the Protective Cap. L'(.)tL.i As long as the Protective Cap remains in place, the system is considered "Out of Service". Step 6. After the ceiling has been com- pleted with the 2-1/2 inch (63,5 mm) di- ameter clearance hole and in prepa- ration for installing the Cover Plate! Retainer Assembly, remove and dis- card the Protective Cap. Verify that the Deflector moves up and down freely. If the Sprinkler is damaged and the Deflector does not move up and down freely, replace the entire Sprinkler. Do not attempt to modify or repair a damaged sprinkler. Step 7. When installing an Air and Dust Seal, refer to Figure 5; otherwise, proceed to Step 8. To attach the Air and Dust Seal, verify the angle of the outside edge of the seal is oriented ac- cording to Figure 5. Start the edge of the Retainer in the grooved slot of the Air and Dust Seal and continue around the retainer until the entire Air and Dust Seal is engaged. Step 8. Screw on the Cover Plate! Retainer Assembly until the Retainer (shown in Figure 2) or the Air and Dust Seal (shown in Figure 5) contacts the ceiling. Do not continue to screw on the Cover Plate/Retainer Assembly so that it lifts a ceiling panel out of its normal position. If you cannot engage the Cover Plate/Retainer Assembly with the Support Cup or you cannot engage the Cover Plate/Retainer As- sembly sufficiently to contact the ceil- ing, you must reposition the Sprinkler Fitting. TFPIBI Page 4 of 4 SUPPORT SPRINKLER FACE OF ORIENT CUP CEILING BEVEL AS COVER SHOWN PLATE SEMBLY Ac AIR AND DUST SEAL LIP OF COVER RETAINER PLATE FIGURE 5 OPTIONAL AIR AND DUST SEAL FOR SERIES RFII (TY3551) Care and Maintenance The TYCO Series RFII 5.6 K-fac- tor, "Royal Flush II" Concealed Pen- dent Sprinklers must be maintained and serviced in accordance with this section. Before closing a fire protection system main control valve for maintenance work on the fire protection system that it controls, obtain permission to shut down the affected fire protection sys- tem from the proper authorities and notify all personnel who may be affect- ed by this action. Absence of the Cover Plate/Retainer Assembly can delay sprinkler opera- tion in a fire situation. When properly installed, there is a nominal 3/32 inch (2,4 mm) air gap be- tween the lip of the Cover Plate and the ceiling, as shown in Figure 2. This air gap is necessary for proper operation of the sprinkler. If the ceil- ing requires repainting after sprinkler installation, ensure that the new paint does not seal off any of the air gap. Do not pull the Cover Plate relative to the Enclosure. Separation may result. Sprinklers which are found to be leak- ing or exhibiting visible signs of corro- sion must be replaced. Automatic sprinklers must never be painted, plated, coated, or other- wise altered after leaving the factory. Modified sprinklers must be replaced. Sprinklers that have been exposed to corrosive products of combustion, but have not operated, should be replaced if they cannot be completely cleaned by wiping the sprinkler with a cloth or by brushing it with a soft bristle brush. Care must be exercised to avoid dam- age to the sprinklers - before, during, and after installation. Sprinklers dam- aged by dropping, striking, wrench twist/slippage, or the like, must be re- placed. Also, replace any sprinkler that has a cracked bulb or that has lost liquid from its bulb. (Ref. Installation Section.) Exercise care to avoid damage to sprinklers before, during, and after in- stallation. Replace sprinklers damaged by dropping, striking, wrench twisting, wrench slipping, or the like. Also, re- place any sprinkler that has a cracked bulb or that has lost liquid from its bulb. (Refer to the Installation section.) Ordering Procedure Contact your local distributor for availability. When placing an order, indicate the full product name. Sprinkler/Support Cup Assembly Specify: Series RFII (specify SIN), K=5.6, "Royal Flush II" Pendent Sprin- klers (specify) temperature rating and (specify) finish, P/N (specify). 155°F (68°C) 200°F (93°C) 1Y3531 51-792-1-155 51-792-1-200 TY3551 51-790-1-155 51-790-1-200 Separately Ordered Cover Plate/ Retainer Assembly: Specify: (temperature rating from be- low) Series RFII Concealed Cover Plate with (finish), P/N (specify). 139°F (59°C)(a) 165°F (74°C)(b) Grey White (RAL9002) .... 56-792-0-135 56-792-0-165 Brass..........56-792-1-135 56-792-1-165 Pure White (c) (RAL9010) .... 56-792-3-135 56-792-3-165 Signal White (RAL9003) .... 56-792-4-135 56-792-4-165 Jet Black (RAL9005) .... 56-792-6-135 59-792-6-165 Brushed Chrome ........56-792-8-135 56-792-8-165 Chrome ........56-792-9-135 56-792-9-165 Custom ........56-792-X-135 56-792-X-165 For use with 155°F (68°C) sprinklers. For use with 200°F (93°C) sprinklers. Eastern Hemisphere sales only. Sprinkler Wrench Specify: RFII Sprinkler Wrench, P/N 56-000-1-075. Air and Dust Seal Specify: Air and Dust Seal, P/N 56-908-1-001. If you must remove a sprinkler, do not reinstall it or a replacement without re- installing the Cover Plate/Retainer As- sembly. If a Cover Plate/Retainer As- sembly becomes dislodged during service, replace it immediately. The owner is responsible for the in- spection, testing, and maintenance of their fire protection system and devic- es in compliance with this document, as well as with the applicable stan- dards of the National Fire Protection Association (e.g., NFPA 25), in addition to the standards of any other authori- ties having jurisdiction. Contact the in- stalling contractor or sprinkler manu- facturer regarding any questions. Automatic sprinkler systems should be inspected, tested, and maintained by a qualified Inspection Service in accor- dance with local requirements and/or national code. GLOBAL HEADQUARTERS 11400 Pennbrook Parkway, Lansdale, PA 19446 1 Telephone +1-215-362-0700 Copyright © 2013 Tyco Fire Products, LP. All rights reserved. tqcc, TEFLON is trademark of The DuPont Corporation. L'L.)tL.J The Series TY-FRL Sprinklers de- scribed herein must be installed and maintained in compliance with this document, as well as with the appli- cable standards of the National Fire Protection Association, in addition to the standards of any other authorities having jurisdiction. Failure to do so may impair the performance of these devices. The owner is responsible for main- taining their fire protection system and devices in proper operating con- dition. Contact the installing contrac- tor or sprinkler manufacturer with any questions. ing. It uses a two-piece Style 20 (1/2 inch NPT) Recessed Escutcheon. The Sprinkler Recessed Escutcheon provides 1/4 inch (6,4 mm) of recessed adjustment Identification or up to 1/2 inch (12,7 mm) of total ad- justment from the flush pen Numbers dent position. The adjustment provid- ed by the Recessed Escutcheon re- TY1121...... Upright 2.8K, 1/2"NPT duces the accuracy to which the fixed pipe drops to the sprinklers must cut. An intermediate level version of the 5.6 and 8.0 K-factor, Series TY-FRL Pendent Sprinkler can be obtained by utilizing the Series TY-FRL Pen- dent Sprinkler in combination with the Model S4 Shield. The TYCO Series TY-FRL, 2.8, 5.6, and 8.0 K-factor, Upright and Pendent Sprinklers described in this data sheet are quick response, standard cover- age, solder type spray sprinklers de- signed for use in light and ordinary hazard commercial occupancies such as banks, hotels, shopping malls, schools, hospitals, etc. The recessed version of the 2.8 and 5.6 K-factor, Series TY-FRL Pendent Sprinkler, where applicable, is intend- ed for use in areas with a finished ceil- General Description IMPORTANT Always refer to Technical Data Sheet TFP 700 for the "INSTALLER WARNING" that provides cau- tions with respect to handling and installation of sprinkler sys- tems and components. Improp- er handling and installation can permanently damage a sprin- kler system or its components and cause the sprinkler to fail to operate in a fire situation or cause it to operate prematurely. TY4121......Upright 8.0K, 3/4"NPT 1Y4221 .... Pendent 8.0K, 3/4"NPT TY1121 is a redesignation for S1879 and G8973. TY1221 is a redesignation for S1880 and G8971. TY3121 is a redesignation for S1864 and G8974. TY3221 is a redesignation for S1865 and G8972. TY4121 is a redesignation for S1866 and G8174. TY4221 is a redesignation for S1867 and G8172. Page 1 of 6 OCTOBER 2013 TFPI3O tuca Fire Protection Products Worldwide Contacts I www.tyco-fire.com Series TY-FRL - 2.8,y 5.6,, and 80 K-factor Upright, Pendent, and Recessed Pendent Sprinklers Quick Response, Standard Coverage 1 - Frame 5 - Link 7 - Button 2 - Strut Assembly 8 - Seal 3 - Deflector' 6 - Ejection 4 - Hook Spring WREN( AREA STYLE 2C RECESSEI TFPI3O Page 2 of 6 * Temperature rating ** Pipe thread connections per is indicated on ISO 7-1 can be provided on ESCUTCHEON Deflector, special request. 01 ATI QTKII DEFLECTOR * SURFACE 1 - Frame 5 - Link 7 - Button 2 - Strut Assembly 8 - Seal 3 - Deflector 6 - Ejection 9 - Bushing 4 - Hook Spring 9, I' 1 2-11/16" (68,3 mm) 2" (50,8 mm) WRENCH AREA. UPR 2-11/1€ (68,3 mr I 7/16" ) (11,1 mm) NOMINAL MAKE-IN 1/2 NPT** I WRENCH DEFLE( FLANGES IGHT PENDENT RECESSED PENDENT CROSS SECTION STYLE 20 RECESSED L___ ESCUTCHEON TOR* 2- 7/8" (73,0 mm) DIA. FIGURE 1 QUICK RESPONSE SERIES TY-FRL UPRIGHT (TYI12I) AND PENDENT (TY1221) SPRINKLERS 2.8 K-FACTOR, 1/2 INCH NPT * Temperature rating is indicated on Deflector. ** Pipe thread connections per 1S07-1 ct i special re ci, lie PIUVIUCIJ UI I ESCUTCHEON quest. PLATE SEATING SURFACE I-L (68,3 mm) (50,8 mm) —Ld L DEFLECTOR* .-2-7/8 FLANGES UPRIGHT PENDENT DEFLECTOR * 2-11/1€ (68,3 mr 7/16' (11,1 mm) I NOMINAL I MAKE-IN I * 1/2' NPT** WRENCH RECESSED PENDENT CROSS SECTION ESCUTCHB V (73,0 mm) DIA. FIGURE 2 QUICK RESPONSE SERIES TY-FRL UPRIGHT (TY3 121) AND PENDENT (TY3221) SPRINKLERS 5.6 K-FACTOR, 1/2 INCH NPT DEFLECTOR * 2-13/16' (71,4 mm) 1/2" (12,7 mm) NOMINAL MAKE-IN HWRENCH FLANGES CEILING PLATE SEATING SURFACE /WRENCI 2-15/16 (74,6 mm) 2-3/16" (55,6 mm) DEFLECTOR * 1 - Frame 6 - Ejection 2 - Strut Spring 1 - Deflector* 7 - Button 4 -Hook 8-Seal 5 - Link 8 Assembly 7 * Temperature rating is indicated on Deflector. 2 ** Pipe thread connections per ISO 7-1 can be provided on special request. 3* 3/4" NPT' TFPI3O Page 3 of 6 UPRIGHT PENDENT CROSS SECTION FIGURE 3 QUICK RESPONSE SERIES TY-FRL UPRIGHT (TY4121) AND PENDENT (TY4221) SPRINKLERS 8.0 K-FACTOR, 3/4 INCH NPT Technical Data Approvals UL and C-UL Listed. FM, NYC, and LPCB Approved. (Refer to Table A for complete approval information includ- ing corrosion resistant status.) Maximum Working Pressure 175 psi (12,1 bar) Discharge Coefficient K = 2.8 GPM/psil'2 (40,3 LPM/barll2) K = 5.6 GPM/p5i112 (80,6 LPM/barl'2) K = 8.0 GPM/p51112 (115,2 LPM/bar112) Temperature Ratings Refer to Table A Finishes Sprinkler: Refer to Table A Recessed Escutcheon: White Coated, Chrome Plated, or Brass Plated Physical Characteristics Frame .......................Bronze Strut .........................Monel Deflector .................... .Bronze Hook.........................Monel Link Assembly .................Nickel Ejection Spring................Inconel Button.......................Bronze Seal .......................TEFLON Bushing (2.8K only) .............Brass Operation The fusible link (heat collector) assem- bly is comprised of two halves that are joined together by a thin layer of solder. When the rated temperature is reached, the solder melts and the two link halves separate, allowing the sprinkler to operate. Design Criteria The TYCO Series TY-FRL Pendent and Upright Sprinklers are intended for fire protection systems designed in accordance with the standard instal- lation rules recognized by the appli- cable Listing or Approval agency (e.g., UL Listing is based on the require- ments of NFPA 13, and FM Approval is based on the requirements of FM's Loss Prevention Data Sheets). Only the Style 20 Recessed Escutcheon, as applicable, is to be used for recessed pendent installations. Installation The TYCO Series TY-FRL Sprinklers must be installed in accordance with- this section. A leak tight 1/2 inch NPT sprinkler joint should be obtained with a torque of 7 to 14 ft./lbs. (9,5 to 19,0 Nm). A leak tight 3/4 inch NPT sprinkler joint should be obtained with a torque of 10 to 20 ft./lbs. (13,4 to 26,8 Nm). Higher levels of torque may distort the sprin- kler inlet and cause leakage or impair- ment of the sprinkler. Do not attempt to make-up for insuf- ficient adjustment in the escutcheon plate by under-or over-tightening the sprinkler. Readjust the position of the sprinkler fitting to suit. Series TY-FRL Pendent and Upright Sprinkler Installation The Series TY-FRL Pendent and Up- right Sprinklers must be installed in accordance with this section. Step 1. Pendent sprinklers are to be installed in the pendent position, and upright sprinklers are to be installed in the upright position. Step 2. With pipe thread sealant ap- plied to the pipe threads, hand tighten the sprinkler into the sprinkler fitting. Step 3. Tighten the sprinkler into the sprinkler fitting using only the W-Type 9 Sprinkler Wrench (Ref. Figure 6). With reference to Figures 1, 2, and 3, the W-Type 9 Sprinkler Wrench is to be applied to the wrench area. TFP13O Page 4 of 6 SPRINKLER FINISH K TYPE TEMP. FRAME NATURAL CHROME RATING COLOR BRASS PLATED CODE PENDENT 165°F (74°C) Unpainted (TY1221) 212°F (100-C) White 28 UPRIGHT 165F (74°C) Unpainted 212°F(100°C) White NPT RECESSED 165°F (74°C) Unpainted PENDENT 212°F (100°C) White - (TY1221 w/Style 20) PENDENT 165°F (74°C) Unpainted 1, 2, 3, 4, 5 (TY3221) 212°F (100°C) White 1, 2, 3, 5 5.6 UPRIGHT 165°F (74°C) Unpainted 1, 2, 3, 4, 5 NPT (TY3121) 212°F (100°C) White 1, 2, 3, 5 RECESSED 165°F (74°C) Unpainted PENDENT 1,2,5 (TY3221 w/Style 20) 212°F (100°C) White PENDENT 165°F (74°C) Unpainted 8.0 (TY4221) 212°F (100°C) White 3/4" 1,2,3,5 NPT UPRIGHT 165°F (74°C) Unpainted 212°F (100°C) White (TY4121) NOTES: Listed by Underwriters Laboratories, Inc. (UL) as Quick Response Sprinklers Listed by Underwriters Laboratories, Inc. for use in Canada (C-UL) as Quick Response Sprinklers. Approved by Factory Mutual Research Corporation (FM) as Quick Response Sprinklers. Approved by the Loss Prevention Certification Board (LPCB Ref. No. 094a/03) as Quick Response Sprinklers. Approved by the City of New York under MEA 112-04-E. TABLE A LABORATORY LISTINGS AND APPROVALS Series TY-FRL Recessed Pendent Sprinkler Installation The Series TY-FRL Recessed Pendent Sprinklers must be installed in accor- dance with the following instructions. Step A. After installing the Style 20 Mounting Plate, as applicable, over the sprinkler threads and with pipe thread sealant applied to the pipe threads, hand tighten the sprinkler into the sprinkler fitting. Step B. Tighten the sprinkler into the sprinkler fitting using only the W-Type 12 Recessed Sprinkler Wrench (Ref. Figure 7). With reference to Figure 1, or 2, the W-Type 12 Recessed Sprin- kler Wrench is to be applied to the sprinkler wrenching flanges. Step C. After the ceiling has been in- stalled or the finish coat has been ap- plied, slide on the Style 20 Escutch- eon over the Series TY-FRL Sprinkler and push the Escutcheon over the Mounting Plate until its flange comes in contact with the ceiling. 1/2±1/8 2-7/8' DIA. 1/2 (12,7 mm) (12,7±3,2 mm) (73,0 mm) 1/4' (6,4 mm) FACE OF 2-1/4 DIA. MOUNTING I PLATE I SPRINKLER / 57,2 mm I FITTING 1/8 MOUNTING SURFACE CLOSURE TY-FRL FIGURE 4 SERIES TY-FRL (TY1221) RECESSED PENDENT SPRINKLER ASSEMBLY WITH TWO-PIECE 1/2 INCH TOTAL ADJUSTMENT STYLE 20 RECESSED ESCUTCHEON 2.8 K-FACTOR, 1/2 INCH NPT 1/2±1/8' 2-7/8' DIA. 1/2 (12,7 mm) (12,7±3,2 mm) (73,0 mm) 1/4 (6,4 mm) FACE OF 2-1/4" DIA. _ MOUNTING SPRINKLER [ (57,2 mm) PLATE FITTING iTi MOUNTING SURFACE UI MM) / t I 1-3/4(44,5mm) 1-1/2" (38,1 mm) CLOSURE TY-FRL FIGURE 5 SERIES TY-FRL (TY3221) RECESSED PENDENT SPRINKLER ASSEMBLY WITH TWO-PIECE 1/2 INCH TOTAL ADJUSTMENT STYLE 20 RECESSED ESCUTCHEON 5.6 K-FACTOR, 1/2 INCH NPT TFPI3O Page 5 of 6 Care and Maintenance The TYCO Series TY-FRL Sprinklers must be maintained and serviced in accordance with this section. Before closing a fire protection sys- tem main control valve for mainte- nance work on the fire protection sys- tem that it controls, permission to shut down the affected fire protection sys- tem must be obtained from the prop- er authorities and all personnel who may be affected by this action must be notified. Absence of an escutcheon, which is used to cover a clearance hole, may delay the time to sprinkler operation in a fire situation. Sprinklers that are found to be leaking or exhibiting visible signs of corrosion must be replaced. Automatic sprinklers must never be painted, plated, coated or otherwise altered after leaving the factory. Modi- fied or over-heated sprinklers must be replaced. Care must be exercised to avoid dam- age to the sprinklers -before, during, and after installation. Sprinklers dam- aged by dropping, striking, wrench twist/slippage, or the like, must be replaced. The owner is responsible for the in- spection, testing, and maintenance of their fire protection system and de- vices in compliance with this docu- ment, as well as with the applicable standards of the National Fire Pro- WRENCH RECESS T z PUSH WRENCH UP TO ENSURE ENGAGEMENT WITH SPRINKLER WRENCHING AREA FIGURE 7 W-TYPE 12 RECESSED SPRINKLER WRENCH tection Association (e.g., NFPA 25), in addition to the standards of any oth- er authorities having jurisdiction. The installing contractor or sprinkler man- ufacturer should be contacted relative to any questions. It is recommended that automatic sprinkler systems be inspected, test- ed, and maintained by a qualified In- spection Service in accordance with local requirements and/or national codes. TPFI3O Page 6 of 6 P/N 58 - XXX - X - XXX SIN SPRINKLER TEMPERATURE I I 973 2.8K UPRIGHT (1/2"NPT) TY1121 NATURAL BRAS S RATING _________________ I I r 981 2.8K PENDENT (112"NPT) TY1221 CHROME PLATED ________________________ 65 165°F(74°C) 212 974 5.6K UPRIGHT (112"NPT) TY3121 212-F (100-C) _____________________ 982 5.6K PENDENT (1/2-NP T) TY3221 174 8.0K UPRIGHT (314"NPT) 1Y4121 172 8.0K PENDENT (3/4"NPT) TY4221 TABLE B SERIES TY-FRL PENDENT AND UPRIGHT SPRINKLERS PART NUMBER SELECTION Ordering Procedure Contact your local distributor for avail- ability. When placing an order, indi- cate the full product name and Part Number (P/N). Sprinkler Assemblies with NPT Thread Connections Specify: Series TY-FRL (specify SIN), (specify K-factor), (specify Up- right, Pendent, or Recessed Pendent) Sprinkler Quick Response, (specify) temperature rating, (specify type of finish), P/N (specify from Table B) Recessed Escutcheon Specify: Style 20 Recessed Es- cutcheon with (specify*) finish, P/N (specify*) *Refer to Technical Data Sheet TFP770 Sprinkler Wrench Specify: W-Type 9 Sprinkler Wrench, P/N 56-000-1-849 Specify: W-Type 12 Sprinkler Wrench, P/N 56-798-1-001 GLOBAL HEADQUARTERS 11400 Pennbrook Parkway, Lansdale, PA 19446 I Telephone +1-215-362-0700 Copyright © 2013 Tyco Fire Products, LP. All rights reserved. tyco TEFLON is trademark of The DuPont Corporation. Fire Protection Products t1goo Fire Protection Products Worldwide www.tyco-fire.com Contacts Models BB, SD, HIP, and AP Specific Application Sprinklers For Protecting Attics General Description The TYCO Model BB (Back to Back), SD (Single Directional), HIP, and AP (Attic Plus) Specific Application Sprin- klers for Protecting Attics are fire sprinklers for combustible and non- combustible sloped attic spaces. The Model BB, SD, and HIP are Specific Application Attic Sprinklers, whereas the Model AP is a Specific Applica- tion Combustible Concealed Space Sprinkler having specific applica- tion criteria for its use with the Mod- els BB, SD, and HIP in attic spaces. Specific Application Attic Sprinklers provide superior fire protection in attic spaces, and when compared to Stan- dard Spray Sprinklers, cost savings are achieved by eliminating branch- line materials and the associated in- stallation labor. The Specific Applica- tion Sprinklers for Protecting Attics have undergone the most extensive fire testing ever performed for sloped attic spaces. They are UL Listed with their specific application guidelines for use as special sprinklers as defined by the National Fire Protection Associa- tion (NFPA). The Specific Application Attic Sprin- klers provide an extended coverage spacing alternative to the restricted spacing of Standard Spray Sprinklers. The restricted spacings of Standard Spray Sprinklers used within attics is described in the 2007 edition of NFPA 13, Table 8.6.2.2.1(a) and Section 8.6.4.1.4. IMPORTANT Always refer to Technical Data Sheet TFP700 for the "INSTALLER WARNING" that provides cau- tions with respect to handling and installation of sprinkler sys- tems and components. Improp- er handling and installation can permanently damage a sprin- kler system or its components and cause the sprinkler to fall to operate in a fire situation or cause it to operate prematurely. Page 1 of 28 The Specific Application Attic Sprin- klers are the first sprinklers to be: Listed for extended coverage in combustible construction Full-scale fire tested in both wet and dry system scenarios Full-scale tested for use in wood truss construction Listed for specific roof slopes (Ref. Table A) The Specific Application Attic Sprin- klers provide the best level of pro- tection, and control cost by eliminat- ing the need for additional sprinklers and branchline piping. In many cas- es, an attic can be entirely protected with just one line of piping located be- low the peak of the roof using Model BB (Back to Back) Sprinklers. If there is a need for Model SD (Single Direc- tional) or Model HIP Sprinklers, one line of either of these sprinkler types is sufficient at each area being cov- ered. For example and assuming the use of Standard Spray Sprinklers, a system in a 60 foot (18,3 m) wide attic, with up to a 12:12 roof pitch, designed to the 2007 edition of NFPA 13, would require seven branchlines to cover the main portion of the attic and several additional branchlines to cover the hip areas. With the Specific Application Attic Sprinklers, the required coverage can be obtained with just one branch- line running below the peak and one down each slope of the hip beam. This would result in approximately 90% less pipe needed for installation. This reduction in the number of branch- lines saves the cost of the pipe, fit- tings, hangers, and associated labor by eliminating up to five branchlines. Another important aspect of the Spe- cific Application Attic Sprinkler tech- nology is the reduction in system volume. This volume reduction may result in reducing the size of a dry pipe valve (and air compressor) and possibly allow for quicker water deliv- ery times, eliminating the need for an accelerator. AUGUST 2014 111 TFP6IO TFP61O Page 2 of 28 I Components: I 1 -Frame 4-Bulb I I 2 - Button 5 - Compression I I3 - Sealing Screw Assembly 6 - Deflector 2-1/4' 1-5/8' (57,2 mm) H(41,3 rnrn)'i 1-1/8 FLOW \ I 13/16" (28,6 mm) (20,6 mm) FLOW t 6 2-1 8,, 2 (54,0 mm) THREAD RELIEF mm)] /4SNPT NOMINAL MAKE-IN WRENCH FRAME CROSS FLATS ARMS SECTION ELEVATION FIGURE A MODELS BB1, BB2 & BB3 WITH 8.0 K-FACTOR SPECIFIC APPLICATION ATTIC SPRINKLERS Components: 1 - Frame 4 - Bulb 2 - Button 5 - Compression 3 - Sealing Screw Assembly 6 - Deflector 2-1/4" 1-5/8' (57,2 mm) mm) 1-1/8" J 13/16' ____ (28,6 mm) (20,6m V11 I "J 6 ' tf FLO FLOW * 2-1/8" 2 THREA (54,0 mm) : D RELIEF L '1 7/16(11,1 mm)] /1/2" NPT / NOMINAL MAKE-IN WRENCH FRAME FLATS ARMS CROSS SECTION ELEVATION FIGURE C MODELS BB I, 862 & BB3 WITH 4.2 K-FACTOR SPECIFIC APPLICATION ATTIC SPRINKLERS Components: 1 - Body 5 - Compression 8 - Deflector 2 - Cap Screw 9 - Rivet 3 - Sealing 6 - Lever 10 - Diffuser Assembly 7 - Deflector 11 - Link 4 - Saddle Frame Assembly L__ 1-9/16' 2-1/4" F1_0' (39,7 mm)] (57,2 mm) 11 9 I - 1-1/8" (28,6 mm) 8 I FLOW FLOW 2-1/2' (63,5 mm) R/6FRAME ARMS 2 3 4 WRENCH 1/2' 7/16" HEX NPT (11,1 mm) NOMINAL CROSS MAKE-IN SECTION ELEVATION FIGURE B MODELS BBI, BB2 & BB3 WITH 5.6 K-FACTOR SPECIFIC APPLICATION ATTIC SPRINKLERS Components: I I 1 - Body 5 - Compression 8 - Deflector I I 2 - Cap Screw 9 - Rivet I I 3 - Sealing 6 - Lever 10 - Link I I Assembly 7 - Deflector Assembly I 4 - Saddle Frame I 1-5/16' 2-1/8" (33,3 mm) (54,0 mm) 1-5/16" 8 (33,4 4mm) fl 10 FLOW FRAME ARMS l 6 3' (76,2 mm) 2 1 7/16" (11,1 mm)J WRENCH 1/2' NOMINAL HEX NPT CROSS MAKE-IN SECTION ELEVATION FIGURE D MODELS SDI, SD2 & SD3 WITH 5.6 K-FACTOR SPECIFIC APPLICATION ATTIC SPRINKLERS Components: 1 - Frame 4 - Bulb 2 - Button 5 - Compression 3 - Sealing Screw Assembly 6 - Deflector 2-1/8 2' - (54,0 mm) (50,8 mm) - 1-1/16' -J 1-1/4' (27,0 mm) (31,8 mm) . Tb71 - FLOW 2-1/8' (54,0 mm) 7/16(11,1 mm)—J / 1/2' NPT / NOMINAL MAKE-IN WRENCH FRAME FLATS ARMS CROSS SECTION ELEVATION TFP6IO Page 3 of 28 FIGURE E MODEL HIP WITH 5.6 K-FACTOR SPECIFIC APPLICATION ATTIC SPRINKLERS Components: 1 - Frame 5 - Compression 2 - Sealing Screw Assembly 6 - Deflector 3 - Button 7 - Ejection 4 - Bulb Spring 1-11/16" (42,9 mm) 6 5 - SPRINKLER FRAME ARMS 2-1/4" (57,2 mm) IC RENCH 2 FLATS 1/2 NPT 7/16(11,1 mm) NOMINAL MAKE-IN CROSS SECTION ELEVATION FIGURE F MODEL AP WITH 4.2 or 5.6 K-FACTOR SPECIFIC APPLICATION COMBUSTIBLE CONCEALED SPACE SPRINKLERS The other cost reduction is the Listing of BlazeMaster CPVC for use in attic spaces to feed the wet system Spe- cific Application Sprinklers for Pro- tecting Attics, as well as to feed the wet system sprinklers below the ceil- ing. Traditionally, BlazeMaster CPVC has been used on the lower floors in the joist space above a ceiling that do not require sprinklers. The cost of us- ing CPVC on those floors can now be translated to the upper floor even if sprinklers are required in the attic. There are four (4) models of the Spe- cific Application Sprinklers for Pro- tecting Attics - BB (Back to Back Dual Directional), SD (Single Directional), HIP, and AP (Attic Plus). The BB (Back to Back) and SD (Single Directional) Sprinklers have three (3) separate ver- sions that are used for different roof pitches. The pitches, as applicable, can vary from a minimum of 3:12 to a maximum of 12:12 (Ref. Table A). BB Sprinkler (Back to Back Dual Directional) The Model BB Specific Application At- tic Sprinkler (Figures A, B & C) throws a narrow but long pattern. The nar- row spacing along the ridge serves two purposes: the response time is reduced by placing the sprinklers no farther than 6 feet (1,8 m) apart, and the spray can be concentrated in the throw direction to obtain a pattern that will cover up to 30 feet (9,1 m) in each direction when measured horizontal- ly. There are three (3) different models (i.e., BB1, BB2, and BB3) that account for different roof slopes, and each model is provided in one of three dif- ferent orifice sizes (K=4.2, 5.6, or 8.0). SD Sprinkler (Single Directional) The Model SD (Single Directional) Specific Application Attic Sprinkler (Figure D), like the Model BB, throws a narrow but long pattern. However, un- like the Model BB, the Model SD only throws in one direction. These sprin- klers are primarily used where shear walls or draft curtains have been in- stalled within an attic space. Another use is when the framing direction is parallel with the outside wall in the hip area (Ref. Figure 13). In this case, the SD (Single Directional) would be used on one side of the slope and AP Sprin- klers or Standard Spray Sprinklers would be used to protect the other side. The Model SD Sprinklers must be installed in a vertical upright orien- tation and not angled with the slope. (Achieving the vertical upright orien- tation may require the use of a swing joint if the SD Sprinklers are being fed from a line running along and paral- lel to the roof hip.) There are three (3) different models (SD1, SD2, and SD3) that account for different roof slopes. HIP Sprinkler The HIP Specific Application Attic Sprinkler (Figure E) covers the area of the hip in the attic. This is a slight- ly different concept than the BB (Back to Back) or SD (Single Directional). The HIP Sprinkler is located along the slope running down the hip, and throws a 900 pattern toward the out- side eaves. This pattern allows the water to "corner" and control the fire. The HIP does not throw much water directly up or down the hip, but rath- er it throws most of the pattern out to each side (90°) down the slope of the roof. This sprinkler is typically spaced 6 feet (1,8 m) to 3 feet (0,9 m) on center down the slope. To use the HIP Sprin- kler, the framing must be perpendicu- lar to the outside wall (Ref. Figure 12) and the maximum throw cannot ex- ceed 28 feet (8,5 m) measured hori- zontally. The HIP, unlike the BB (Back to Back) and SD (Single Directional), is installed with the deflector parallel with the slope. There is only one mod- el with flows and pressures for two different spacings. TFP6IO Page 4 of 28 AP Sprinkler (Attic Plus) The AP Sprinklers are to be installed in the upright orientation with their de- flector parallel to the roof. The Model AP Sprinklers (Figure F) are intended to be used to provide protection of at- tic areas outside the scope of appli- cations for the BB, SD, or HIP Sprin- klers. The AP Sprinklers must only be used in conjunction with other Specific Application Attic Sprinklers, i.e., BB, SD, and HIP, or as permitted in other sections of this document. When used, the AP Sprinklers will pro- vide a hydraulic advantage over Stan- dard Spray Sprinklers for the protec- tion of attic areas outside the scope of application for the BB, SD, or HIP Sprinklers. The Specific Application Sprinklers for Protecting Attics described here- in must be installed and maintained in compliance with this document, as well as with the applicable standards of the National Fire Protection Asso- ciation, in addition to the standards of any other authorities having jurisdic- tion. Failure to do so may impair the performance of these devices. The owner is responsible for main- taining their fire protection system and devices in proper operating con- dition. Contact the installing contrac- tor or product manufacturer with any questions. Sprinkler Identification Number (SIN) * The "TY" prefix is a re-designation of the previous "C" prefix (e.g., 1Y4180 is a re-designation for C4180). Technical Data Approvals UL & C-UL Listed (These Approvals only apply to the service conditions indicated in the De- sign Criteria section on Page 6 and the Design Guidelines section on Page 8.) Pipe Thread Connection 1/2 inch NPT for K=4.2 & 5.6 3/4 inch NPT for K=8.0 Discharge Coefficient K = 4.2 gpm/psi112 (60,5 pm/bar112) K = 5.6 gpm/psi1'2 (80,6 1pm/bar"2) K = 8.0 gpm/p5i112 (115,5 1pm/bar112) Temperature Rating Intermediate Temperature as follows: -200°F (93°C) for BB (K4.2 & K8.0), HIP, AP 212°F (1 00°C) for BB (K5.6), SD Finish Natural Brass Physical Characteristics (Figures A, C & E) Frame ............................Bronze Button.....................Bronze/Copper Sealing Assembly ...........Beryllium Nickel w/TEFLON Bulb .....................Glass (3 mm dia.) Link ............................... Monet Compression Screw .................Brass Deflector.....................Brass/Bronze Physical Characteristics (Figures B & D) Body..............................Brass Cap..............................Bronze Sealing Assembly ...........Beryllium Nickel w/TEFLON Saddle ............................Brass Link Assembly ......................Nickel Compression Screw .................Brass Deflector .....................Brass/Bronze Lever .....................Bronze Deflector Frame ............................Bronze Diffuser ............................ Brass Rivet ..............................Brass Physical Characteristics (Figure F) Frame .............................Brass Button............................Bronze Sealing Assembly ...........Beryllium Nickel w/TEFLON Bulb .....................Glass (3 mm dia.) Compression Screw .................Brass Deflector..........................Bronze Operation BB (K=8.0 & 4.2), HIP (K=5.6) & AP (5.6 & 4.2) The glass bulb contains a fluid that ex- pands when exposed to heat. When the rated temperature is reached, the fluid expands sufficiently to shatter the glass bulb, allowing the sprinkler to activate and water to flow. BB (K=5.6) & SD (K=5.6) The fusible link assembly is comprised of two link halves which are joined by a thin layer of solder. When the rated temperature is reached, the solder melts and the two link halves sepa- rate, allowing the sprinkler to activate and water to flow. TY4180* - BB1, K=8.0 TY4181* - BB2, K=80 TY4182* - BB3, K=8.0 TY3180* - BB1, K=5.6 TY3181* - BB2, K=5.6 K=5.6 ci 1EE EII -. TY21 R9 - RR3, 2: t4 56 TY3187* HIP, TY2190 :AP: K=4.2 TFP6IO Page 5 of 28 Installation The TYCO Specific Application Attic Sprinklers for Protecting Attics must be installed in accordance with this section. Do not install any bulb-type sprin- kler if the bulb is cracked or there is a loss of liquid from the bulb. With the sprinkler held horizontally, a small air bubble should be present. The diam- eter of the air bubble is approximately 1/16 inch (1,6 mm) for the 155°F (68°C) and 3/32 inch (2,4 mm) for the 200°F (93°C) temperature ratings. A leak-tight 1/2 inch NPT sprinkler joint should be obtained by applying a minimum-to-maximum torque of 7 to 14 ft.lbs. (9,5 to 19,0 Nm). Higher lev- els of torque can distort the sprinkler inlet with consequent leakage or im- pairment of the sprinkler. Step 1. Sprinklers must be oriented correctly as follows: Model BB Sprinklers are to be in- stalled in the upright vertical po- sition with the flow arrows on the deflector pointing down the two op- posing slopes. Model SD Sprinklers are to be in- stalled in the upright vertical posi- tion with the flow direction arrow on the deflector pointing down the slope. The Model HIP Sprinklers are to be installed with the deflector at the top and with the sprinkler centerline perpendicular to the ridge of the hip roof and with the flow direction ar- rows on the deflector pointing down the two opposing slopes. (Unlike the Model BB and Model SD, the Model HIP is installed angled so -that its deflector is parallel with the slope of the hip ridgeline.) The Model AP Sprinklers are to be installed in the upright position with the deflector parallel to the roof slope. There are no flow arrows on the deflector to consider; however, a good piping practice is to position all the Model AP Sprinklers so that their frame arms are in the same direction. Step 2. With pipe thread sealant ap- plied to the pipe threads, hand-tighten the sprinkler into the sprinkler fitting. Note: With reference to Figure G, do not grasp the sprinkler by the deflector. t WRENCH FLATS?~ ENGAGE SPRINKLER THREAD RELIEF 7USEEND WITH WRENCH JAW FLANGES WRENCH JAW FLANGE KED- A' ONLY FIGURE H W-TYPE 3 SPRINKLER WRENCH For Use with BB(K=8.0) Sprinklers WRENCH FLATS ENGAGE SPRINKLER THREAD RELIEF %END WRENCH LANGES WRENCH UJAW FLANGE M - A ONLY FIGURE J W-TYPE 6 SPRINKLER WRENCH For Use with BB (K=4.2) Sprinklers Step 3. Wrench-tighten the sprinkler using only the wrenches shown in Figures H thru M. Wrenches are only to be applied to the sprinkler wrench flats or wrench hex, as applicable. WRENCH FLATS ENGAGE SPRINKLER THREAD RELIEF WITH WRENCH N JAW FLANGES 'N. WRENCH 7"A"ONLY ND \ JAW FLANGE ED -' FIGURE K W-TYPE 20 SPRINKLER WRENCH For Use with HIP (K=5.6) Sprinklers WRENCH HEX APPLY WRENCH:4 TO WRENCH HEX ONLY Q', ADJUST WRENCH JAW TO FIT WRENCH HEX FIGURE L ADJUSTABLE WRENCH For Use with BB (K=5.6) & SD (K=5.6) Sprinklers WRENCH FLATS ENGAGE SPRINKLER THREAD RELIEF WITH WRENCH N JAW FLANGES N WRENCH USE END \ JAW FLANGE MARKED- A ONLY FIGURE M W-TYPE 6 SPRINKLER WRENCH For Use with AP (K=4.2 & 5.6) Sprinklers TFP6IO Page 6 of 28 Design Criteria Area of Use Roof structures, combustible and noncombustible, including wood joist/ rafters and wood trussed attics, with a ceiling below. System Type for BB, SD, HIP, or AP Wet using CPVC pipe Wet or dry using steel pipe Note: Use of the 4.2 K sprinklers in dry pipe systems is permitted by sec- tion 8.3.4.3 of NFPA 13 (2007 edition) where piping is corrosion resistant or internally galvanized. Hazard Light Hazard BB, SD, or HIP Allowable Roof Span (Coverage) and Roof Pitch Refer to Table A for allowable roof spans and roof pitches, as well as for the associated minimum sprinkler flows and pressures. Figures 11 21 11 & 12 illustrate where the roof span is to be measured. Coverage Beyond BB, SD or HIP Allowable Roof Spans Up to 10 feet (3,1 m) of coverage at the eave(s) beyond the allowable roof spans for BB, SD, or HIP Sprinklers may be obtained by using a single row of AP Sprinklers (Ref. Figures 14A, 14B & 15). BB, SD, HIP, or AP Minimum Distance Between Sprinklers 4 feet (1,2 m) as measured along the branchline for BB and SD (Ref. Figure 3) 3 feet (0,9 m) as measured along the branchline for HIP (Ref. Figure 12) 7 feet (2,1 m) between AP Sprinklers BB, SD, HIP, or AP Maximum Distance Between Sprinklers 6 feet (1,8 m) on center along the branchline (Ref. Figures 3 & 12) for BB, SD, and HIP For AP, the maximum spacing is 10 feet (3,1 m) perpendicular to slope and 12 feet (3,6 m) parallel to slope. When there is more than one row of AP Sprinklers, the sprinklers must be staggered per Figure 20-13-3. BB, SD, HIP, or AP Minimum Distance to AP Sprinklers or Standard Spray Sprinklers As measured along the peak/ridge di- rection (Ref. Figure 4), 6 feet (1,8 m) from BB, SD, and HIP to Standard Spray Sprinklers As measured along the peak/ridge di- rection (Ref. Figure 4), 7 feet (2,1 m) from AP to Standard Spray Sprinklers In the slope direction (Ref. Figure 6), 26 feet (7,9 m) from BB or HIP Sprin- klers to AP Sprinklers or Standard Spray Sprinklers BB, SD, or HIP Deflector Installation Position Below Peak/Ridge or Deck For roof pitches of 4:12 (33%) to 12:12 (100%), 22 inches (558,8 mm) maxi- mum, 16 inches (406,4 mm) minimum (Ref. Figures 2 & 5). For roof pitches of 3:12 (25%) up to 4:12 (33%) (only 4.2K Model BB), 12 inches (304,8 mm) maximum below the peak and a minimum of 1 inch (25,4 mm) below the bottom of top chord or solid wood rafter AP Deflector Position and Roof Pitch 1 to 3 inches (25,4 to 75,6 mm) below the bottom of the top chord or bottom of solid wood rafter, where the roof pitch is 3:12 to 12:12 and the top chord or solid wood rafter is a nominal 12 inches (600 mm) or less BB or SD Deflector Installation Position Above Scissor Truss 18 inches (457,2 mm) minimum (Ref. Figure 5) BB, SD, or HIP Minimum Distance Away from Trusses Attic Sprinklers must be installed 6 inches (152,4 mm) away from the face of trusses (Ref. Figure 7) SD Distance from Shear Wall or Draft Curtain 4 to 6 inches (101,6 to 152,4 mm) from face, and minimum 8 inches (203,2 mm) above bottom of draft curtain (Ref. Figure 2) Draft Curtains Draft curtains installed to permit the installation of Attic Sprinklers shall be constructed so as to not allow heat to escape through or above the draft curtain. The draft curtain may be constructed of 1/2 inch (12,7 mm) plywood. BB or HIP Maximum Distance from the Center Line of the Ridge 6 inches (152,4 mm) (Ref. Figure 8) with the deflector located 16 inches (406,4 mm) to 22 inches (558,8 mm) from the peak Use of UL Listed BlazeMaster CPVC Piping with Specific Application Sprinklers for Protecting Attics (Wet Systems Only) BlazeMaster CPVC piping may be used in a combustible concealed at- tic space requiring sprinklers when in- stalled in accordance with the follow- ing guidelines: Note: Where the use of non-combus- tible insulation is specified, verify with the insulation manufacturer as to the non-combustibility of the insulation. The non-combustible insulation (i.e., fiberglass) may be faced or unfaced. Where faced, the facing need not be non-combustible. The insulation is to have a flame spread index of not more than 25. Verify chemical compatibility of the insulation with BlazeMaster CPVC by consulting www.lubrizol.com. BlazeMaster CPVC may be used to feed the wet system ceiling sprin- klers on the floor below. There must be 6 inches (152,4 mm) of noncom- bustible insulation covering the hor- izontal or vertical pipe (Ref. Figures 9A, 9B & 9C) extending 12 inch- es (304,8 mm) on each side away from the centerline of the pipe, and the area above the CPVC must be protected by Model BB, SD, HIP, or AP Sprinklers (Ref. Figure 9A). If the pipe is located inside the ceil- ing joist, the joist channel must be covered or filled with 6 inches (152,4 mm) of non-combustible in- sulation on top of the pipe and the area above must be protected by BB, SD, HIP, or AP Sprinklers (Ref. Figure 9B). Insulation is for fire pro- tection purposes. It is not freeze protection. BlazeMaster CPVC must be installed in accordance with the BlazeMaster installation guide instructions. With reference to Figure 19, Blaze- Master CPVC may be used exposed to feed wet system BB, SD, or HIP Sprinklers where: Risers are vertical and protected by a BB, SD, or HIP Sprinklers lo- cated at a maximum lateral dis- tance of 12 inches (304,8 mm) from the riser centerline BB, SD, or HIP Sprinklers are di- rectly mounted on the branchline BB, SD, or HIP Sprinklers are on arm-overs and located at a max- imum lateral distance of 6 inch- es (152,4 mm) from the branchline centerline BB, SD, or HIP Sprinklers are on vertical sprigs attached to the branchline BB, SD, or HIP Sprinklers are on arm-over or angled sprigs, and lo- cated at a maximum lateral dis- tance of 6 inches (152,4 mm) from the branchline centerline A minimum lateral distance of 18 inches (450 mm) is maintained be- tween the CPVC pipe and a heat producing device such as heat pumps, fan motors, and heat lamps TFP6IO Page 7 of 28 DRY PIPE ALLOWABLE SYSTEM ROOF SPAN, MINIMUM MINIMUM MAXIMUM MODEL K SIN (a) (b) (e) FLOW PRESSURE Rise PITCH, Over Run (%) WATER Feet 'm' gpm (1pm) psi (bar) DELIVERY TIME, Seconds BB1 8.0 TY4180 :s60 (18,3) 38 (144) 22.6 (1,5) 4:12 (33) to less than 7:12 (58) (c) 13132 8.0 TY4181 w60 (18,3) 38 (144) 22.6 (1,5) 7:12 (58) to less than 10:12 (83) (C) B33 8.0 TY4182 s60 (18,3) 40(152) 25.0(1,7) 10:12 (83) to 12:12 (100) (c) 131311 5.6 1Y3180 >40 (12,2) to ~60 (18,3) 38(144) 46.0(3,2) 4:12 (33) to less than 7:12 (58) (C) B132 5.6 TY3181 >40 (12,2) to 60 (18,3) 38(144) 46.0(3,2) 7:12 (58) to less than 10:12 (83) (c) BB3 5.6 TY3182 >40 (12,2) to 60(18,3) 38 (144) 46.0(3,2) 10:12 (83) to 12:12 (100) (c) B131 1Y3180 s40(12,2) 25 (95) 20.0 (1,4) 4:12 (33) to less than 7:12 (58) (c) BB2 TY3181 ~40 (12,2) 25 (95) 20.0 (1,4) 7:12 (58) to less than 10:12 (83) (C) BB3 Lx3i.82 k4. -40(12,2) 25 (35) 20.0 (1,4) 10:12 (83) te 12:12 (1°O) (c) BB1 TY2180 ~20 (6,1) 13 (49) 96 (0,7) 3:12 (25) to less than 7:12 (58) 45 (d) 13132 T'?2'TT 20 (,l) 13 (43) 0.6 ,0,7) 7:1 (50) to 1exx Ihari lu: i (3J BB3 4.2 TY2182 ~20 (6,1) 13 (49) 9.6 (0,7) 10:12 (83) to 12:12 (100) 45 (d) SD1 5.6 1Y3183 >30 (9,1) to :540 (12,2) 35 (132) 39.0(2,7) 4:12 (33) to less than 7:12 (58) (c) SD2 5.6 TY3184 >30 (9,1) to :540 (12,2) 35(132) 39.0 (2,7) 7:12 (58) to less than 10:12 (83) (c) SD3 5.6 ].18 'fl Q,1) Wg 10 (12,2) 35 (132) 39.9(2,7-) 10:12 (93) to 12:1 (100) SD1 5.6 1Y3183 >10(3,0) to s;30 (9,1) 25 (95) 20.0(1,4) 4:12 (33) to less than 7:12 (58) (C) SD2 5.6 T9T4 >10 (3,0)to ~ju (9, 1) 25(95) 20.0(1,4) 7:12 (30) to less titan 10:12 (83) (C) SD3 5.6 TY3185 >10(3,0)to :s30 (9,1) 25(95) 20.0(1,4) 10:12 (83) to 12:12 (100) (C) SD1 5.6 TY3183 :s 10 (3,0) 19 (72) 11.5(0,8) 4:12 (33) to less than 7:12 (58) (c) SD2 5.6 TY3184 :510 (3,0) 19(72) 11.5 (0,8) 7:12 (58)to less than 10:12 (83) (c) SD3 5.6 TY3185 dO (3,0) 19 (72) 11.5 (0,8) 10:12 (83) to 12:12 (100) (c) HIP 5.6 1Y3187 >20(6,1) to :528 (8.5) 34 (1 29) 36 9(2 ) 412 (33) to 12:12 (100) (c) HIP 5.6 1Y3187 :s20 (6,1) 25 (95) 20.0(1,4) 4:12 (33) to 12:12 (100) (c) AP 5.6 TY3190 10(3,1) x 12 (3,6) -See note (e) Minimum (psi (U,4S bar) Minimum 0.10 gpm/ft2 3:12 (25) to 12:12 (100) -60 (d) AP 42 1Y2190 (4,1 mm/mm.) Design Density 3:12 (25) to 12:12 (100) 60 (d) Notes: The BB and SD roof span is measured horizontally (not along the slope) as shown in Figure 1 and 2. The HIP roof span is measured horizontally as shown in Figure 12. Refer to 2007 edition of NFPA 13, Section 7.2.3. Maximum water delivery time for all size of systems. The AR roof span is measured along the slope. Maximum 10 feet (31 n!) perpendicular to slope by maximum 12 feet (3,6 m) parallel to slope. TABLE A ALLOWABLE ROOF SPAN, FLOW, PRESSURE, AND PITCH FOR SPECIFIC APPLICATION SPRINKLERS FOR PROTECTING ATTICS TFP6IO Page 8 of 28 BlazeMaster CPVC may be used exposed to provide wet system, vertical or angled, sprigs to AP Sprinklers (Ref. Figures 17A & 17B) where: The exposed portion of an angled sprig is a maximum length of 3 feet (0,9 m), the sprig is supported ad- jacent to the AP Sprinkler, and ver- tical restraint is provided using the CPVC hanger support for horizon- tal pipe runs Vertical sprigs have a maximum exposed length of 10 feet (3,05 m), the AP Sprinkler is located at a maximum lateral distance of 12 inches (3304,8 mm) from the sprig centerline, and the sprig is sup- ported at the swing joint to the AP Sprinkler A minimum 6 inches (152,4 mm) deep of non-combustible insulation extending 12 inches (304,8 mm) on each side away from the centerline of the CPVC branchline feeding the AP sprigs (Ref. Figure 17A). If the CPVC branchline is located inside the ceiling joist, the joist channel must be covered or filled with a minimum of 6 inches (152,4 mm) deep of noncombustible insula- tion on top of the branchline feed- ing the AP sprigs (Refer to Figure 17B). Insulation is for fire protection purposes. It is not freeze protec- tion. Additional depth of non-com- bustible insulation may be added to reduce the exposed length of the AP sprigs. A minimum lateral distance of 18 inches (450 mm) is maintained be- tween the CPVC pipe and a heat producing device such as heat pumps, fan motors, and heat lamps Mismatched Slopes Refer to Figure 10. Obstructions For BB, SD, and HIP, refer to Figure 16. For AP Sprinklers, refer to Figure 18. BB, SD, HIP, and AP Sprinklers may be installed directly on maximum 2-1/2 inch NPS (DN65) branch lines without the need for sprigs. See the 2007 edition of NFPA 13, 8.8.5.2 for requirements when installed on pipe greater than 2-1/2 inch NPS (DN65). Hydraulic Requirements Refer to Figure 20. To Determine the Correct Flow and Pressure For BB, SD, or HIP Sprinklers, deter- mine the roof span (measured hori- zontally) and the slope of the roof, and then refer to Table A. There is no in- terpolation of the flow and pressure shown. Round all cases to the next higher spacing. For example, a 45 feet (13,7 m) span with the BB1 (K=8.0) would be calculated at the 60 feet (18,3 m) span. For the AP Sprinklers, the minimum design pressure is 7 psi, and the mini- mum design density is 0.10 gpm/ft2 (4,1 mm/mm). The NFPA 13, 20 psi (1,4 bar) minimum operating pressure for Standard Spray Sprinkler spacings parallel to the ridge that are above 8 feet (2,4 m) does not apply to the AR Coverage Area Coverage area for the BB (Back to Back) Sprinklers is determined by twice the distance of the furthest throw measured along the slope multiplied by the distance along the branchline (maximum distance along branchline is 6 feet [1,8 m] re- gardless of the length of the throw). Note: The distance along the branch- line may have to be reduced to less than the maximum of 6 feet (1,8 m) to remain under 400 ft2 (37,2 m2) maxi- mum depending on the slope and the span. In no case can the span exceed 60 feet (18,3 m) without additional Standard Spray Sprinklers. Coverage area for the SD (Single Di- rectional) Sprinklers is the distance along the branchline multiplied by the distance of the throw down the slope. Regardless of the throw, the maximum distance along the branchline is 6 feet (1,8 m), the max- imum throw measured horizontally is 40 feet (12,2 m), and the maxi- mum coverage per sprinkler is 400 ft2 (37,2 m2). Coverage area for the HIP Sprin- klers is the distance down the larger slope multiplied by two, and multi- plied by the distance between the sprinklers as measured along the slope of the hip. Coverage area for the AP (Attic Plus) Sprinklers is the distance along the branchline multiplied by the dis- tance between the branchlines. The maximum spacing is 10 feet (3,1 m) perpendicular to the slope and 12 feet (3,6 m) parallel to slope, and as measured on the slope. When there is more than one row of AP Sprinklers, the sprinklers must be staggered per Figure 20-B-3. The maximum spacing per sprinkler is 120 ft2 (11,1 m2). Design Guidelines To design a project with attic sprin- klers use these steps as a guideline: Determine if single, dual directional or hip sprinkler is needed. Determine the roof slope is between 3:12 to 12:12. If more than one slope is being used on a project, select the correct sprinkler for each area. Follow the guidelines for each type of sprinkler. Calculate the sprinkler system in ac- cordance with the appropriate flow and pressure information provid- ed in Table A, as well as Figure 20. There is no interpolation of the flows and pressures shown on the chart. For BB Sprinklers (Back to Back Dual Directional) Verify framing direction is perpen- dicular to outside wall (Ref. Figure 12). If not, cover that area with AP Sprinklers or Standard Spray Sprin- klers (Ref. Figure 13). Determine the throw needed (see spacing requirements in Table A). If over 20 feet (6,1 m) and up to 60 feet (18,3 m) is required, use the 8.0 K-factor, BB Sprinklers to reduce the pressure required. If pressure is not a concern, use the 5.6 K-fac- tor, BB Sprinklers to minimize over discharge. If less than 20 feet (6,1 m) is re- quired, use the 4.2 K-factor, Back to Back Dual Directional to minimize pressure and flow requirements Determine the distance along the slope. If the distance is not equal, use the longer side. Multiply the lon- ger side by two to determine the spacing down the slope. Four hun- dred divided by this value will de- termine the maximum spacing along the ridge. The maximum dis- tance is 6 feet (1,8 m). For exam- ple, a 12:12 slope at the maximum span of 60 feet (18,3 m) will produce a slope length of approximately 42.5 feet (13,0 m). That number multi- plied by two produces an 85 feet (25,9 m) throw. Four hundred square feet maximum divided by an 85 feet (25,9 m) throw only allows a 4 feet 8 inches (1,4 m) spacing along the ridge. Using the maximum spacing, space the sprinklers along the ridge. Avoid obstructions as shown in Fig- ure 16. If necessary, add Model AP Sprinklers or Standard Spray Sprin- klers to maintain coverage around obstructions. TFP6IO Page 9 of 28 For SD Sprinklers (Single Directional) Determine the throw needed. As the 400 ft2 (37,2 m2) is not a fac- tor with the SD Sprinklers, the max- imum spacing is 6 feet (1,8 m) and the minimum is 4 feet (1,2 m) (Ref. Figures 2 & 11). (The reason 400 ft2 is not an issue with the single di- rectional is because, at its max- imum spacing, 6 feet [1,8 m] on center / covering 40 feet [12,2 m] flat / a 12:12 slope / and the throw being 56.5 feet [17,2 m], the 400 ft2 [37,2 m2] maximum would not be exceeded.) Avoid obstructions as shown in Fig- ure 16. If necessary, add Model AP Sprinklers or Standard Spray Sprin- klers to maintain coverage around obstructions. For HIP Sprinklers Verify framing direction is perpen- dicular to outside wall (Ref. Figure 12). If not, cover that area with AP Sprinklers or Standard Spray Sprin- klers (Ref. Figure 13) From the intersection of the top of the hip and the ridge, the maximum distance down the slope of the hip is 3 feet (0,9 m). Start the layout with the first sprinkler as close to that point as possible, but no further, while staying 6 inches (152,4 mm) away from the face of the truss- es. Remember the slope of the hip is not equal to the slope of the roof from the ridge to the outside wall. Continue to space sprinklers down the hip at a maximum of 6 feet (1,8 m) on center as measured along the slope of the hip. When the bottom of the hip is encountered, the last sprinkler must be within 7-1/2 feet (2,3 m) of the outside wall as mea- sured flat (plan view). If this pipe is "cut to fit", remember to account for the different slopes of the hip and the roof, as well as distances measured along the slope verses horizontal in plan view must be ac- counted for. Avoid obstructions as shown in Fig- ure 16. If necessary, add Model AP Sprinklers or Standard Spray Sprin- klers to maintain coverage around obstructions. Care and Maintenance The TYCO Specific Application Sprin- klers for Protecting Attics must be maintained and serviced in accor- dance with this section. Before closing a fire protection system main control valve for maintenance work on the fire protection system that it controls, obtain permission to shut down the affected fire protection sys- tem from the proper authorities and notify all personnel who may be affect- ed by this action. The owner is responsible for the in- spection, testing, and maintenance of their fire protection system and devic- es in compliance with this document, as well as with the applicable stan- dards of the National Fire Protection Association (e.g., NFPA 25), in addition to the standards of any other authori- ties having jurisdiction. Contact the in- stalling contractor or product manu- facturer with any questions. Automatic sprinkler systems should be inspected, tested, and maintained by a qualified Inspection Service in accordance with local requirements and/or national code. Sprinklers that are found to be leaking or exhibiting visible signs of corrosion must be replaced. Automatic sprinklers must never be painted, plated, coated, or otherwise altered after leaving the factory. Modi- fied sprinklers must be replaced. Over-heated solder type sprinklers must be replaced. Bulb-type sprin- klers that have been exposed to cor- rosive products of combustion, but have not operated, should be replaced if they cannot be completely cleaned by wiping the sprinkler with a cloth or by brushing it with a soft bristle brush. Care must be exercised to avoid dam- age to the sprinklers before, during, and after installation. Sprinklers dam- aged by dropping, striking, wrench twist/slippage, or the like, must be replaced. Also, replace any sprinkler that has a cracked bulb or that has lost liquid from its bulb. (Refer to In- stallation Section.) Limited Warranty For warranty terms and conditions, visit www.tyco-fire.com. Ordering Procedure Contact your local distributor for avail- ability. When placing an order, indi- cate the full product name and Part Number (P/N). Sprinkler Assemblies with NPT Thread Connections Specify: Model (specify), (specify) K- factor, SIN (specify), Specific Applica- tion Attic Sprinkler, P/N (specify): BB1 (K=8.0), 1Y4180 ..................PIN 51-623-1-200 B82 (K=8.0, TY4181 ...................PIN 51-621-1-200 BB3 (K=8.0), 1Y4182 ..................PIN 51-622-1-200 13131 (K=5.6), 1Y3180 ..................P/N 50-601-1-212 BB2 (K=5.6), 1Y3181 ..................P/N 50-602-1-212 BB3 (K=5.6), 1Y3182 ..................P/N 50-603-1-212 BB1 (K=4.2), TY2180 ..................P/N 50-620-1-200 BB2 (K=4.2), 1Y2181 ..................PIN 50-621-1-200 B83 (K=4.2), TY2182 ..................P/N 50-622-1-200 Sf31 (K=5.6), 1Y3183 ...................P/N 50-611-1-212 SD2 (K=5.6), TY3184 ...................P/N 50-612-1-212 SD3 (K=5.6), TY3185 ..................P/N 50-613-1-212 HIP (K=5.6), 1Y3187 ..................P/N 51-620-1-200 AP (K=5.6), 1Y3190 ..................P/N 50-625-1-200 AP (K=4.2), 1Y2190 ..................P/N 50-624-1-200 Sprinkler Wrench Specify: W-Type 3 Sprinkler Wrench, P/N 56-895-1-001 Specify: W-Type 20 Sprinkler Wrench, P/N 56-000-1-106 Specify: W-Type 6 Sprinkler Wrench, P/N 56-000-6-387 TFP6IO Page 10 of 28 ROOF SPAN (COVERAGE) BACK TO BACK STANDARD SPRINKLER TRUSS SCISSOR 12 TRUSS FIGURE 1 6-0' (1,83 m) MAXIMUM________ 4-0' (1,22 m) MINIMUM II II II II \ II II BBorSDATTIC II II SPRINKLERS RIDGE II II H BRANCH II II II II I LINE I II II II II II II 11 TRUSS 1 II II CEILING II II II II II / II II II II II / II FIGURE 3 ' I 6'(152,4 mm) MAX. DECK ROOF SPAN 4 (101,6 mm) MIN. (COVERAGE) FROM WALL AP or STANDARD ,7T SPRAY SPRINKLER SINGLE DIRECTIONAL g- SPRINKLERS I SEE I 22' (558,8 mm) MAX. 16" (406,4 mm) MIN. ________ FIG 11 BOTTOM OF SHEATHING DRAFT 8" M CURTAIN FULL WALL TO DECK TO DECK (20 3,2 mm FIGURE 2 7-0" (2,1 m) MIN. FOR AP SPRINKLERS 6'-0"(1,8 m) MINIMUM FOR STANDARD SPRAY SPRINKLERS II I AP or STANDARD II ATTIC II II SPRAY SPRINKLER II SPRINKLER H II RIDGE H BRANCH I II II I..It'JE II II It II TRUSS 1 CEILING I 1 H H H FIGURE 4 22' (558,8 mm) MAX. BB, SD or HIP ATTIC 16' (406,4 mm) MIN. SPRINKLER -or- - / STANDARD FOR A ROOF PITCH TRUSS 18' MIN. LESS THAN 4:12 (33%), (457,2 mm) 12" (304,8 mm) MAXIMUM BELOW PEAK AND 1" (25,4 mm) MINIMUM / / BELOW BOTTOM OF RAFTER TRUSS /IN TOP CHORD OR \ SCISSOR 26-0' (7,92 m) MINIMUM BB, SD or HIP ATTIC SPRINKLER AP or STANDARD SPRAY SPRINKLERS FIGURE 5 FIGURE 6 6' (152,4 mm) MINIMUM II BB, SDorHIP II SPRINKLER_i \ RIDGE BRANCH II II II LINE I II II TRUSS- 11 CEILING 1 ii II II ii I' II 6" (152,4 mm) MAXIMUM 22" (558,8 mm) MAX. 16" (406,4 mm) MIN. BOTTOM OF SHEATHING BB or HIP ATTIC SPRINKLER FIGURE 7 FIGURE 8 NON-COMBUSTIBLE INSULATION ATTIC FOR FIRE PROTECTION OF CPVC PIPE, SPRINKLER NOT FREEZE PROTECTION PROTECTED OPTION B SPACE 6" MIN. /\( (1524 mm)4i\ CPVC PIPE CEILING JOIST \ & FITTINGS SPRINKLER CEILING FIGURE 9B TFP6IO Page 11 0f28 ATTIC F-1 0 2"MIN---+-12"MIN 48 mm) ' (304,8 mmT SPRINKLER PROTECTED SPACE 6" MIN. (152,4 mm) CEILING / / T NON-COMBUSTIBLE / INSULATION FOR FIRE JOIST / PROTECTION OF CPVC CPVC PIPE CEILING PIPE, NOT FREEZE & FITTINGS SPRINKLER PROTECTION FIGURE 9A NON-COMBUSTIBLE INSULATION ATTIC FOR FIRE PROTECTION OF CPVC PIPE, SPRINKLER NOT FREEZE PROTECTION PROTECTED SPACE VERTICAL RISE _ 76 (152,4 mm) CEILING - \-JOIST CEILING \ CPVC PIPE ELEVATION CHANGE \ & FITTINGS CEILING FIGURE 9C FIGURE 9 NON-COMBUSTIBLE INSULATION FOR THE PROTECTION OF CPVC PIPE SINGLE DIRECTIONAL SPRINKLERS AS APPROPRIATE FOR RESPECTIVE SLOPE DRAFT CURTAIN & MIN. (SHOWN) (203,2 mm) OR FULL WALL I TO ROOF DECK -> ZA WHEN ANGLE A" DOES NOT EQUAL ANGLE "B" FIGURE 10 PERMITTED USE OF ATTIC SPRINKLERS FOR MISMATCHED SLOPES AP or STANDARD SPRAY SPRINKLER COVERAGE ON SLOPE \BB, SID or HIP COVERAGE ON \ HORIZONTAL 7 / CEILING ROOF JOIST JOIST OR TOP CHORD AP or STANDARD SPRAY SPRINKLER COVERAGE ON SLOPE BB, SDor HIP COVERAGE ON MAXIMUM HORIZONTAL PERMITTED TOP OF INSULATION NON-COMBUSTIBLE ROOF JOIST INSULATION OR TOP CHORD FIGURE 11 COVERAGE STARTING POINT AT EAVE TRUSSES IN HIP SLOPE AREA PARALLEL TO OUTSIDE WALL MAXIMUM T OUTSIDE WALL 40'-0 (12,2 m) I SINGLE HORIZONTAL -J DIRECTIONAL ROOF SPAN I SPRINKLERS (COVERAGE) HIP RIDGES TFP6IO Page 12 of 28 I- 7-6" (2,3 m) MAX. HORIZONTAL II I II I - HIP SPRINKLERS -- I I I I I I I I I BACK PROTECT AREA ON - - - - I I I I I I I TO BACK FIGURE 12 BOTH SIDES OF - - - - I I I I I I I I SPRINKLERS HIP RIDGE HIP ROOF INSTALLATION WITH RAFTERS FRAMED RAFTERS IN HIP SLOPE --HIP --- PERPENDICULAR /IROOF TO AREA PERPENDICULAR SLOPE - I I I I I TO OUTSIDE WALL - - - - -I OUTSIDE WALL I I I II I SLOPE (SHOWNWITHHIP SPRINKLERS PROTECTING I OUTSIDE-- I RIDGE LINE HIP SLOPE & ADJACENT MAXIMUM WALL - - AREAS TO HIP SLOPE) 28'-0" (8,5 m) HORIZONTAL HIP RIDGES 6-0" (1,8 m) MAX. 3'-0"(0,9 m) SEE FIG. 11 3'-O" (0,9 m) MIN. MAX. ON ON HIP SLOPE HIP SLOPE h_6'0"(1,8m)MAX. STANDARD SPRAY SPRINKLERS INSTALLED PER NFPA 13 IN HIP SLOPE AREA WHEN TRUSSES ARE FRAMED PARALLEL TO OUTSIDE WALL rit BACK TO BACK H-1INKLERS IHIP / :ISLOPE: >+_\ ROOF SLOPE H \ RIDGE LINE 3'-O"(0,9m) MAX. ON / HIP SLOPE FIGURE 13A HIP ROOF INSTALLATION WITH TRUSSES FRAMED PARALLEL TO OUTSIDE WALL (SHOWN WITH STANDARD SPRAY OR AP SPRINKLERS IN HIP SLOPE) WHERE AN AREA (SHOWN NON-SHADED) IS PROTECTED WITH AP SPRINKLERS, CPVC MAY BE USED FOR CEILING PROTECTION BELOW (SEE PAGE 6) 3'-0'(0,9m) MAX. ON - HIP SLOPE CPVC PIPE MAY BE USED IN SHADED AREA ONLY FOR CEILING PROTECTION BELOW (SEE PAGE 6 FIGURE 13B HIP ROOF INSTALLATION WITH TRUSSES FRAMED PARALLEL TO OUTSIDE WALL (SHOWN WITH STANDARD SPRAY OR AP SPRINKLERS IN HIP SLOPE & ADJACENT AREAS TO HIP SLOPE) STANDARD SPRAY SPRINKLERS INSTALLED PER NFPA 13 IN HIP SLOPE AREA WHEN TRUSSES ARE FRAMED PARALLEL TO OUTSIDE WALL TRUSSES IN HIP SLOPE AREA PARALLEL TO OUTSIDE WALL OUTSIDE WALL WHERE AN AREA (SHOWN NON-SHADED) IS PROTECTED WITH AP SPRINKLERS, CPVC MAY BE USED FOR CEILING PROTECTION BELOW (SEE PAGE 6) - 6'-cr(1,8m) MAX. I I BACK TO BACK I I I \ IS I I SPRINKLERS I I I I I IlISIlI I I I 1 I I I HIP I SE I ROOF SLOPE III] I S IlISII I I I I I RIDGE LINE H IIiI• CPVC PIPE MAY BE USED IN SHADED AREA ONLY HIP RIDGES FOR CEILING PROTECTION BELOW (SEE PAGE 6) 6-0" MA (1,83 m 4-0" MI (1,22 rn AP SPRINKLERS SPACED 8-0" (2,4 m) TO 7'-0 (1,8 m) ON CENTER SEE FIG. 11 SD SPAN (TABLE A) 10,-0,' MAX. (3,05 m) SPRINKLER COVERAGE . 6-0" (1,83 m) /1 SD ATTIC SPRINKLER TFP6IO Page 13 of 28 Attic Spaces Greater Than 60 Feet (18,3m) up to 80 Feet (24,4m) Wide, (Ref. Figures 14 & 15) Only 8.0 K, BB Sprinklers in conjunction with AP Sprinklers or Standard Spray Sprinklers can be used to protect attics up to 80 feet (24,4 m) wide. NOTE Attics over 80 feet (24,4 m) wide must use Standard Spray Sprinklers throughout because Attic Sprinklers have not been tested in this scenario. For single ridge construction (Ref. Figure 14A & 1413), use 8.01K, BB Sprinklers to protect the center portion. AP Sprinklers (Ref. Fig. 14A) or Standard Spray Sprinklers (Ref. Fig. 1413) are then used to protect up to 10 feet (3,1 m) of width at the eaves beyond the maximum allowable 60 foot (18,3 m) span of the 8.0K, BB Sprinklers. For hip roof construction (Ref. Figure 15), use 8.01K, BB Sprinklers in the center portion and HIP Sprinklers can be located down the entire hip. AP Sprinklers or Standard Spray Sprinklers are then used to protect up to 10 feet (3,1 m) of width at the eaves beyond the maximum allowable 60 foot (18,3 m) span of the 8.01K, BB Sprinklers, and the maximum allowable horizontal coverage of the HIP Sprinklers. BB SPAN (TABLE A) AP 10-0' MAX. SPRINKLERS (3,05 m) BB ATTIC SPACED AP 6'0" SPRINKLER 8-0" (2,4 m) SPRINKLER (1,83 m) TO ON CENTER '\\ /(122m)\ FIGURE 14A FIGURE 14B 101-0" HIP BACK TO BACK (3,0 m) SPRINKLERS SPRINKLERS HIP RIDGES - • • -rn 10-0" (3,0m) AP SPRINKLERS . RIDGE AT THE EAVES * LINE a PERIMETER F HIP . / ROOF PROTECTION . • SLOPE AREA BB SPAN -. .• (TABLE A) S S S (3,0 rn) CPVC PIPE MAY BE USED IN SHADED I 7-0" to 10'-0 AREA FOR CEILING (2,1 m to 3,0 m) PROTECTION BELOW I ON CENTER FOR (SEE PAGE 6) AP SPRINKLERS FIGURE 15 TFPGIO Page 14 of 28 BB ATTIC SPRINKLER 3-1/2 MIN. (88,9 mm) AIR SPACE 36 IN. M (914,4 mm) NO ADDITIONAL 6" MAX. SPRINKLER (152,4 mm) REQUIRED BB ATTIC ANY SPRINKLER DISTANCE GREATER THAN 6' (152,4 mm) I ADDITIONAL AP OR STANDARD SPRAY SPRINKLER REQUIRED (LOCATE PER FIGURE , 14A OR 149)' FIGURE 16A FIGURE 16B There can be a maximum 6 inch (152,4 mm) high Horizontal Obstruction as long as it is 36 inches (914,4 mm), measured vertically, below the Attic Sprinkler. If the obstruction is closer or larger, there must be a sprinkler on the other side of the obstruction. Reference Figures 16A and 16B. This criteria does not limit the top chord of the trusses or the depth of the rafter, but does limit the obstructions that run across the trusses or rafters. - - 66 ATTIC SPRINKLER NO 6' (152 IVIINI , UM MINIMUM 4 mm) 36' (914,4 mm) ER A ADDITIONAL SPRINKLER \\ REQUIRED FIGURE 16C LESS THAN 69 ATTIC 6' (152,4 mm) SPRINKLER 36° (914,4 mm) ADDITIONAL AP "\ MINIMUM OR STANDARD SPRAY SPRINKLER(S) REQUIRED (LOCATE PER FIGURE 14A OR 149) ZA \\\ 2:L1\1 GTERANN iT t ,4'-0" (1,2 m) FIGURE 16D If the Horizontal Obstruction is below the sprinkler, there must be 6 inches (152,4 mm) clearance over the top of the obstruction, and the obstruction must be 4 feet (1,2 m) or less in width to allow water to pass both over and under the obstruction. The clearance is measured perpendicular to and from the bottom of the rafter. If there is not 6 inches (152,4 mm) of clearance above the obstruction, a sprinkler must be located on the other side of the obstruction. If the obstruction is greater than 4 feet (1,2 m) in width, a sprinkler must be added below the obstruction. Reference Figures 16C and 16D, where the maximum spacing for AP Sprin- klers is 12 feet (3,7 m) and Standard Spray Sprinklers is 15 feet (4,6 m). Dimension A Distance B Additional Sprinkler Required Beyond Obstruction Maximum Horizontal Dimension of Obstruction Minimum Horizontal Distance to Obstruction All Vertical Obstructions <6(152,4 mm) YES 1/2°-1'(12,7mm-25,4mm) 6' (152,4 mm) NO 1°-4" (25,4 mm-101,6 mm) 12"(304,8 mm) NO 4-8" (101,4 mm-203,2 mm) 24"(609,6 mm) NO 8-10" (203,2 mm-254,0 mm) 5-0" (1,52 m) NO 10'-20" (254,0 mm-508,0 mm) 10-0" (3,05 m) NO 20-30" (508,0 mm-762,0 mm) 15-0" (4,57 m) NO 30-40" (762,0 mm-1016,0 mm) 20-0" (6,10 m) NO 40'-48" (1016,0 mm-1219,2 mm) 25-0" (7,62 m) NO >48(1219,2 mm) Any Distance YES DIMENSION A PER TABLE DIMENSION B I11N PER TABLE ADDITIONAL AP OR STANDARD SPRAY SPRINKLER REQUIRED (LOCATE PER FIGURE ,i, 14AOR14B) ' FIGURE 16E For Vertical Obstructions, the maximum dimension of the obstruction is its width and the horizontal distance away from the obstruction is measured horizontally. FIGURE 16 (1 0F2) OBSTRUCTIONS TO WATER DISTRIBUTION - BB, SD & HIP to Water Distribution for Attic Sprinklers Differ from Standard Sprinklers as TFP6IO Page 15 of 28 Figure 16F Area Outside of Mechanical Space or Similar Compartmental Space When a BB Sprinkler is 36 inches (914,4 mm) or greater above the space, and 36 inches (914,4 mm) or greater clearance above the space is present, additional sprinklers are not needed. When a BB Sprinkler is a 36 inches (914,4 mm) or greater above the space, and a 12 to 36 inches (304,8 mm to 914,4 mm) clearance above the space is present, Intermediate Level Standard Sprinklers are to be installed to protect the obstructed area. Otherwise, the area beyond the mechanical space is to be protected as shown by installing Standard Spray Sprin- klers as necessary - OR - by constructing a shear wall and installing SD Sprinklers. Note: In all cases, the mechanical space or similar compart- mented space is to be sprinklered per its respective hazard rating and separated from the light hazard attic space by construction that has a fire resistance rating based on the water supply duration required for the hazard rating within the mechanical space or similar compartmented space. BB ATTIC SPRINKLER 36 R (914,4 mm) 7 NO O ADDITIONAL SPRINKLERS /\ 36 (914,4 mm) OR GREATER REQUIRED STANDARD MECHANI( SPRAY SPRINKLER SPACE 4' (101 6 mm) TO 6" (152,4 mm) TYP. 12' (304,8 mm)TO 36' (914,4 mm) 36" (914,4 mm) /I... OR GREATER INTERMEDIATE SPRAY SPRINKLER =BELEVEL STANDARD STANDARD MECHANICAL 4" (101,6 mm) TO SPRAY SPRINKLER SPACE 6" (152,4 mm) TYP. BB ATTIC SPRINKLER STANDARD SPRAY SPRINKLER LESS THAN 12" (304,8 mm) /\ Figure 16G Piggyback Trusses When a BB Sprinkler can be installed below or between stiffeners and maintain the 16 to 22 inch (404,4 to 558,8 mm) distance to the peak, as well as the "V" and "H" clear- ance to the stiffeners, additional sprinklers are not required. When the stiffeners are located a minimum of 12 inches (304,8 mm) below the BB Sprinkler, the stiffeners are 7-1/2 inches (190,5 mm) maximum in width, the openings are 12 inches (304,8 mm) minimum, and there is 70% minimum open area, additional sprinklers are not required. Otherwise, additional sprinklers are required as shown. V H BB1 BB2 BB3 0" 0' 0" 0" V>0' V+15" 1 V+10" V+8' BOTTOM STIFFENERS TOP OF BB ATTIC DEFLECTOR SPRINKLER BB ATTIC SPRINKLER 70% MINIMUM OPEN AREA 12" MIN. STIFFENERS 3-1/2" MIN. (88,9 mm) (304,8 mm) AIR SPACE H 7-1/2'MAX. I l., (190,5 mm) 1 I l 12'MIN. I (304,8 mm) BB ATTIC LESS THAN SPRINKLER OR 70% OPEN AREA, STANDARD SPRAY OPENINGS LESS THAN SPRINKLER 12" (304,8 mm) WIDE, OR STIFFENERS INTERMEDIATE GREATER THAN 7-1 LEVEL /2" (190,5 mm) STANDARD SPRINKLER " WIDE MECHANICAL SPACE PROTECT WITH ADD SHEAR WALL AND I STANDARD SPRAY PROTECT WITH SINGLE SINGLE INSTALL SINGLE SPRINKLERS DIRECTIONAL SPRINKLERS DIRECTIONAL DRAFT CURTAIN DIRECTIONAL SPRINKLER OR FULL WALL SPRINKLER FIGURE 16 (2 0F2) OBSTRUCTIONS TO WATER DISTRIBUTION - BB, SD & HIP (Obstructions to Water Distribution for Attic Sprinklers Differ from Standard Sprinklers as Shown) TFP6IO Page 16 of 28 3-0' MAX. __- AP (0,9 m) SPRINKLER AP -\- SPRIG \ 6' r JOIST ("¼ (152,4 mm) L12' MIN. I / 12' MIN. (304,8 mmr' (304,8 mm) NON-COMBUSTIBLE INSULATION FOR FIRE PROTECTION OF CPVC CEILING PIPE, NOT FREEZE PROTECTION OPTION A AP SPRINKLER IF 10'-0"MAX AP SPRIG (3,0 m) 6' MIN. c-JOIST I (152,4 mm) 12" MIN. I 12' MIN. (304,8 mm) (304,8 mm) NON-COMBUSTIBLE INSULATION FOR FIRE PROTECTION OF CPVC CEILING PIPE, NOT FREEZE PROTECTION OPTION B FIGURE 17A EXPOSED CPVC WITH AP SPRINKLERS AND BRANCHLINE OVER JOISTS ,,__ (0,9m) _- SPRINKLER AP SPRIG AP PRINKLER 10-0' MAX. AP (3,0 m) t::~- SPRIG FIGURE 178 EXPOSED CPVC WITH AP SPRINKLERS AND JOIST JOIST BRANCHLINE WITHIN JOISTS 6" MIN. / NON-COMBUSTIBLE (152,4 mm) / INSULATION FOR FIRE / PROTECTION OF CPVC I PIPE, NOT FREEZE CEILING PROTECTION OPTION A 6"M" / NON-COMBUSTIBLE (152,4 mm) I INSULATION FOR FIRE / PROTECTION OF CPVC / PIPE, NOT FREEZE CEILING PROTECTION OPTION B OBSTRUCTION OBSTRUCTION AP SPRINKLER SPRINKLER D t -•I L.- A~3Cor3D ~ 24'(6019,6 mm) D (UAse dimension C or D, whichever is greater) ELEVATION VIEW PLAN VIEW Horizontal Minimum Distance Vertical Distance (A) - Below Deflector (B) (e152,4 mm) (76,2 mm) >6'109' (>152,4 mm to 228,6 mm) (101,6 mm) >9 to 12' 6' (>228,6 mm to 304,8 mm) (88,9 mm) >12' to 15' 8' (>304,8 mm to 381,0 mm) (203,2 mm) >15' to 18" 9-1/2" (>381,0 mm 10457,2mm) (241,3 mm) >18'1o24' 12-1/2' (>457,2 mm 10609,6mm) (317,5 mm) >24'Io30' 15-1/2' (>609,6 mm to 762,0 mm) (393,7 mm) >30' 18' (>762,0 mm) (457,2 mm) FIGURE 18 OBSTRUCTIONS TO WATER DISTRIBUTION FOR MODEL AP SPRINKLERS BI AP SPRINKLER OBSTRUCTION TFP6IO Page 17 of 28 6" (150 mm) MAX. B 12" (300 mm) MAX. = ARMOVER SPRIG ARM ANGLE SPRIG ARMOVER BRANCHLINE PVERTICALRISER ANCH LINE L SPRIG (IRECT MOUNT VERTICAL RISER FIGURE 19 EXPOSED CPVC WITH BB, SD, AND HIP SPRINKLERS HYDRAULIC CALCULATIONS Attic sprinklers must be calculated in conformance with these guidelines. In all cases, the design area shall include the most hydraulically demanding sprinklers. More than one set of calculations may be required to prove different situations. For individual areas requiring more than four AP Sprinklers, the maximum area of attic protected by AP Sprinklers is lim- ited to 3000 ft2 (279 m2) in any single area. Areas must be separated by a minimum of 15 feet (4,6 m) by an area protected by BB, SD,or HIP Sprinklers, in order to be considered separate areas. The hydraulic calculations have been divided into three parts as follows: FIGURE 20-A: "Attics Protected Entirety By BB, SD, and HIP Attic Sprinklers". 20-A-1 (Page 18) BB Sprinklers 20-A-2 (Page 18) BB and HIP Sprinklers 20-A-3 (Page 19) BB and SD Sprinklers 9) 69 Spfinkle FIGURE 20-13: "Attics Protected With A Mixture Of BB. SD, and HIP Attic Sprinklers And AP Sprinklers". 20-13-1 (Page 20) SD Sprinklers & AP Sprinklers At The Ridge 20-13-2 (Page 20) BB Sprinklers & AP Sprinklers At The Eaves or Beyond An Obstruction 20-B-3 (Page 21) BB Sprinklers & AP Sprinklers At The Hip 20-B-4 (Page 21) BB Sprinklers, SD Sprinklers, HIP Sprinklers, & AP Sprinklers At The Hip 20-B-5 (Page 22) BB, SD, or HIP Sprinklers & AP Sprinklers in a Dormer, at a Cross, or at an Ell 20-B-6 (Page 22) BB,SD, or HIP Sprinklers & AP Sprinklers Separated By Compartmentalization FIGURE 20-C: "Attics Protected With A Mixture Of BB. SD, and HIP Attic Sprinklers And Standard Spray Sprinklers". 20-C-1 (Page 23) SD Sprinklers & Standard Spray Sprinklers At The Ridge 20-C-2 (Page 23) BB Sprinklers & Standard Spray Sprinklers At The Eaves or Beyond An Obstruction 20-C-3 (Page 24) BB Sprinklers & Standard Spray Sprinklers At The Hip 20-C-4 (Page 25) BB Sprinklers, SD Sprinklers, HIP Sprinklers, & Standard Spray Sprinklers At The Hip 20-C-5 (Page 26) BB, SD, or HIP Sprinklers & Standard Spray Sprinklers in a Dormer, at a Cross, or at an Ell 20-C-6 (Page 26) BB, SD, or HIP Sprinklers & Standard Sprinklers Separated By Compartmentalization I MODEL BB MODEL SID MODEL AP BACK TO BACK T SINGLE DIRECTIONAL MODEL HIP OR STANDARD SPRAY FIGURE 20 HYDRAULIC CALCULATIONS DRY YYDTF.M SFHCV•JN DRY SYSTEM SHOWN TFP6IO Page 18 of 28 FIGURE 20-A- 1. BB SPRINKLERS Wet Systems - Calculate the most demanding five sprinklers. RIDGE Dry Systems - Calculate the most demanding seven sprinklers (see adjacent figure). DRY SYSTEM SHOWN RID RE FIGURE 20-A-2. BB AND HIP SPRINKLERS Wet Systems - Calculate the most de- manding five sprinklers. Dry Systems - Calculate the most de- manding seven sprinklers, and then calcu- late the most demanding contiguous nine sprinklers with a maximum of seven to be BB Sprinklers (see adjacent figures). Use the most demanding calculation. TFP61O Page 19 of 28 FIGURE 20-A-3. BB AND SD SPRINKLERS Wet Systems - Calculate the most de- manding five BB Sprinklers plus two SD Sprinklers. Dry Systems - Calculate the most de- manding seven BB Sprinklers plus up to two SD Sprinklers (see adjacent figure). OBSTRUCTION RIDGE DRY SYSTEM SHOWN FIGURE 20-A-4. SD SPRINKLERS RIDGE I Wet Systems - Calculate the most de- a a a a a a a a a * * manding five SD Sprinklers. T X T T I I \x Dry Systems - Calculate the most de- WALL OR manding nine SD Sprinklers (see adja- DRAFT CURTAIN cent figure). AT RIDGE DRY SYSTEM SHOWN FIGURE 20-A-5. SD AND HIP SPRINKLERS Wet Systems - Calculate the most de- manding five sprinklers. Dry Systems - Calculate the most demand- ing nine sprinklers with a maximum of seven to be SD Sprinklers (see adjacent figure). RIDGE : : : : : : ::: WALL OR DRAFT CURTAIN AT RIDGE DRY SYSTEM SHOWN FIGURE 20-A-6. HIP SPRINKLERS Wet Systems - Calculate the most de- manding five sprinklers (see adjacent fig- ure). Dry Systems - Calculate the most de- manding nine sprinklers. 0 WET SYSTEM SHOWN TFPGIO Page 20 of 28 FIGURE 20-B- 1. SD SPRIN- KLERS & AP SPRINKLERS AT THE RIDGE Wet Systems - Calculate the most demanding five sprinklers of one type. Use the most de- manding calculation. Dry Systems - Calculate the most demanding nine SD Sprin- klers, and then calculate the most demanding seven AP Sprinklers. Use the most demanding calcu- lation (see adjacent figure). 1 & & a a a a a aa * a a RIDGE ----.---- . ---. _S--------S_-• -S • WALLS OR DRAFT CURTAINS DRY SYSTEM SHOWN . . S S • • RIDGE p S S S S S • DRY SYSTEM SHOWN S S OBSTRU( TION RIDGE P P 4----• P P P P P P P DRY SYSTEM SHOWN S S S S S S - A a a a a a a I a * * a DRY SYSTEM SHOWN FIGURE 20-B-2. BB OR SD SPRINKLERS & AP SPRIN- KLERS AT THE EAVES OR BEYOND AN OBSTRUCTION Wet Systems - Calculate the most demanding five BB or SD Sprinklers plus up to two most demanding AP Sprinklers. Dry Systems - Calculate the most demanding seven BB or SD Sprinklers plus up to two most demanding AP Sprinklers (see adjacent figures). AREA 2 AREA 1 AREA -H WITH AP WITH BB WITH AP SPRINKLERS SPRINKLERS SPRINKLERS STAGGERED SPACING WHEN MORE THAN ONE ROW MINIMUM SEPARATION 15'-0'(4,6m) WALL OR DRAFT CURTAIN DRY SYSTEM SHOWN AREA 2 AREA 1 AREA 3 WITH AP WITH 88 & SD WITH AP SPRINKLERS SPRINKLERS SPRINKLERS 15-0 (4,6 m) TFP6IO Page 21 of 28 FIGURE 20-B-3. BB SPRINKLERS & AP SPRIN- KLERS AT THE HIP Where the total number of AP Sprinklers at the hip is greater than four: Wet Systems - Calculate the most demanding five BB Sprin- klers plus the two most demand- ing AP Sprinklers, and then cal- culate the most demanding area up to 1500 ft2 (137 m2) having AP Sprinklers (e.g., Area 2 in adjacent upper figure). Use the most de- manding calculation. Dry Systems - Calculate the most demanding seven BB Sprin- klers plus the two most demand- ing AP Sprinklers, and then cal- culate the most demanding area up to 1950 ft2 (181 m2) having AP Sprinklers (e.g., Area 2 in adjacent upper figure). Use the most de- manding calculation. FIGURE 20-B-4. BB SPRIN- KLERS, SD SPRINKLERS, HIP SPRINKLERS, & AP SPRIN- KLERS AT THE HIP Where the total number of AP Sprinklers at the hip is four or. less: Wet Systems - Calculate the most demanding five BB, SD, or HIP Sprinklers plus up to two most demanding AP Sprinklers. Dry Systems - Calculate the most demanding nine BB, SD, or HIP Sprinklers plus up to two most demanding AP Sprinklers (Of the nine BB, SD, or HIP Sprin- klers, calculate up to a maximum of seven BB Sprinklers, see adja- cent upper figure). Where the total number of AP Sprinklers at the hip is greater than four: Wet Systems - Calculate up to the most demanding five BB, SD, or HIP Sprinklers plus the two most demanding AP Sprinklers, and then calculate the most de- manding area up to 1500 ft2 (137 m2) having AP Sprinklers(e.g., Area 2). Use the most demanding calculation. Dry Systems - Calculate up to the most demanding nine BB, SD, or HIP Sprinklers plus the two most demanding AP Sprinklers, and then calculate the most de- manding area up to 1950 ft2 (181 m2) having AP Sprinklers (e.g., Area 2). Use the most demanding calculation. FIGURE 20-B-5. BB, SD, OR HIP SPRINKLERS & AP SPRINKLERS IN A DORMER, AT CROSS, AT A HIP ORATANELL Where the quantity of AP Sprin- klers in each dormer, cross, or ell is four or less (see adjacent fig- ure) and all of the dormers, cross- es and ells meet the maximum four AP Sprinkler criteria, calculate the BB, SD, or HIP Sprinkler demand as described in Part A-i thru A-6 or Part B-i thru B-4, plus up to two of the most demanding AP Sprinklers in the dormer, cross, or ell that is adjacent to the BB, SD, or HIP Sprinklers that are being included in the demand calculation. Where the quantity of AP Sprin- klers in any dormer, cross, or ell is greater than four, refer to Figure B- 3. SF (4 AP INKLERS R LESS) \. I •\\ RIDGE II /• / WALL DORMER BUILT ON TOP OF ROOF OR SHEATHING RIDGE TFP6IO Page 22 of 28 FIGURE 20-B-6. BB,SD, OR HIP SPRINKLERS & AP SPRINKLERS SEPARATED BY COMPARTMENTALIZATION Wet Systems - Calculate the BB, SD, or HIP Sprinkler de- mand as described in Part A-i thru A-6 or Part B-i thru B-4, and then calculate the most de- manding area up to 1500 ft2 (137 m2) having AP Sprinklers. Use the most demanding cal- culation (see adjacent figure). Dry Systems - Calculate the BB, SD, or HIP Sprinkler de- mand as described in Part A-i thru A-6 or Part B-i thru B-4, and then calculate the most de- manding area up to 1950 ft2 (181 m2) having AP Sprinklers. Use the most demanding cal- culation (see adjacent figure). TFP6IO Pge 23 of 28 FIGURE 20-C- 1. SD SPRINKLERS & STANDARD SPRAY SPRINKLERS AT THE RIDGE Wet Systems - Calculate the most demanding five sprinklers of one type. Use the most demanding calculation. Dry Systems - Calculate the most demanding nine SD Sprinklers, and then calculate the most demand- ing seven Standard Spray Sprinklers. Use the most demanding calculation (see adjacent figures). I I I I II I I I & & A A RIDGE . 0 0 0 • S S 0 0 V V V V V V V V V V V V\T WALLS C IR DRAFT DRY SYSTEM SHOWN FIGURE 20-C-2. BB SPRINKLERS & STANDARD SPRAY SPRINKLERS BEYOND AN OBSTRUCTION Wet Systems - Calculate the most demanding five BB Sprinklers plus up to two most demanding Standard Spray Sprinklers. Dry Systems - Calculate the most demanding seven BB Sprinklers plus up to two most demanding Stan- dard Spray Sprinklers (see adjacent figures). DRY SYSTEM SHOWN TFP6IO Page 24 of 28 FIGURE 20-C-3. BB SPRINKLERS & STANDARD SPRAY SPRIN- KLERS AT THE HIP Where the total number of standard spray sprinklers at the hip is greater than four: Wet Systems - Calculate the most demanding five BB Sprinklers plus up to two most demanding Stan- dard Spray Sprinklers, and then calculate the most demanding re- mote design area (including all sprinkler types) per NFPA 13 (i.e., area reduction for quick response and 30% increase for sloped ceil- ings). Use the most demanding calculation. Dry Systems - Calculate the most demanding seven BB Sprinklers plus up to two most demanding Stand Spray Sprinklers, and then calculate the most demanding de- sign area (including all sprinkler types) per NFPA 13 (i.e., 30% in- crease for sloped ceilings and 30% increase for dry systems). Include all sprinkler types within this area (see adjacent figure). Use the most demanding calculation. FIRST CALCULATION \. . •\\\\ _____ _____ : 0 •-4---•- • S DRY SYSTEM SHOWN SECOND CALCULATION 0\0 S RDCF p •__•_-__--+-__•_ p p ( •, /• O. F i 1/0 DRY SYSTEM SYSTEM SHOWN NOTE: Dry Pipe = 1500 SQ. FT. (NFPA Light Hazard)x 1.3 x 1.3 = 2535 SQ. FT. TFP6IO Page 25 of 28 FIGURE 20-C-4. BB SPRINKLERS, SD SPRINKLERS, HIP SPRINKLERS, & STANDARD SPRAY SPRINKLERS AT THE HIP Where the total number of Standard Spray Sprinklers at the hip is four or less: Wet Systems - Calculate the most demanding five BB, SD, or HIP Sprin- klers plus up to two most demanding Standard Spray Sprinklers. Dry Systems - Calculate the most de- manding nine BB, SD, or HIP Sprin- klers plus up to two most demanding Standard Spray Sprinklers (Of the nine BB,SD, or HIP Sprinklers, calculate up to a maximum of seven BB Sprinklers, see adjacent upper figure). Where the total number of standard spray sprinklers at the hip is greater than four: Wet Systems - Calculate the most demanding five BB, SD, or HIP Sprin- klers plus up to two most demanding Standard Spray Sprinklers, and then calculate the most demanding remote design area (Including all sprinklers types) per NFPA 13 (i.e., area reduction for quick response & 30% increase for sloped ceilings). Use the most de- manding calculation. Dry Systems - Calculate the most de- manding nine BB, SD, or HIP Sprin- klers plus up to two most demanding Standard Spray Sprinklers (Of the nine BB,SD, or HIP Sprinklers, calculate up to a maximum of seven BB Sprinklers, see adjacent upper figure), and then calculate the most demanding design area (including all sprinkler types) per NFPA 13 (i.e., 30% increase for sloped ceilings & 30% increase for dry sys- tems). Include all sprinklers types with- in this area (see adjacent figure). WALL OR DRAFT CURTAIN DRY SYSTEM SHOWN FIRST CALCULATION DRY SYSTEM SHOWN SECOND CALCULATION * a H D E '. —. . —+ • T 35SCfl (2355 DRY SYSTEM SHOWN NOTE: Dry Pipe =15OO SQ. FE (NFPA Light Hazard) xi.3x13=2535SQ. Ft TFP6IO Page 26 of 28 FIGURE 20-C-5. BB, SD, OR HIP SPRINKLERS & STANDARD SPRAY SPRINKLERS IN A DORMER, AT CROSS, AT HIP, ORATAN ELL Where the quantity of standard spray sprinklers -in each dormer, cross, or ell is four or less (see adjacent figure) and all of the dormers, crosses and ells meet the maximum four standard sprinkler criteria, calculate the At- tic Sprinkler demand as described in Part A-i thru A-6 or Part B-i thru B-4, plus up to two of the most demand- ing standard spray sprinklers in the dormer, cross, or ell that is adjacent to the Attic Sprinklers that are being in- cluded in the demand calculation. Where the quantity of standard spray sprinklers in any dormer, cross, or ell is greater than four, refer to Figure C-3. STANDARD SPRAY SPRINKLERS (4 OR LESS) I P STANDARD SPRAY SPRINKLERS (4 OR LESS) i7tt, STAN SP (4 STANDARD SPRAY SPRINKLERS (4 OR LESS) FIGURE 20-C-6. BB, SD, OR HIP SPRINKLERS & STANDARD SPRIN- KLERS SEPARATED BY COMPART- MENTALIZATION Calculate the Attic Sprinkler demand as described in Part A-i thru A-6 or Part C-i thru C-4, and then calculate the Standard Spray Sprinklers per NFPA 13. Use the most demanding calculation (see adjacent figure). N. ..'\ RIDGE • . / ,/• - WALL .1. DORMER BUILT ON TOP OF ROOF OR SHEATHING RIDGE 100' (25,4 m) T 60'(15,2 m) (5,1 n) (10,2 H 100'(25,4m) I 20' 60'( 152 20' (5,1 m) , m) (5,1 m) : 40 (10,2 m) / TFPGIO Page 27 of 28 MODEL AP SPRINKLERS WET PIPE SYSTEM 12 i 100'(25,4 m) - (5,1 M) - 60' (15,2 m) (5,1 M) (1 m) $ $ -+- - 100 (25,4 m) 20 152 60'( m) ______ 20 (5,1 m) j (55 m) (10,2m) (Ref. Figure 20-13-3) - Calculation 1: Calculate the most demanding five BB Sprinklers plus the two most de- manding AP Sprinklers. Calculation 1 Calculation 2: Calculate the most demanding area up to 1500 ft2 having AP Sprinklers. In this case the design area will be 800 ft2 (40 ft. x 20 ft.) Use the most demanding calculation - (i.e., for proving the adequacy of the water supply). Where AP Sprinklers are utilized, CPVC pipe may be used to supply the AP Sprinklers, as well as the ceil- Calculation 2 ing sprinklers below the AP Sprin- klers (See Page 6). STANDARD SPRAY SPRINKLERS WET PIPE SYSTEM (Ref. Figure 20-C-3) Calculation 1: Calculate the most demanding five - BB Sprinklers plus the two most de- manding Standard Spray Sprinklers. Calculation 2: Calculate the most demanding re- Calculation 1 mote design area (Including all sprin- klers types) per NFPA 13 (i.e., area reduction for quick response & 30% increase for sloped ceilings). In this case the theoretical design area is 1463 ft2 (1500 ft2 x 0.75* x 1.3). The actual design area, however, will - need to be 1520 ft2 to pick up the entire coverage area of the last BB Sprinkler. Use the most demanding calculation Calculation 2 (i.e., for proving the adequacy of the water supply). Where Standard Sprinklers are uti- lized, CPVC pipe CANNOT be used to supply the Standard Spray Sprin- klers or the ceiling sprinklers below the Standard Spray Sprinklers. * A 25% reduction for 20 ft. ceiling. FIGURE 21 EXAMPLE FOR A WET PIPE SYSTEM HYDRAULIC DESIGN AREA COMPARISON OF MODEL AP SPRINKLERS VERSES STANDARD SPRAY SPRINKLERS WHERE MODEL AP OR STANDARD SPRAY SPRINKLERS ARE USED IN HIP AREAS OUTSIDE THE SCOPE OF APPLICATION FOR MODEL BB BACK-TO-BACK SPRINKLERS TFP6IO Page 28 of 28 12 i 20, I 100' (25,4 m) (5,1 m) - 60' (15,2 m) (5,1rn) 40, (10,2m) , Calculation 1 100' (25,4 m) -- (51m) 60' (15,2 m) 20, (5,1 m) (10,2 m) • I I I I I • I I • Calculation 2 MODEL AP SPRINKLERS DRY PIPE SYSTEM (Ref. Figure 20-B-3) Calculation 1: Calculate the most demanding seven BB Sprinklers plus the two most de- manding AP Sprinklers. Calculation 2: Calculate the most demanding area up to 1950 ft2 having AP Sprinklers. In this case the design area will be 800 ft2 (40 ft. x 20 ft.) Use the most demanding calculation (i.e., for proving the adequacy of the water supply). 12 1 100' (25,4 m) (5Th) 60' (15,2 rn) (5Th) (1 0,2 m) • • • _4_+_4_Kc\\ Calculation 1 -, 100' (25,4 m) (5,1 M) - 60'(15,2 m) (5rn) IN V (10,2 m) Calculation 2 STANDARD SPRAY SPRINKLERS DRY PIPE SYSTEM (Ref. Figure 20-C-3) Calculation 1: Calculate the most demanding seven BB Sprinklers plus the two most de- manding Standard Spray Sprinklers. Calculation 2: Calculate the most demanding re- mote design area (Including all sprin- klers types) per NFPA 13 (i.e., 30% increase for sloped ceilings & 30% increase for dry systems). In this case the theoretical design area will be 2535 ft2 (1500 ft2 x 1.3 x 1.3). The actual design area, however, will- need to be 2720 ft2 to pick up the entire coverage area of the last BB Sprinkler. Use the most demanding calculation (i.e., for proving the adequacy of the water supply). FIGURE 22 EXAMPLE FOR A DRY PIPE SYSTEM HYDRAULIC DESIGN AREA COMPARISON OF MODEL AP SPRINKLERS VERSES STANDARD SPRAY SPRINKLERS WHERE MODEL AP OR STANDARD SPRAY SPRINKLERS ARE USED IN HIP AREAS OUTSIDE THE SCOPE OF APPLICATION FOR MODEL BB BACK-TO-BACK SPRINKLERS GLOBAL HEADQUARTERS 1 1400 Pennbrook Parkway, Lansdale, PA 19446 1 Telephone +1-215-362-0700 Copyright © 2014 Tyco Fire Products, LP. All rights reserved. tyca TEFLON is a trademark of The DuPont Corporation Fire Protection Products Rl7pMaster i a trailemirk cit Thci I i ihri,ril C'Mrrinraticin ES-A-3000SS EXISTING BACKFLOW - FOR REFERENCE ONLY Series 3000SS A M E S Double Check Detector Assemblies.' ssemblies FIRE Sizes: 21/2 - 12' (65— 300mm) Series 3000SS Double Check Detector Assemblies are designed for use in accordance with water utility non health hazard containment requirements It is mandatory to prevent the reverseflow of fire protection system substances, i.e., glycerinwetting agents, stagnantwater and water of non-potable quality from being pumped or siphoned into the potable water supply. Specifications A Double Check Detector Assembly shall be installed on fire protection systems when connected to a drinking water supply. Degree of hazard present is determined by the local authority having jurisdiction. The main valve body shall be manufactured from 300 Series stainless steel to provide corrosion resistance, 100% lead free* through the waterway. The double check detector assembly consists of two independently operat- ing, spring loaded check valves, two UL, FM, OSY resilient seated gate valves, and bypass assembly. The bypass assembly consists of a meter (cubic ft. or gallons), a double check including shutoff valves and required test cocks. Each cam-check shall be internally loaded and provide a positive drip tight closure against reverse flow. Cam-check includes a stainless steel cam arm and spring, rubber faced disc and a replaceable seat. There shall be no brass or bronze parts used within the cam-check valve assembly. The check valve seats shall be of molded thermoplastic construction. The use of seat screws as a retention method is prohibited. All internal parts shall be accessible through a single cover on the valve assembly. The valve cover shall be held in place through the use of a single grooved style two-bolt coupling. The bypass line shall be hydraulically sized to accurately measure low flow. The bypass line shall con- sist of a meter, a small diameter double check assembly with test cocks and isolation valves. The bypass line double check valve shall have two independently operating modular poppet check valves, and top mounted test cocks. The assembly shall be an Ames 3000SS. Materials Features Cam-Check Assembly valve provides low head loss Short lay length is ideally suited for ret- rofit installations Stainless Steel body is halt the weight of competitive designs reducing installa- tion and shipping cost Stainless steel construction provides long term corrosion protection and maximum strength Single top access cover with two-bolt grooved style coupling for ease of main- tenance No special tools required for servicing Compact construction allows for smaller vaults and enclosures Furnished with 5/8" x 3/4' bronze meter (gpm or cfm) Detects underground leaks and unauthorized water use Maybe installed horizontal or vertical "flow up" position Available Models Suffix: LG - less shutoff valves OSY - UL/FM outside stem and yoke resil- ient seated gate valves OSY FxG - flanged inlet gate connection and grooved outlet gate connection OSY GxF - grooved inlet gate connection and flanged outlet gate connection OSY GxG - grooved inlet gate connection and grooved outlet gate connection CFM - cubic feet per minute All internal metal parts: 300 Series stainless steel, Main valve body: 300 Series stainless steel, GPM - gallons per minute meter Check assembly: Noryl® Flange dimension in accordance with AWWA Class D. Post indicator plate and operating nut Noryl® is a reaistered trademark of General Electric Company. available - consult factory l Ii'E It is illegal to use this product in any plumbing system providing *The wetted surface of this product contacted water for human consumption, such as drinking or dishwashing, by consumable water contains less than in the United States. Before installing standard material product, 0.25% of lead by weight. consult your local water authorfty, building and plumbing codes. Job Name - Contractor Job Location Approval Engineer Contractor's P.O. No. Approval - Representative Ames product specifications in U.S. customary units and metric are approximate and are provided for reference only. For precise measurements, please contact Ames Technical Service. Ames reserves the right to change or modify product design, construction, specifications, or materials without prior notice and without incurring any obligation to make such changes and modifications on Ames products previously or subsequently sold. amesfirewater.com Pressure - Temperature Temperature Range: 33°F - 110°F (0.5°C - 43°C) Maximum Working Pressure: 175psi (12 bar) Capacity Flow curves astested by Underwriters Laboratory perUL1469, 1996. Rated flow **UL Tested .r .. • ___. u_u i • I_______u II I• _______. I__. I• iraim JM•••••••••• •••U• •••••••••U ••r4• u•aum- a••• C [o 0 0 00. I L A Standards ASSE 1048, AWWA C510-92, GSA B64.5, UL 1469 Approvals UL Classified (OSY only), FM (sizes 21/2° - 10, OSY only) fISSE :8:::1 SSIl!,, o-® kPa psi 6" (150mm) * ** 103 15 83 12 62 9 41 6 21 3 0 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 gpm 380 760 1140 1520 1900 2280 2660 3040 3420 3800 4180 4560 4940 5329 5700 1pm 5 10 15 fps 1.5 3 4.6 'mps kPa psi 8" (200mm) * ** 83 12 - 62 9 41 6 - 213 0 2500 gpm 250 500 750 1000 12501500 1750 20002250 950 1900 2850 3800 4750 5700 6650 7600 8550 9500 1pm 5 10 15 fps 1.5 3 46 mps kPa Pd 10" (250mm) * ** 103 15 83 12 62 9 41 6 21 3 0250 500 750 1000 1250 1508 1750 2000 2250 2500 3000 3500 gpm 950 1900 2850 3800 4750 5700 6650 7600 8550 9500 11400 13300 1pm 5 10 fps 1.5 3 mps 12" (300mm) kPa psi 110 16 - 97 14 -- 83 12 69 10 - 558 41 6 28 4 14 2 0 500 1000 1500 2000 2500 3000 3500 40DO 4500 gpm 1900 3850 5700 7600 9500 11400 13300 15200 17180 1pm 5 10 fps 1.5 3 sips Open) SIZE (DN) DIMENSIONS NET WEIGHT NET llWEIGHT 1 in. mm in. A mm in. C (OSY) mm in. 0 mm G in. mm L in. mm P in. mm w/Gates lb.kg. w/o Gates lb. kg- 21/2 65 37965 163/8 416 31/2 89 10250 22559 121/2 318 15570 6831 380 38965 18/479 33/4 95 10250 22559 13330 230104 7032 4100 401016 22/4578 41/2 114 10250 22559 141/2 368 240109 7333 6150 481/2 1232 301/8 765 51/2 140 15381 271/2 699 151/2 394 390177 12054 8200 521/2 1334 373/4 959 6I4 171 15381 291/2 749 181/2_464 572259 18082 10250 551/2 1410 453/4 1162 8200 1 15381 1 291/2 749 191/2 495 774351 1 19086 12300 571/2 1461 531/8 1349 91/2 241 1 15381 1 291/2 749 21533 1044474 1 220100 AL AMES Iá19OO1-2OO8 FIRE&WATERWORKS amesfirewater.com ''J P RT IFI ED A. Watts Water Technologies Company USA: Backflow- Tel: (916) 928-0123 • Fax: (9 16) 928-9333 Control Valves- Tel: (713) 943-0688 • Fax: (713) 944-9445 Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 Latin America: Tel: (52) 81-1001-8600 ES-A-3000SS 1410 © 2014 Ames Fire & Waterworks Approvals/Listings: VicFlexTM Sprinkler Fittings X.A_C_t:aU1id Series AH1, AH2 and AH4 Braided Flexible Hose Assemblies 10.85 Brackets: Style AB1 for suspended and hard-lid ceilings, allows installation before ceiling tiles in place Style AB2 for hard-lid ceilings, allows for vertical sprinkler adjustment Style AB4 for hard-lid ceilings with hat-furring channel grid systems, allows for vertical sprinkler adjustment USTED See ViCtSLIh: Publcalon 1001 kr more details. Product Description: VicFlex sprinkler fittings provide sprinkler installation on suspended ceiling grids, wood or metal stud/joist or hat furring channel hard-lid ceilings utilizing a flexible, stainless steel hose and steel bracket assembly. Refer to the Installation Manual for all applicable ASTM ceiling material and installation standards. System Components Hoses: Series AH1 Braided Hose Series AH2 Braided Hose Series AH4 Braided Hose Assembly lengths: 31, 36, 48, 60, 72°/90, 914, 1220, 1525, 1830mm. Note: length includes branch-line nipple and 5.757140mm straight reducer. Sprinkler Reducers: ½" and A"/15 and 20 mm sprinkler connections and 5.75°/140mm, 97230mm, 13/330mm straight lengths and short, long 90 elbows. Note: The short 900 elbow is typically used with concealed sprinklers while the long 90 elbow is typically used in the installation of recessed pendent sprinklers. Branch Connections: 1/25mm NPT or BSPT branch line nipples for attaching to rigid pipe. 34'720mm NPT or BSPT available for VdS. Job/Owner System No. Location Contractor Submitted By Date Style A137 for suspended ceilings and hard-lid ceilings Style A137 Adjustable for suspended and hard-lid ceilings Style AB8 for hard-lid ceilings (regionally available) Style AB9 for hard-lid ceilings with hat furring channel grid systems Style AB10 for Armstrong® TechZone ceilings Engineer Spec Section Paragraph Approved Date victaulic.com I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 10.85 5839 Rev U Updated 08/2014 © 2014 victaulic Company. All rights reserved. 1 jtauIIc victauUccom I VicFlex Sprinkler Fittings I AH1 I AH21 AH4 I Publication 10.85 Technical Specifications: Material Specifications: Maximum Working Temperature: 2250F/1070C Maximum Working Pressure: 200 psi/1375 kPa (FM Approval) 175 psi/1206 kPa (cULus Listed -Series AH2 only) 1600 kPa/232 psi (VdS Approved) Connections: To branch line (inlet) via 1/25.4 mm NPT or BSPT male thread OR To branch line (inlet) via A'/20 mm BSPT male thread (VdS only) To sprinkler head (outlet) via ½' or A"/15 mm or 20 mm NPT or BSPT female thread Minimum Bend Radius: 77178 mm (FM Approval) 2/51 mm (cULus Listed - Series AH2 only) 3/76.2 mm (cULus Listed - Series AH1 only) 3/76.2 mm (VdS Approved) Maximum Allowable Sprinkler K-Factors: FM (½"/15mm reducer) K5.6/8,1 (SI.) (3A/20mm reducer) K14.0/20,2 (S.l.) cULus (1/2'/15mm reducer) K8.0/11,5 (SI.) (3%'/20mm reducer) K14.0/20,2 (SI.) VdS (½"/lSmm reducer) K5.6/8,1 (SI.) (34'/20mm reducer) K8.0/11,5 (S.l.) Series AH1 Flexible Hose: Type 304 Stainless Steel Collar/Weld Fitting: Type 304 Stainless Steel Gasket Seal: Victaulic EPDM Isolation Ring: Nylon Nut and Nipple: Carbon Steel, Zinc Plated Reducers (½ or /4"): Carbon Steel, Zinc-Plated Series AH2 Flexible Hose: Type 304 Stainless Steel Collar/Weld Fitting: Type 304 Stainless Steel Gasket Seal: Victaulic EPDM Isolation Ring: Nylon Nut and Nipple: Carbon Steel, Zinc Plated Reducers (1/2 or /4"): Carbon Steel, Zinc-Plated Series AH4 Flexible Hose: Type 304 Stainless Steel Collar/Weld Fitting: Type 304 Stainless Steel Gasket Seal: EPDM per ASIM D2000 Isolation Ring: N/A Nut and Nipple: Carbon Steel, Zinc-Plated Reducers (½ or /4"): Carbon Steel, Zinc-Plated Brackets: Carbon Steel, Zinc-Plated 10.85 5839 Rev u updated 08/2014 © 2014 Victaulic Company. All rights reserved. victaulic.com 2 \j'1tauIic victaulic.com I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 FRICTION LOSS DATA: USTED C -Series AH2 Braided Hose with Straight 5.75" Reducers -Style AB1 and AB10 Brackets Series AH2 Hose Maximum Length of Equivalent Length Number of Stainless Steel of 1"/33.7mm 90 Bends at 2I51mm Flexible Hose Outlet Size Sch. 40 Pipe (C=120) Bend Radius inches inches/type feet/meters 1,V/Straight 16/4.9 4 31 1/4 /Straight 17/5.2 4 1/2"/Straight 21/6.4 5 36 -.---.---- .wlStraight .23P 5 8 8 48 34"/Straight .............. . .... 37/11.3 8 ½"/Straight 46/14.0 10 60 S!aiht 46/14.0 10 1/2"/Straight 55/16.8 12 72 3/4 /Straight 53/16.2 12 Series AH2 Braided Hose Equivalent Length Design Guide I Equivalent length values at various numbers of 90 degree bends at 2/51mm center line bend radius Length of Stainless Steel Flexible Outlet 1 2 3 4 5 6~in 8 9 10 11 12 Hose Size 0 Bends Bends Bends Bends Bends Bends Bend Bends Bends Bends Bends Bends inches inches feet/meters 1 W 5.0/1.5 8.5/2.6 11.0/3.4 13.0/4.0 16.0/4.9 N.A N.A N.A N.A N.A N.A N.A N.A 3/4 6.5/2.0 10.0/3.0 12.5/3.8 14.0/4.3 17.0/5.2 N.A N.A N.A N.A N.A N.A N.A N.A W 10.5/3.2 13.5/4.1 1 16.0/4.9 18.0/5.5 19.0/5.8 21.0/6.4 N.A N.A N.A N.A N.A N.A N.A 6 3/4 12.0/3.7 14.0/43 17.0/5.2 19.5/5.9 20.0/6.1 23.0/7.0 N.A N.A NLA N.A N.A N.A N.A ½ 11.5/3.5 15.5/4.7 17.0/5.2 19.5/5.9 20.0/6.1 21.0/6.4 22.0/6.7 28.0/8.5 32.0/9.8 N.A N.A N.A N.A 8 13.0/4.0 17.0/5.2 19.0/5.8 21.5/6.6 24.5/7.5 26.0/7.9 27.0/8.2 30.0/9.1 37.0/11.31, N.A N.A N.A N.A 1/2 15.5/4.7 21.5/6.6 24.0/7.3 27.0/8.2 28.5/8.7 30.0/9.1 31.0/9.4 37.0/11.3 42.0/12.844.0/13.4 46.0/14.01 N.A N.A 60 - 3/4' 16.0/4.9 123.on.0 24.0/7.3 28.0/8.5 29.5/9.0 30.5/9.3 j38.0/11.6 42.0/12.81440/13.4 46.0/14.01 N.A N.A 32.0/9.8 36.5/11.1.37.5/11.4140.5/12.5 41.0/12..L12,8 46.0/14.049.0/14.9 52.0/15.854.0/16.5 55.0/16.81 72 3%' 24.0/7.3 32.0/9.8 32.5/9.9 35.0/10.7 21 4 41.O/12.S I6.0/14.050.0/15.2 S1.0/1S.Si52.0/15.8 53.0/16.2 Note: values for use with 5.75' straight reducers. How to use this Design Guide: I For some systems, it may be advantageous for the designer to calculate the system hydraulics using shorter equivalent lengths associated with fewer than the maximum allowable number of bends. In this case, the designer may select a design number of bends for the job and use the associated equivalent length from the design guide to determine the system hydraulics. 2 It is possible that the actual installed condition of some of the flexible drops may have more bends than the designer selected. When this happens, the design guide may be used to find equivalent lengths based on the actual installed number of bends for particular sprinkler installations. The system hydraulics can be recalculated using actual equivalent lengths to verify the performance of the system. 10.85 5839 Rev u updated 08/2014 0 2014 victaulic Company. All rights reserved. victaulic.com 3 ___________ victauliccom I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 1085 FRICTION LOSS DATA: LITED -Series AM Braided Hose with Straight 5.75 Reducers -Style AB1 and AB10 Brackets Series AH1 Hose Length of Equivalent Length Stainless Steel of 1'/33.7mm XBend3"n6.2mm Flexible Hose Outlet Size Sch. 40 Pipe (C=120) inches inches/type feet/meters 31 - 1/2"/Straight 3/4"/Straight 52/15.8 ./ 3 55/16.8 3 36 ½"/Straight 3/4"/StLi~l 911t 63/19.2 4 66/20.1 . . 48 ½/Straight 36"/Straight 78/23.8, 4 80/2( 4 60 ½"/Straight 36"/Straight 8)f6.8 4 ,/90/27.4 4 72 ½"/Straight 1/4"/Straight 112/34.1 5 118/36.0 5 Series AM Braided Hose Equivalent Length Design Length of I Stainless : .0•• Steel Flexible Outlet 1 3 4 5 Hose Size 0 Bends Bends Jill nds _Bends Bends Bends feet/meters inches inches ½ " 22 732 42 52 N.A N.A 31 3/4" 2,/ 33 44 55 N.A N.A ½ " 33 43 1 53 63 N.A 36 3/4" 26 36 46 1 56 66 N.A 48 16 36 46 57 68 78 N.A 40 51 60 . 71 80 N.A ½ /" 46 56 67 77 88 N.A 60 / 3/4" 47 5 58 69 80 90 . N.A 1/2" 59 1 69 79 91 102 j 112 3/4" 62 173 84 95 106 118 Note: Values for use with 5.75" straight reducers. How to use this Design Guide: 1 For some systems, it may be advantageous for the designer to calculate the system hydraulics using shorter equivalent lengths associated with fewer than the maximum allowable number of bends. In this case, the designer may select a design number of bends for the job and use the associated equivalent length from the design guide to determine the System hydraulics. 2 It is possible that the actual installed condition of some of the flexible drops may have more bends than the designer selected. When this happens, the design guide may be used to find equivalent lengths based on the actual installed number of bends for particular sprinkler installations. The System hydraulics can be recalculated using actual equivalent lengths to verify the performance of the system. 10.85 5839 Rev U Updated 08/2014 © 2014 Victaulic company. All rights reserved. victaulic.com 4 xt A_______ victaulic.corn I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 FRICTION LOSS DATA: -Series AH1, AH2 and AH4 Braided Hose -Various brackets specific to hose Series AH1 Hose Series AH2 Hose Series AH4 Hose - For use with Style AB1, AB2, For use with Style AB1, AB2, AB4, AB7, AB7 Adj., AB8, AB9 AB4, AB7, AB7 Adj., AB8, AB9 For use with Style AB1, AB7, AB8, and AB10 VicFlex Brackets and AB10 VicFlex Brackets and AB9 VicFlex Brackets Maximum Maximum Maximum Length of Stainless Equivalent Number of Equivalent Number Equivalent Number Steel Length of 900 Bends at I Length of of 900 Bends at Length of of 900 Bends at Flexible Sprinkler Outlet 10133.7mm 7"I178mm Bend 1°I33.7mm 7'I178mm 1"/33.7mm 7/178mm Hose* K-Factor Size Sch. 40 Pipe Radius Sch. 40 Pipe Bend Radius Sch. 40 Pipe Bend Radius inches mperial/S.l inches/type feet/meters feet/meters feet/meters ½'/5trai9ht53.8/16.4 23.5/7.1 31 5.6/8.1 Elbow 53.8/16.4 2 23/7.0 2½'/90 2 ----- 21.7/6.6 2trihL. 63.7/19.4 27.8/8.5 29.7/9.0 36 56/81 2 27.7/8.4 2 29.8/9.0 2 1/2'/90_Elbow 63.1/19.2 _7Straigt 87.9/26.8 38.2/11.6 27.5/8.3 48 5.6/8.1 37.4/11.4 . 29.2/8.9 W/90' Elbow 85.8/26.1 112.2/34.1 42.4/12.9 35.7/10.9 60 56/81 43/13.1 37.2/11.3 1/2 1/2"/Straight ' /90 Elbow 108.4/33.0 725.6/8.1½VStra ight 136.5/41.6 4 1/2'/90' Elbow 131.1/39.9 48.5/14.7 4 47.5/14.5 4 jStrait 44.4/13.5 20.7/6.3 31 80/115 2 20.5/6.2 2 14.6/4.4 2 6'/90 Elbow 47.6/14.5 jStraiht 55.6/16.9 25.0/7.6 21.7/6. 36 8.0/11.5 2 57.5/17.5 24.6/7.5 2 22.4/6.8 2 3/4'/90 Elbow 3 StrhL. 82.8/25.2 35.5/10.8 21.2/6.4 48 8.0/11.5 81.7/24.9 34.7/10.6 3/'/90' Elbow 34'/Straight 110.1/33.5 39.6/12.1 27.9/8.5 60 8.0/11.5 40.1/12.2 28.9/8.8 4/90' Elbow 105.9/32.2 3/4"/Straight 137.3 43.5/1 3.2 38.8/11.8 72 8.0/11.5 45.2/13.7 39.4/12.0 /4/90 Elbow 130.2/39.7 34/Straiqht 45.5/13.8 17.8/5.4 16.4/5.0 31 11 2/161 • 2 18/5.5 2 19.9/6.1 2 /.4'/90' Elbow 47.1/14.3 JStraihL 66.3/20.2 22.2/6.7 21.7/6.6 36 11.2/16.1 2 22.1/6.7 2 24.2/7.4 2 3/4'/90' Elbow 57.5/17.5 3/4 /Strai9L 82.7/25.2 32.9/10.0 28.5/8.7 48 11 2/161 • 32.1/9.8 - 29.9/9.1 ~'/90 Elbow • 82.8/25.2 3/4'/Straight 109.1/33.2 36.8/11.2 34.7/10.5 60 11 161 / • 108.1/32.9 37.1/11.3 30.3/9.2 ~'/90'Elbow 3/4"/Straght 135.5/41.3 40.5/12.3 38.6/11.6 4 72 112/161 41.9/12.7 1.38.6/11.7 ~'/90Elbow 133.4/40.6 ._Ltrai!_. 44.3/13.5 14.9/4.5 16.3/5.0 31 140/202 2 46.4/14.1 15.5/4.72 2 19.9/6.1 4'/90'Elbow 36 14.0/20.2 7traiht 55.5/16.9 2 19.4/5.9 W/90' Elbow 56.7/17.3 19.6/5.9 24.2/7.4 3 S!!ai. .83.0/25.3 .30.3/9.2 28.3/8.6 48 140/202 3/4"/90* Elbow 82.1/25.0 29.5/8.9 29.9/9.1 3/traight 110.4/33.6 33.9/10_J 34.9/10.6 60 140/202 4 34.1/10.4 30.3/9.2 /4/90_ Elbow 107.5/32.7 3 LSt!t 137.9/42.0 37.5/11.4 41.5/12.6 72 140/202 • 38.6/11.7 ___38.6/11.7 14'/90'Elbow 132.8/40.4 FM Notes: Series AH1, AH2 and AH4 have been tested and Approved by FM Global for use in wet, dry and preaction systems per NFPA 13, 13R, and 13D and FM data sheets 2-0, 2-5, and 2-8. FM 1637 and Vds standards for safety include, but are not limited to, pressure cycling, corrosion resistance, flow characterisitics, vibration resistance, leakage, mechanical and hydrostatic strength. Differences in equivalent lengths are due to varying test methods, per FM 1637 and VdS standards. Refer to these standards for additional information regarding friction loss test methods. EXAMPLE: A 48-inch hose installed with two 30° bends and two 90° bends at a 7-inch bend radius is permitted and considered equivalent to the data in the table shown above. In this example, the total number of degrees is 240°, which is less than the allowable 270°. 10.85 5839 Rev U updated 08/2014 © 2014 Victaulic Company. All rights reserved. victaulic.com 5 \J$$tauIic victaulic.com I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 FRICTION LOSS DATA; VdS -Series AH1, AH2 and AH4 Braided Hose -Style AB1, AB2, AB4, AB7, AB7 Adj., AB8, AB9, and AB10 Brackets Series AH1 Hose Series AH2 Hose Series AH4 Hose Equivalent Length of Equivalent Length of 1 Equivalent Length of steel pipe according to steel pipe according to i steel pipe according to EN 10255 DN 20 EN 10255 DN 25 EN 10255 DN 25 Maximum Number (26,9 x 2,65) and (33,7 x 3,25) and (33,7 x 3,25) and of 90 Bends at Length of Stainless Outlet relating to a flow relating to a flow relating to a flow 3/76.2mm Bend Steel Flexible Hose Size velocity of 5 m/s velocity of 5 m/s velocity of 5 m/s Radius mm/inches mm/inches type meters/feet meters/feet meters/feet 790/31 15mm 1W / Straight 4.0/12.9 5.5/18.0 5.5/18.0 3 20 mm / W / Straight 915/36 4.6/15.0 6.4/21.0 6.4/21.0 3 20 .mm/~/Straht l5mm/W/Straight 1220/48 6.1/20.0 20 mm / W/ Straight 8.5/27.9 8.5/27.9 3 j/Strai!, 1525/60 20 mm / 3/4'/ Straight 7.6/25.0 10.7/35.1 10.7/35.1 4 lsmm/½/Straight 1830/72 9.2/30.0 20mm/ "/Straight 12.8/42.0 12.8/42.0 4 VdS Ceiling Manufacturers List AB1, A132, A137, AB10 AMF Armstrong Chicago Metallic Dipling Durlum Geipel Gema-Armstrong Hilti Knauf Lafarge Linder Odenwald Richter Rigips Rockfon Pagos Suckow & Fischer USG Donn AB3 AB4/9 ABS No specific approval No specific approval 1. H/ti Kriauf Lafarge Lindner Rigips 10.85 5839 Rev U Updated 08/2014 © 2014 Victaulic Company. All rights reserved. victauIiccom 6 _________ Series AH2 Braided Hose Series AM Braided Hose Item Description 1 _2_ Flexible Hose Isolation Ring (series AH2 only) 3 Gasket 4 Nut Branch Line Nipple 6 Braid Collar/Weld Fitting 8 Sleeve (AH2 Only) victauliccorn I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 Product Details - Series AH1 Braided Hose Hose Length Dimensions Hose Length A B 31 36 25.25 31.25 31 36 48 42.25 48 .60 54.25 - 60 72 66.25 72 Standard 5.75/140 mm straight reducer Optional 9.0/229 mm straight reducer 13.0/330 mm straight reducer 2.62'! 66.5 mm 4.837 1227mm Short 90° elbow reducer Long 90° elbow reducer Note: The Short 90° elbow reducer is typically used with concealed sprinklers while the longer 90 elbow is typically used in the installation of recessed pendent sprinklers. 10.85 5839 Rev U Updated 08/2014 02014 Victaulic company. All rights reserved. victauliccom . 7 \J'11tauIic' victaulic.comI VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 VicFlex Brackets Style AB1 Suspended Ceilings Hard-Lid Ceilings (FM Only) Item Description 1 24"/610mm 0r48"/1219mm Square Bar 2 Patented 1-Bee' Center Bracket 3 End Bracket *Both sizes FM/VdS approved, cULus listed Style AB2 Hard-Lid Ceilings Item Description 1 24'/61Ommor4871219mm Square Bar* 2 Patent-Pending adjustable Center bracket 3 End Bracket *Both sizes FM/VdS approved. Note: 5/3k or 4mm hex key required for adjustment Style AB4 Hard-Lid Ceilings with Hat furring channel grid system Item Description 1 24"/610mrn or 48/1219mm Square Bare 2 Patent-Pending adjustable Center bracket 3 End Bracket for Hat Furrina Channel Both sizes FM/VdS approved. Note: IA2 or 4mm hex key required for adjustment 10.85 5839 Rev U updated 08/2014 © 2014 Victaulic Company. All rights reserved. vdauhcom 8 \JtauIic VicFlex Brackets Style AB7 Suspended Ceilings Hard-Lid Ceilings Item Description 24/610mm or 48/1219mm Square Bar 2 I Patented 1-Bee2 Center Bracket 3 End Bracket *Both sizes FM/VdS approved. Style AB7 Adjustable Suspended Ceilings Hard-Lid Ceilings Item Description 700mm or 1400mm Square Bar* 2 i Patented 1-Bee2 Center Bracket 3 End Bracket (adjustable) *Both sizes FM and VDS approved Style AB8 Hard-Lid Ceilings Item Description 700mm or 1400mm Square Bar* - 2 Patented 1-Bee2 Center Bracket 1 3 End Bracket (adjustable) *80th sizes FM/VdS approved Style AB9 Hard-Lid ceilings with Hat furring channel grid system Item I Description i_il 24"/610mm or 48/1219mm Square Bar 2 Patented 1-8ee2 Center Bracket 3 End Bracket for Hat Furrina Channel *Both sizes FM/VdS approved Style AB1O Suspended ceilings Armstrong® TechZone" Item Description 1 j 6*1152mm Square Bare 2 1 Patented 1-Bee Center Bracket 3 i End Bracket *FM/VdS approved, cULus listed. victaulic.com I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 10.85 5839 Rev U Updated 08/2014 © 2014 Victaulic Company. All rights reserved. victauliccom 9 \JttauIic victau!ic.corn I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication. 10.85 Braided Hose Assembly Suspended Ceiling Grid with Recessed Sprinkler - Clearances above ceiling tile at various center-line bend radii Hose Clearance Chart Dimension Inches/mm Minimum Bend RadiusR 2/50 3/80 4/100 5/125 6/150 7/175 Minimum 10.75/273 11.75/298.5 12.75/324 13.75/349 14.75/375 15.75/400 1,7/4 Typical ca Sr on Center P2707 '4119 MM MAX. RECESS V2707 3/4'/19mm Max. Recess Suspended Ceiling Grid with 90°Elbow (Long) Hose Clearance Chart I See Chart Dimension mm Min. 200 Note: Style AB1 and Series AH2 figures shown. Typical ceiling grid Variations of ceiling grids, sprinkler heads, brackets, and hoses are permitted but may result in clearance Seenotr differences from the figures above. i1mil!' 247610 10.85 5839 Rev U Updated 08/2014 © 2014 Victaulic company. All rights reserved. victaulic.com 10 x.A-c-taulic~ an V3802 ½'/12.7mm Max. Recess victauliccom I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 Series AQB Braided Hose Assembly Suspended Ceiling Grid with Hat Furring Channel Hose Clearance Chart Dimension Inches/mm Minimum Bend Radius 'R 2/50 3/80 4/100 5/125 6/150 ! 7/175 See Chart Minimum 10.3/262 11.3/287 12.3/313 13.3/338 14.3/363.5 15.3/389 See there e Note V2708 ½'/12.7mm Max. Recess Suspended Ceiling Grid with 9000bow (Short) Hose Clearance Chart Inches! Dimension mm 8 A Mm. 200 Note: Style AB9 and Series AH2 figures shown. Variations of ceiling grids, sprinkler heads, brackets, and hoses are permitted but may result in clearance differences from the figures above. 10.85 5839 Rev u updated 08/2014 © 2014 Victaulic Company. All rights reserved. victauliC.com 11 . \./tauIic victaulic.com I VicFlex Sprinkler Fittings I AH1 I AH2 I AH4 I Publication 10.85 Flexible Hose In-Plane Bend Characteristics TWO BENDS fi OR Minim " Minimum um bend radius end radius b Minimum bend radius ONE BEND Minimum> bend radius 2X Minimum Minimum bend radius bend radius OR Note: For out-of-plane (three-dimensional) bends- care must be taken to avoid imparting torsional stress on the hose Model Number Correlation VicFlex AquaFlexw Designation Designation Series AH4 Outlet Series AQB Series AFB Hose Size Hose Hose Assembly inches Assembly Assembly AI-1431 ½ AQB31HLD AFB31HLD AQB31TLD AFB31TLD - 3/4 A11436 ½ AQB36HLD AFB36I-ILD - 3/4 AQB36TLD AFB36TLD ½ AQB48HLD AFB48HLD AH4-48 AQB48TLD AFB48TLD 3/4 AH460 ½ AQB60HLD AFB60HLD AQB60TLD 1 AFB60TLD - 34 ½ AQB72HLD AFB72HLD AH472 AQB72TLD i AFB72TLD - 3/4 WARNING . It is the responsibility of the system designer to verify suitability of Type 304/304L stainless steel flexible hose for use with the intended fluid-media within the piping system and external environments. S The effect of chemical composition, pH level, operating temperature, chloride level, oxygen level, and flow rate on Type 3041304L stainless steel flexible hose must be evaluated by the material specifier to confirm system life will be acceptable for the intended service. Failure to follow these instructions could cause product failure, resulting in serious personal injury and/or property damage. Installation Note Reference should always be made to the I-iCC Vi&lic Field lni:silaor Huirdhook for This product shall be manufactured by Victaulic or to Victaulic specifications. All products the product you are installing. Handbooks are included with each shipment of Victaulic to be installed in accordance with current Victaulic installation/assembly instructions. products for complete installation and assembly data, and are available in PDF format Victaulic reserves the right to change product specifications, designs and standard on our website at www.victaulic.com, equipment without notice and without incurring obligations. Warnanty Trademarks Refer to the Warranty section of the current Price List or contact Victaulic for details. Victaulic and VicFleo are registered trademarks of Victaulic Company. 10.85 5839 Rev U updated 08/2014 0 2014 Victaulic company. All rights reserved. vktauUccorn 12 JctauIicr : + + _,p I LI lot son . - 41P lot boo IN 10, + I :•+.+ +++1 ++ 1lr - + + -r!- . *? +-- Sc edu e- O®/Sc' du e-4 )®' Fully Listed and FM Approved Sprinkler Pipe When you specify Schedule- 10/Schedule-40 sprinkler pipe you get a UL listed and FM approved product. Although these products do not require separate approvals, Schedule-10/Schedule-40 gives you the extra quality assurance you demand. Our Sch-10 (11("-.- 8") pipe and Sch-40 (1"- 214) pipe have passed the same thorough lab testing as our other listed pipe products, and receive periodic mill inspections from both UL and FM agents to ensure consistent quality. Schedule-10/Schedule-40 product can be "hot-dip" galvanized to meet FM requirements for dry systems in accordance with the zinc coating specifications of ASTM A- 123. Our advanced formula mill coating of- fers a clean, durable surface. It is also paint-ready for custom color applications without special preparation. The internal surface of all black Allied Tube & Conduit Fire Sprinkler pipe products up to 4.5000" in diameter is coated with our new Antibacterial For- mula, "ABF". In scientific laboratory test, ABS proved to have superior resis- tance to microbial colonization of pipe walls, thereby delaying or possibly pre- venting the onset of Microbiologically Influenced corrosion (MIC) when the First Sprinkler System is first installed. Meets "Buy American" requirement c( and is available through distributors in the USA, Canada and Mexico. NPS In; mm Nominal I.D. In; mm Wt. Lbs/Fl; Kg/rn Sch-40 WI. (H20 Filled) Lbs/Ft; Kg/rn Specifications Pcs/ Lift Wt/Lift (21') Lbs; Kg WI/Lift (24') Lbs; Kg WI/Lift (25') Lbs, Kg z TuI049 1.680 2.05 70 2,470 2.5 3.03 70 1,120 1,26u 1.380 2.270 2.93 51 2,431 2,778 2,894 31" 1,313 Z -772' 1.610 2.720 3.61 44 2,513 2,872 4.0 3.37 44 1.140 I,3O37T ( 50 067 350 513 30 2.300 2628 ~liF 2738 21/2' 65 2.469 62.7 5.790 8.6 7.86 11.73 19 19 2,310 1,048 2,640 1,197 2,750 1,247 3 [0 Specifications NPS Nominal I.D. WI. WI. (H20 Filled) Pcs/ WI/Lift (21') WI/Lift (24') WI/Lift (25') In; mm In; mm Lbs/Fl; Kg/rn Lbs/Fl; Kg/rn Lift Lbs; Kg Lbs, Kg Lbs; Kg 1.097 1.400 1.81 91 2,675 3,053 3,185 25 27.9 2.1 2.70 91 1,213 1,385 1,445 11/4 " 1.442 1.810 2.52 61 2,319 2,664 2,760 32 36.6 2.7 3.75 61 1,052 1,208 1,252 11/2' 1.682 2.080 3.04 61 2,664 3,045 3,172 40 42.7 3.1 4.52 61 1,208 1,381 1,439 2.157 2.640 4.22 37 2,051 2,344 2,442 39 6.28 37 930 1Ufi3_j108 21/2" 2.635 3.530 5.89 30 2,224 2,542 2,648 1 1201 3.260 4.330 7.94 19 1,728 1,975 2,057 80 82.8 6.4 11.82 19 784 896 933 4.260 5.610 11.78 19 2,238 2,558 2,665 90 108.2 8.3 17.53 19 1,015 1,160 1,209 5.295 7.77 17.33 10 1,632 1,865 1,943 125 134.5 11.56 25.80 10 740 846 881 6.357 9.290 23.03 10 1,951 2,230 2,322 150 161.5 13.8 34.27 10 885 1,012 1,053 8' 8.249 16.490 40.15 7 2,424 2,770 2,885 200 209.5 24.5 59.75 7 1,100 1,256 1,309 Schedule-10/Schedule-40 pipe are in compliance with the following: ASTM A-135, and NFPA 13. Both pipe products have a working pressure rating of 300 psi maximum and also meet the stringent requirement for the following tests: OR Welded Outlets Hydrostatic Pressure Side Wall Rupture Vibration Test tL,CD a viral part of your world @ <~> 9 Listed Approved Listed 16100 S. Lathrop. Harvey, IL 60426 Customer Service: " allied 11350 Norcom Rd. . Philadelphia, PA 19154 (800) 882-5543 TUBE &CONDUIT 2525 N. 27th Ave. - Phoenix, AZ 85009 Fax 708-339-1806 S5 -3 tUCDJ Fire & Building .1 Products. Technical Services: Tel: (800) 381-9312 / Fax: (800) 791-5500 www.tyco-fire.com Grinnell Grooved Fire Protection Products Grooved Fittings General Description BJ 1 1 See Fire Protection [LI [VdSj Submittal Sheet for Pressure Rating and Listing/Approval U6 L Information The grooved fittings provide an economical and efficient method of changing direction, adding an outlet, reducing, or capping grooved piping systems. Grooved fittings are available in durable ductile iron or fabricated steel as indicated. Note: Figure 510S and 519S fittings are special short radius fittings with smaller center to end dimensions than standard grooved fittings. Depending on the size and coupling used, there maybe interferences at the bolt pads that require repositioning of the coupling orientation. The use of flange adapters is not recommended with Figures 510S and 519S fittings. Contact Tyco Fire Products for details. WARNING The Fittings described herein must be installed and maintainedin compliance with this document, as well as with the applicable standards of the National Fire Protection Association, in addition to the standards of any other authorities having jurisdiction. Failure to do so may impair the performance of this device. The owner is responsible for maintaining their fire protection system and devices in proper operating condition. The installing contractor or sprink/ermanufacturershould be contacted with any questions. Technical Data Approvals: UL, FM, ULC, VdS, and LPCB; Note: See Fire Protection Submittal Sheet for exact Listing I Approval information. Material: Cast: Figures: 201,210,219,250,260,501,510, 519, 51 ODE, 501S, 5105 and 519S - Ductile iron conforming to ASTM A-536, Grade 65-45-12 Fabricated Steel: Figures 391, 392, 393, 312, 313, 321, 327, 341 and 350 - Carbon Steel, (Sizes 11/4' - 6" are Schedule 40); (Sizes 8'- 12' are Schedule 30), conforming to ASTM A-53 Grade B Protective Coatings: Non-lead orange paint Fire brigade red (optional) non-lead paint Hot dipped galvanized conforming to ASTM A-153 Ordering Procedure When placing an order, indicate the full product name. Please specifythe quantity, figure number, wall thickness, and size. Grinnell Grooved Piping Products, valves, accessories and other products are available throughoutthe U.S., Canada, and internationally, through a network of distribution centers. You may write directly or call 215-362-0700 for the distributor nearest you. Care and Maintenance The owner is responsible for the inspection, testing, and maintenance of their fire protection system and devices in accordance with the applicable standards ofthe National Fire Protection Association (e.g., NFPA 25), in addition to the standards of any authority having jurisdiction. The installing contractor or product manufacturer should be contacted relative to any questions. Any impairment must be immediately corrected. It is recommended that automatic sprinkler systems be inspected, tested, and maintained by a qualified Inspection Service. Limited Warranty Products manufactured by Tyco Fire Products are warranted solely to the original Buyer for ten (10) years against defects in material and workmanship when paid for and properly installed and maintained under normal use and service. This warranty will expire ten (10) years from date of shipment byTyco Fire Products. No warranty is given for products or components manufactured by companies not affiliated by ownership with Tyco Fire Products orfor products and components which have been subject to misuse, improper installation, corrosion, orwhich have not been installed, maintained, modified or repaired in accordance with applicable Standards of the National Fire Protection Association (NFPA), and/orthe standards of any other Authorities Having Jurisdiction. Materials found byTyco.Rre Products to be defective shall be either repaired or replaced, at Tyco Fire Products' sole option. Tyco Fire Products neither assumes, nor authorizes any person to assume for it, any other obligation in connection with the sale of products or parts of products. Tyco Fire Productsshall not be responsi bleforsprinklersystem design errors or inaccurate orincompleteinformation supplied by Buyer or Buyer's representatives. IN NO EVENT SHALL TYCO FIRE PRODUCTS BE LIABLE, IN CONTRACT, TORT, STRICT LIABILITY OR UNDER ANY OTHER LEGAL THEORY, FOR INCIDENTAL, INDIRECT, SPECIAL OR CONSEQUENTIAL DAMAGES, INCLUDING BUTNOT LIMITED TO LABOR CHARGES, REGARDLESS OF WHETHERTYCO FIRE PRODUCTS WAS INFORMED ABOUT THE POSSIBILITY OF SUCH DAMAGES, AND IN NO EVENT SHALL TYCO FIRE PRODUCTS' LIABILITY EXCEED AN AMOUNT EQUAL TO THE SALES PRICE. THE FOREGOING WARRANTY MADE IN liEU OF ANY AND ALL OTHER WARRANTIES EXPRESS OR IMPLIED, INCLUDING WARRANTIES OF MERCHANTABILITY AND FITNESS FOR A PARI1CULAR PURPOSE. Page 1 of 6 September 2004 TFPISIO Figure 201 Figure 210 Figure 219 Figure 2601: 450 Elbow 90° Elbow Tee End Cap Nominal C to E Appx. WI. C to E Appx. Wt. C to E Appx. Wt. E to E Appx. Wt. Size Inches Lbs. Inches Lbs. Inches Lbs. Inches Lbs. mm Kg. mm Kg. mm Kg. mm Kg. 1 1 1 ' 0.9 2.75 1.0 2.75 1.4 0.88 0.4 44.5 0.4 69.9 0.5 69.9 0.6 1 22.4 0.2 11/20 1.75 1.1 2.75 1.2 2.75 1.8 0.88 0.6 44.5 0.5 69.9 0.5 69.9 0.8 22.4 0.3 20 2.00 1.8 3.25 2.0 3.25 2.7 0.88 0.9 50.8 0.8 82.6 0.9 82.6 1.2 22.4 0.4 1 2/2 2.2 3.75 3.0 3.75 5.8 0.88 0.9 57.2 1.0 95.3 1.4 95.3 2.6 22.4 0.4 76.1 mm 2.25 2.2 3.75 3.0 3.75 5.8 0.94 1.1 57.2 1.0 95.3 1.4 95.3 2.6 23.9 0.5 3.5 4.25 4.5 4.25 7.0 0.88 1.1 63.5 1.6 108.0 2.0 108.0 3.2 22.4 0.5 108.0mm 2.88 5.5 4.75 8.5 4.75 11.5 73.0 2.5 120.7 3.9 120.7 5.2 - - 3.00 5.2 5.00 8.5 5.00 11.8 1.00 2.6 76.2 2.4 127.0 3.9 127.0 5.4 25.4 1.2 133.0mm 3.25 7.7 5.25 11.3 5.25 10.6 82.6 3.5 133.4 5.1 133.4 4.8 - - 139.7mm 3.25 7.7 5.50 11.3 5.50 15.3 0.92 4.7 82.6 3.5 139.7 5.1 139.7 6.9 23.4 2.1 8.5 5.50 13.5 5.50 17.0 1.00 5.0 82.6 3.9 139.7 6.1 139.7 7.7 25.4 2.3 159.0mm 12.0 6.00 14.6 6.00 13.9 88.9 5.4 152.4 6.6 152.4 6.3 - - 165.1 mm ö 12.0 6.50 18.5 6.50 26.0 1.00 7.5 88.9 5.4 165.1 8.4 165.1 11.8 25.4 3.4 6" ö 12.0 6.50 18.5 6.50 26.0 1.00 7.5 88.9 5.4 165.1 8.4 165.1 11.8 25.4 3.4 216.3mm 23.0 7.75 36.5 7.75 45.0 108.0 10.4 196.9 16.6 196.9 20.4 - 80 4.25 23.0 7.75 36.5 7.75 45.0 1.19 12.8 108.0 10.4 196.9 16.6 196.9 20.4 30.2 5.8 10 475 31.0 9.00 60.0 9.00 72.1 1.25 20.0 120.7 14.1 228.6 27.2 228.6 32.7 . 1 9.1 12° 5.25 40.0 10.00 67.0 10.00 92.5 1.25 36.0 1334 18.1 254.0 30.4 254.0 42.0 31.8 1 16.3 Available with tapped plugs, contact Tyco Fire & Building Products. Friction Resistance* (Expressed as Equivalent Straight Pipe) Elbow The Size 900 450 Branch Run Feet Feet Feet Feet Inches MM Meters Meters Meters Meters 11/4 1.9 1.0 T 1.9 42.4 0.6 0.3 1.5 0.6 11/2 2.3 1.2 5.8 2.3 48.3 0.7 0.4 1.8 0.7 2 3.2 1.6 8.0 3.2 60.3 1.0 0.5 2.5 1.0 21/2 3.9 2.0 9.8 3.9 73.0 1.2 0.6 3.0 1.2 4.1 2.1 10.3 4.1 76.1, 1.2 0.6 3.1 1.2 3 4.9 2.4 12.2 4.9 88.9 1.5 0.7 3.7 1.5 6.5 3.3 16.3 6.5 108.0 2.0 1.0 5.0 2.0 4 6.5 3.3 16.3 6.5 114.3 2.0 1.0 5.0 2.0 133.0 8.0 4.0 20.0 8.0 2.4 1.2 6.1 2.4 8.0 4.1 20.0 8.0 139.7 2.4 1.3 6.1 2.4 5 8.2 4.1 20.5 8.2 141.3 2.5 1.3 6.3 2.5 9.5 23.8 9.5 159.0 2.9 1.4 7.2 2.9 9.5 4.8 23.8 9.5 165.1 2.9 1.4 7.2 2.9 6 9.9 5.0 24.8 9.9 168.3 3.0 1.5 7.6 3.0 13.1 6.6 32.8 13.1 216.3mn 4.0 2.0 10.0 4.0 8 13.1 6.6 32.8 13.1 219.1 4.0 2.0 10.0 4.0 10 16.5 8.3 41.3 16.5 273.0 5.0 2.5 12.6 5.0 12 19.9 9.9 49.7 19.9 323.4 6.1 3.0 15.1 6.1 1 Clot I- C to E Figure 201 Figure 210 -C to E-*1 çCIE Figure 219 Figure 260 Page 2 of 6 TFP181b Figures 201, 210, 219, and 260 For reducing tees and branches, use the value that is corrosponding to the branch size. Example: for 8 x 8 x 2 tee, the branch value 2 is 8.0 feet. - Friction resistance for all elbows and tees except Figures 510S and 519S. Figure 501S Friction Resistance 501S, 510S & 519S (Expressed as Equivalent Straight Pipe) Elbow Tee 900 45° Branch Run Size Inches Feet Feet Feet Feet mm Meters Meters Meters Meters 2 3.2 1.6 8.0 3.2 60.3 1.0 0.5 2.5 1.0 21/2 3.9 2.0 9.8 3.9 73.0 1.2 0.6 3.0 1.2 761mn 4.1 2.1 10.3 4.1 1.2 0.6 3.1 1.2 3 4.9 2.4 12.2 4.9 88.9 1.5 0.7 3.7 1.5 4 6.5 3.3 16.3 6.5 114.3 2.0 1.0 5.0 2.0 8.0 4.1 20.0 8.0 1397 ° °° 2.4 1 1.3 6.1 2.4 5 8.2 4.1 20.5 8.2 141.3 2.5 1.3 6.3 2.5 165.1- 9.5 4.8 23.8 9.5 2.9 1.4 7.2 2.9 9.9 5.0 24.8 9.9 168.3 3.0 1.5 7.6 3.0 E6 8 13.1 6.6 32.8 13.1 219.1 4.0 2.0 10.0 4.0 Page 3 of 6 TFP 1810 Figures 501,510, 519 and 51 ODE to C to E __-_CtoE-_j C tiE Figure 519 4ctor- Figure 51 ODE Figure 501 Figure 510 Figure 501 Figure 510 Figure 519 Figure 51 ODE 45° Elbow 90° Elbow Tee 90° Drain Elbow ?1 Appx. Wt. C to E Appx. Wt. C to E Appx. Wt. C to E A B Appx. Wt. Nominal Inches Lbs. Inches Lbs. Inches Lbs. Inches Inches Inches Lbs. Size mm Kg. mm Kg. mm Kg. mm mm mm Kg. 1 /4 1.75 0.9 2.75 1.0 2.75 1.4 44.5 0.4 1 69.9 0.5 1 69.9 0.6 - - - 1 /2 1.75 1.1 2.75 1.2 2.75 1.8 44.5 0.5 69.9 0.5 69.9 0.8 - - - - 2.00 1.8 3.25 2.0 3.25 2.7 2 50.8 0.8 82.6 0.9 82.6 1.2 - - - - 2/2 2.25 2.2 3.75 3.0 3.75 5.8 3.75 2.00 2.75 2.7 57.2 1.0 95.3 1.4 95.3 2.6 95.3 50.8 69.9 1.2 2.50 3.5 425 4.5 4.25 7.0 4.25 2.34 2.75 3.7 63.5 1.6 108.0 2.0 108.0 3.2 108.0 59.4 69.9 1.7 5.2 5.00 8.5 5.00 11.8 5.00 2.85 2.75 7.0 76.2 2.4 127.0 3.9 127.0 5.4 127.0 72.4 69.9 3.2 3.25 8.5 5.50 13.5 5.50 17.0 5.50 3.38 2.75 13.0 82.6 3.9 139.7 6.1 139.7 7.7 139.7 85.9 69.9 5.9 6 350 12.0 6.50 18.5 6.50 26.0 6.50 3.92 2.75 13.4 88.9 5.4 165.1 8.4 165.1 11.8 165.1 99.6 69.9 6.1 8 425 23.0 7.75 36.5 7.75 45.0 7.75 4.95 2.75 26.3 108.0 10.4 1969 16.6 196.9 20.4 196.9 125.7 69.9 11.9 Figures 501S, 510S and 519S Figure 510S° Figure 519S° Figure 501S Figure 510S Figure 519S 45° Elbow 90° Elbow Tee Appx Wt. C to E Appx. Wt. C to E Appx. Wt. Nominal Inches Lbs. Inches Lbs. Inches Lbs. Size min Kg. mm Kg. mm Kg. 2.00 1.8 2.75 1.5 2.75 2.1 2 50.8 0.8 69.9 0.7 69.9 1.0 2V2 2.25 2.2 3.00 2.2 3.00 3.0 57.2 1.0 76.2 1.0 76.2 1.4 76.1mn 2.25 2.2 3.00 2.3 3.00 3.1 57.2 1.0 76.2 1.0 76.2 1.4 2.50 3.5 3.38 3.0 3.38 4.1 63.5 1.6 85.9 1.3 85.9 1.9 3.00 5.2 4.00 5.6 4.00 7.7 76.2 2.4 101.6 2.6 101.6 3.5 139.7mm 3.25 7.7 4.88 8.6 4.88 12.0 82.6 3.5 124.0 3.9 124.0 5.4 50 3.25 8.5 4.88 8.8 4.88 12.0 82.6 3.9 124.0 3.9 124.0 5.4 165.1mm 3.50 12.0 5.50 11.00 5.50 15.0 88.9 5.4 139.7 5.0 139.7 6.8 6 3.50 12.0 5.50 11.2 5.50 15.2 88.9 5.4 139.7 5.1 139.7 6.9 8° 4.25 23.0 6.88 23.4 6.88 31.2 108.0 10.4 174.8 10.6 174.8 14.2 *Note: Figure 510S and 519S fittings are special snort radius fittings with smaller center to end dimensions than standard grooved fittings. Depending on the size and coupling used, there maybe interferences at the bolt pads Which requires repositioning of the coupling orientation. The use of flange adapters is not recommended with Figures 510S and 519S fittings. Contact Tyco Fire Products for details. Page 4 of 6 TFP181O Figures 250 and 350 Figures 250 and 350 Concentric Reducer - Groove x Groove Nominal E to E Appx. Wt. Nominal E to E Appx. Wt. Nominal E to E Appx. Wt. Size Inches Lbs. Size Inches Lbs. Size Inches Lbs. Inches mm Kg. Inches mm Kg. Inches mm Kg. *2 x 11/4 2.50 63.5 1.0 0.5 "139.7,,,, x 3.50 88.9 4.2 1.9 "6 x 4.00 101.6 5.8 2.6 *2 x 11/2 2.50 63.5 1.3 0.6 139.7, x 4 3.50 88.9 4.4 1 2.0 8 x 2 5.00 127.0 12.2 5.5 *21/ x 2 2.50 63.5 1.2 0.5 5 x 1½ 3.50 88.9 4.6 2.1 8 x 21/2 5.00 127.0 12.1 5.5 *761 x 1½ 2.50 63.5 1.5 0.7 5 x 2 3.50 88.9 4.6 2.1 8 x 3 5.00 127.0 12.0 5.5 *761 x 2 2.50 63.5 1.6 0.8 5 x 21/2 3.50 88.9 4.5 2.0 8 x 5.00 127.0 11.9 5.4 3 x 1¼ 2.50 63.5 1.3 0.6 5 x 3 3.50 88.9 4.4 2.0 8 x 5.00 127.0 11.3 5.1 3x1Y2 2.50 1.3 *5 x 3.50 4.5 x 8 6 5.00 10.8 63.5 0.6 88.9 2.0 127.0 4.9 3 x 2 2.50 63.5 1.3 0.6 *1651 x 4.00 101.6 5.5 2.5 10 X 6.00 152.4 21.9 10.0 "3x2½ 3.00 76.2 1.5 0.7 *1651x4 4.00 101.6 6.0 2.7 10x5 6.00 152.4 21.6 9.8 "3 X 76.1mm 3.00 76.2 2.0 0.9 *11***x17*** 4.00 101.6 5.6 2.5 lOx 6 6.00 152.4 21.1 9.6 4x1¼ 3.00 2.2 *6 x 2 4.00 6.0 10 x 8 6.00 19.5 76.2 1.0 101.6 2.7 152.4 8.9 4x1½ 3.00 76.2 2.3 1.0 6 x 2½ 4.00 101.6 6.0 2.7 12x4 7.00 1778 28.0 12.7 "4 x 2 3.00 76.2 2.3 1.0 *6 X 76.1mm 4.00 101.6 6.0 2.7 12 X 6 7.00 1778 30.0 13.6 "4x2½ 3.00 2.3 6 x 4.00 6.0 12 x 8 7.00 28.0 76.2 1.0 101.6 2.7 1778 12.7 "4 X 76.1mm 3.00 76.2 3.2 1.5 *6 x ___ 4.00 101.6 5.9 2.7 12 X 10 7.00 1778 33.0 15.0 3.00 2.6 1[ 4.00 6.3 x 76.2 1.2 "6 x 139.7mm 101.6 2.9 Note: Sizes marked with an asterisk () are only available in Figure 250 Cast. Sizes without an asterisk are only available in Figure 350 Fabricated. N Figure 250 Cast toE-1 Figure 350 Fabricated Sizes 3" to 6" to -M Figure 350 Fabricated Sizes 8" to 12" ADA CAP® Patented P1 e Nominal Dimensions Net O.D. Takeout Center to End Size Outlet Wt. A B C D Inches NPT Inches Inches Inches Inches Lbs. Inches Kg. mm mm mm mm 1/2 1.25 1.75 1.89 0.77 31.8 44.5 48.0 0.3 3/4 1.25 1.75 1.89 0.77 11/2 1.900 48.3 31.8 44.5 48.0 0.3 1 1.37 2.00 2.02 0.88 34.8 50.8 51.3 0.4 1/2 1.25 1.75 1.89 0.92 31.8 44.5 1 48.0 0.4 3/4 1.25 1.75 1.89 0.92 2 2.375 60.3 31.8 44.5 48.0 0.4 1 1.37 2.00 2.02 1.06 34.8 50.8 51.3 0.5 1/2 1.47 1.97 1.89 1.28 37.3 50.0 48.0 0.6 3/ 1.47 1.97 1.89 1.28 21/2 2.875 373 50.0 48.0 0.6 1.37 2.00 2.02 1.50 t 73.0 34.8 50.8 51.3 0.7 lSO-7 threaded outlets are available upon request. Figures 391, Figure 312 Figure 313 392 and 393 221/2° Elbow 111/40 Elbow Adapter Nipples E to E Appx. Wt. C to E Appx. Wt. C to E Appx. Wt. Nominal Inches Lbs. Inches Lbs. Inches Lbs. Size mm Kg. mm Kg. mm Kg. 4.00 0.8 1.75 0.4 1.38 0.4 11/4" 101.6 0.4 44.5 0.2 35.1 0.2 11/2" 4.00 0.9 1.75 0.5 1.38 0.5 101.6 0.4 44.5 0.2 35.1 1 0.2 4.00 1.2 1.88 0.6 1.38 0.6 2' 101.6 0.5 47.8 0.3 35.1 0.3 4.00 1.9 2.00 0.7 1.50 1.1 21/20 101.6 0.9 50.8 0.3 38.1 0.5 4.00 2.5 2.25 1.4 1.50 1.2 101.6 1.1 57.2 0.6 38.1 1 0.5 6.00 5.5 2.63 2.4 1.75 2.2 152.4 2.5 66.8 1.1 44.5 1.0 6.00 7.4 2.88 4.1 2.00 3.3 152.4 3.4 73.2 1.9 50.8 1.5 6.00 9.5 3.13 5.6 2.00 4.6 6" 152.4 4.3 79.5 2.5 50.8 2.1 8" 6.00 14.2 3.88 11.1 2.00 8.7 152.4 6.4 98.6 5.0 50.8 3.9 8.00 27.0 4.38 14.0 2.13 9.1 10 203.2 12.2 11.3 6.4 54.1 1 4.1 8.00 33.0 4.88 22.0 2.25 16.7 12" 203.2 15.0 124.0 1 10.0 57.2 7.6 G~to E Figure 313 to CtoE 11mil Eta E Figure 391 Eta E Figure 392 -H- - Figure 393 Figure 312 C to E Figure 327 Page 5 of 6 TFP1B1O Figures 391, 3929 3939 312 and 313 Figures 327 and 341 I II. EtoE Figure 341 Figure 327 Figure 341 Cross 150 lbs. Flange Adapter C to E Appx. Wt. E to E Appx. Wt. Nominal nches Lbs. Inches Lbs. Size mm kg. mm kg. 11/4 2.75 2.0 4.00 2.8 69.6 0.9 101.6 1.3 1h/2 2.75 2.2 4.00 3.2 69.9 2.0 101.6 1.5 3.25 2.7 4.0 5.2 2" 82.6 1.2 101.6 1 2.4 21/2 3.75 5.0 4.00 8.0 95.3 2.3 101.6 3.6 4.25 7.1 4.00 10.2 108.0 3.2 101.6 4.6 5.00 11.9 6.00 17.2 127.0 5.4 152.4 7.8 5.50 17.1 6.00 21.4 139.7 7.8 152.4 9.7 6.50 27.5 6.00 26.0 6' 165.1 12.5 152.4 11.8 8" 7.75 47.0 6.00 38.4 196.9 21.3 152.4 17.4 9.00 68.0 8.00 65.0 10" 228.6 1 30.8 1 203.2 29.5 12" 10.00 1 107.0 1 8.00 91.0 254.0 48.5 203.2 41.3 Page 6 of 6 TFP181) Figure 321 Figure 321 Reducing Tee Nominal C to E Appx. Wt. Nominal C to E Appx. Wt. Size Inches Lbs. Size Inches Lbs. Inches mm Kg. Inches mm Kg. 11/2 x 11/2 x 11/4 3.25 2.0 6x6x4 6.50 26.6 82.6 0.9 165.1 12.1 2 x 2 x 11/2 3.25 2.7 6x6x5 6.50 27.0 82.6 1.2 165.1 12.2 2Y2 x 21/2 3.75 4.2 8x8x2 7.75 36.2 95.3 1.9 196.9 16.4 21/2 x 21/2 x 11/2 3.75 4.2 8x8x3 7.75 36.5 95.3 1.9 196.9 16.6 21/2 x 21/2 x 2 8x8x4 7.75 36.6 95.3 2.0 196.9 16.6 3 x 3 x 11/2 4.25 5.3 8x8x5 7.75 36.8 108.0 2.4 196.9 16.7 3x3x2 4.25 5.5 8x8x6 7.75 37.0 108.0 2.5 196.9 16.8 3x3x21/2 4.25 5.8 10x 10x2 9.00 57.1 108.0 2.6 228.6 25.9 4X4X1V4 5.00 9.8 10x 10x3 9.00 57.4 127.0 4.4 228.6 26.0 4x4x11/2 5.00 9.9 10x 10x4 9.00 57.6 127.0 4.5 228.6 26.1 4x4x2 5.00 10.1 lOx lOx 5 9.00 57.8 127.0 4.6 228.6 26.2 4X4X2Y2 5.00 10.3 10x 10x6 9.00 58.0 127.0 4.7 228.6 26.3 4x4x3 5.00 10.5 10x10x8 58.4 9.00 127.0 4.8 228.6 26.5 5x5x2 5.50 14.5 12x12x3 10.00 80.2 139.7 6.6 254.0 36.4 5x5x21/2 5.50 14.8 12x12x4 10.00 80.5 139.7 6.7 254.0 36.5 5x5x3 5.50 15.2 12x12x5 10.00 80.7 139.7 6.9 1 254.0 36.6 5x5x4 5.50 15.8 12x12x6 10.00 80.9 139.7 7.2 254.0 36.7 6 x 6 x 2 6.50 26.5 12 x 12 x 8 10.00 91.4 165.1 11.9 254.0 41.5 6x6x21/2 6.50 26.5 12x12x10 10.00 91.8 165.1 12.0 254.0 41.6 6x6x3 6.50 26.5 165.1 12.0 General Notes: It is the Designer's responsibility to select products suitable for the intended service and to ensure ISO that pressure ratings and performance data is not exceeded. Always read and understand the installation instructions 9001 (lH-1000). Never remove any piping component or correct or modify any piping deficiencies without first depressurizing and draining the system. Material and gasket selection should be verified to be compatible for the specific application. Certified Company TYCO FIRE PRODUCTS, 451 North Cannon Avenue, Lansdale, Pennsylvania 19946 Printed U.S.A. C to E -i Figure 321 tqCo Fire & Building I)Products Technical Services: Tel: (800) 381-9312 / Fax: (800) 791-5500 Pipe Fittings NPT Threaded, Ductile Iron General Description The Tyco® Series 800 Threaded Pipe Fittings and California Tees & Elbows are manufactured from ductile iron. They are stronger and more corrosion resistant than cast iron fittings. The additional strength is provided by the ductile properties and by adding mag- nesium while the iron is being poured into the final cast shape. Although lighter than standard cast iron, the fit- tings have an added advantage of be- ing less susceptible to cracking due to their added strength. The Series 800, California, and Figure 719 Threaded Pipe Fittings are a re- designation for the Central Series 800, California, and Figure 719 Threaded Pipe Fittings. WARNINGS The Threaded Pipe Fittings described herein must be installed and main- tained in compliance with this docu- ment, as well as with the applicable standards of the National Fire Pro- tection Association, in addition to the standards of any other authorities hav- ing jurisdiction. Failure to do so may impair the performance of these devices. The owner is responsible for maintain- ing their fire protection system and de- vices in proper operating condition. The installing contractor or sprinkler manufacturer should be contacted with any questions. Technical Data Approvals: UL Listed and FM Approved Maximum Working Pressure: Series 800 and California Fittings 250 psi (17,2 bar) Figure 719 Plug: 250 psi (17,2 bar) Material: Series 800 and California Fittings: Ductile Iron Figure 719 Plug: Cast Iron Pipe Thread: NPT per ANSI B1.20.1 Installation Apply Teflont tape or high quality pipe joint compound on male pipe threads and tighten two to three turns beyond hand tight. NOTE Installers who have not used ductile iron threaded fittings should be in- structed that the fittings are stron- ger than the pipe and overtightening the fitting can create leaks and cause damage to pipe threads. In general, there is about one-half turn difference between cast iron and ductile iron fit- tings. Apply Teflon tape or high qual- ity pipe joint compound on the male pipe threads and tighten two to three turns beyond hand tight. If an auto- matic make-on machine is being used, please exercise caution in setting the machine to the proper parameters pri- or to tightening fittings onto the male pipe threads. -Limited Warranty Products manufactured by Tyco Fire & Building Products (TFBP) are war- ranted solely to the original Buyer for ten (10) years against defects in mate- rial and workmanship when paid for and properly installed and maintained under normal use and service. This warranty will expire ten (10) years from date of shipment by TFBP. No warran- ty is given for products or components manufactured by companies not af- filiated by ownership with TFBP or for products and components which have been subject to misuse, improper in- stallation, corrosion, or which have not been installed, maintained, modified or repaired in accordance with applicable Standards of the National Fire Protec- tion Association, and/or the standards of any other Authorities Having Juris- diction. Materials found by TFBP to be defective shall be either repaired or re- placed, at TFBP's sole option. TFBP neither assumes, nor authorizes any person to assume for it, any other ob- ligation in connection with the sale of products or parts of products. TFBP shall not be responsible for sprinkler system design errors or inaccurate or incomplete information supplied by Buyer or Buyer's representatives. In no event shall TFBP be liable, in contract, tort, strict liability or under any other legal theory, for incidental, indirect, special or consequential dam- ages, including but not limited to labor charges, regardless of whether TFBP was informed about the possibility of such damages, and in no event shall TFBP's liability exceed an amount equal to the sales price. The foregoing warranty is made in lieu of any and all other warranties, ex- press or imDlied, including warranties of merchantability and fitness for a particular purpose. This limited warranty sets forth the ex- clusive remedy for claims based on failure of or defect in products, materi- als or components, whether the claim is made in contract, tort, strict liability or any other legal theory. This warranty will apply to the full ex- tent permitted by law. The invalidity, in whole or part, of any portion of this warranty will not affect the remainder. Ordering Procedure When placing an order, indicate the full product name. Please specify the quantity, figure number, wall thickness, and size. t registered trademark of E. I. du Pont de Nemours and Company or its affiliates. Page 1 of 10 JANUARY, 2008 TFPI7I0 Page 2oflO TFP17I6 A\ /F1 _ _2 7. FIGURE 811 FIGURE 813 90° ELBOW 45° ELBOW Figure 811 B Approx. A B Inches Weight Part I nches Inches (mm) Lbs. Number (mm) (mm) (kg) 0.56 0.24 86206 0.88 0.38 (14,2) (0,11) (22,4) (9,7) 0.75 0.40 86205 1.00 0.44 (19,0) (0,18) (25,4) (11,2) 0.81 0.64 86200 1.13 0.81 (20,6) (0,29) (28,7) (20,6) 1.06 0.95 86201 1.31 0.63 (26,9) (0,43) (33,3) (16,0) 1.19 1.24 86202 1.44 0.69 (30,2) (0,56) (36,6) (17,5) 1.50 1.74 86203 1.68 0.94 (38,1) (0179) (42,7) (23,9) 1.56 3.28 86204 1.94 1.00 (39,6) (1,49) (49,3) (25,4) TABLE 1 NOMINAL DIMENSIONS FIGURES 811 & 813 Nominal Pipe Size Figure 813 ANSI A Approx. Inches Inches Weight Part DN (mm) Lbs. Number (kg) 1/2 1.13 0.22 86780 DN15 (28,7) (0,09) 3/4 1.31 0.33 86781 DN20 (33,3) (0,15) 1 1.50 0.48 86280 DN25 (38.1) (0,21) 1-1/4 1.75 0.73 86281 0N32 (44,5) (0133) 1-1/2 1.94 0.93 86282 DN40 (49,3) (0,42) 2 2.25 1.55 86283 DN50 (5711) (0170) 2-1/2 2.69 2.70 86782 DN65 (68,3) (1,22) Page 3 of 10 TFPI7IO B-1 FIGURE 812 90 REDUCING ELBOW Nominal Pipe Figure 812 Size ANSI A B C D Approx. Inches Inches Inches Inches Inches Weight Lbs . Part Number DN (mm) (mm) (mm) (mm) (kg) 3/4 x 1/2 1.19 1.19 0.63 0:63 0.33 86342 DN20x15 (30,2) (30,2) (16,0) (16,0) (0,15) 1 x 1/2 1.25 1.38 0.56 0.81 0.44 86210 DN25x15 (31,8) (35,1) (14,2) (20,6) (0,20) 1 x3/4 1.38 1.44 0.69 0.88 0.53 86211 DN25x20 (35,1) (36,6) (17,5) (22,4) (0,24) 1-1/4 x 1/2 1.31 1.50 0.63 0.94 0.64 86212 DN32 05 15 (33,3) (38,1) (16,0) (23,9) (0,29) 1-1/4 x 3/4 1.44 1.63 0.75 1.06 0.75 86213 DN32 x 20 (36,6) (41,4) (19,0) (26,9) (0,34) 1-1/4 x 1.56 1.68 0.88 1.00 0.77 86214 DN32 x 25 (39,6) (42,7) (22,4 (25,4) (0,35) 1-1/2x3/4 1.50 1.75 0.75 1.19 0.95 86221 DN40x20 (38,1) (44,4) (19,0) (30,2) (0,43) 1-1/2 x 1 1.63 1.81 0.88 1.13 0.99 86215 DN40 x 25 (41,4) (46,0) (22,4) (28,7) (0145) 1-112 x 1-1/4 1.81 1.88 1.13 1.19 1.14 86216 DN40 x 32 (46,0) (47,8) (28,7) (30,2) (0,52) 2 x 3/4 1.63 1.94 0.88 1.38 1.39 86217 DN50 x 20 (41,4) (49,3) (22,4) (35,1) (0,63) 20 1 1.75 2.06 2.00 1.31 1.58 86218 DN50 x 25 (44,4) (52,3) (50,8) (33,3) (0,72) 2 x 1-1/2 2.00 2.19 1.25 1.44 1.67 86220 DN50 x 40 (50,8) (55,6) (31,8) (36,6) (0,76) 2-1/2x2 2.38 2.63 1.25 1.88 3.01 86262 0N65 x 50 (60,5) (66,8) (31,8) (47,8) (1,36) _________ TABLE 2 NOMINAL DIMENSIONS FIGURE 812 Page 4 of 10 FIGURE 817 CROSS Nominal Pipe Size Figure 817 A B C 0 Approx. ANSI Inches Inches Inches Inches Inches Weight Part DN (mm) (mm) (mm) (mm) Lbs. Number (kg) 1 1.50 1.50 0.81 0.81 0.97 86284 DN25 (38,1) (38,1) (20,6) (20,6) (0,44) 1-1/4 1.75 1.75 1.06 1.06 1.59 DN32 (44,4) (44,4) (26,9) (27,0) (0,72) 86285 1-1/2 1.94 1.94 1.19 1.19 1.89 DN40 (49,3) (49,3) (30,2) (30,2) (0,86) 86286 2 2.25 2.25 1.50 1.50 2.93 DN50 (57,1) (57,1) (38,1) (38,1) (1,33) 86287 1-1/4 x 1-1/4 x x 1.69 1.56 1.00 0.88 1.25 86289 DN32 x 32 x 25 x 25 (42,9) (39,6) (25,4) (22,4) (0,56) 1-1/2 x 1-1/2 x x 1.81 1.63 1.06 1.94 1.48 DN40 x 40 x 25 x 25 (46,0) (41,4) (26,9) (49,3) (0,71) 86322 2 x 2 x 1 x 1 2.00 1.75 1.25 1.06 2.64 86291 DN50x50x25x25 (50,8) (44,4) (31,8) (26,9) (1,20) TABLE 3 NOMINAL DIMENSIONS FIGURE 817 TFP1716 TFPI7I0 Page soflO A7 rTh LE FIGURE 814 FIGURE 818 IRON TEE STRAIGHT COUPLING Figure 814 Figure 818 A B Approx. A B Inches Inches Weight Part Inches Inches (mm) (mm) Lbs. Number (mm) (mm) (kg) 1.13 0.56 0.33 86340 1.38 0.31 (28,7) (14,2) (0,15) (35,1) (7,9) 1.31 0.75 0.50 86341 1.63 0.56 (33,3) (19,0) (0,23) (41,4) (14,0) 1.50 0.81 0.85 86230 1.75 0.38 (38,1) (20,6) (0,38) (44,4) (9,7) 1.75 1.06 1.30 86231 2.00 0.56 (44,4) (26,9) (0,59) (50,8) (14,0) 1.94 1.19 1.63 86232 2.19 0.75 (49,3) (30,2) (0,74) (55,6) (19,0) 2.25 1.50 2.63 86233 2.63 1.13 (57,1) (38,1) (1,19) (66,8) (28,7) 2.69 1.56 4.55 86234 3.00 0.75 (68,3) (39,6) (2,06) (76,2) (19,0) TABLE 4 NOMINAL DIMENSIONS FIGURES 814 & 818 Nominal Pipe Size Approx. ANSI Inches Weight Part DN Lbs. Number (kg) 1/2 0.18 72779 DN15 (0,08) 3/4 0.26 72778 DN20 (0,11) 1 0.44 72755 DN25 (0,20) 1-1/4 0.54 72754 DN32 (0,24) 1-1/2 0.71 72753 DN40 (0,32) 2 1.15 72752 DNSO (0,52) 2-1/2 2.29 72758 DN65 (1,04) TFP171O Page 6 of iô FIGURE 815 REDUCING TEE Nominal Pipe Size Figure 815 A B C D E F Approx. ANSI Inches Inches Inches Inches Inches Inches Inches Weight Part DN (mm) (mm) (mm) (mm) (mm) (mm) Lbs. Number (kg) 3/4 x 3/4 x 1/2 1.19 1.19 1.25 0.63 0.63 0.69 0.46 DN20x20x15 (30,2) (30,2) (31,8) (16,0) (16,0) (17,5) (0,21) 86235 3/4x3/4x1 1.44 1.44 1.38 0.88 0.88 0.69 0.68 DN20x20x25 (36,6) (36.6) (35,1) (22,4) (22,4) (17,5) (0,31) 86755 1 x 1/2 x 1 1.50 1.38 1.50 0.81 0.81 0.81 0.70 DN25 x 15 x 25 (38,1) (35,1) (38,1) (20,6) (206) , (206) , (0 ,32) 86236 1 x3/4x112 1.25 1.19 1.38 0.56 0.63 0.81 0.63 DN25x20x15 (31,8) (30,2) (35,1) (14,2) (16,0) (20,6) (0,28) 86756 1 x 3/4 x 3/4 1.38 1.31 1.44 0.69 0.75 0.88 0.68 DN25x20x20 (35,1) (33,3) (36,6) (17,5) (19,0) (22,4) (0,31) 86757 1 x 3/4 x 1 1.50 1.44 1.50 0.81 0.88 0.81 0.77 86237 DN25 x 20 x 25 (38,1) (36,6) (38,1) (20,6) (22,4) (20,6) (0,35) 1 x 1 x 1/2 1.25 1.25 1.38 0.56 0.56 0.81 0.66 DN25x25x15 (31,8) (31,8) (35,1) (14,3) (14,3) (20,6) (0,30) 86238 1 x1 x3/4 1.38 1.38 1.44 0.69 0.69 0.88 0.73 DN25x25x20 (35,1) 1 (35,1) (36,6) (17.5) (17,5) (22,4) (0,33) 86239 1 x x 1-1/4 1.69 1.69 1.56 1.00 1.00 0.88 0.97 DN25x25x32 (42,9) (42,9) (39,6) (25,4) (25,4) (22,4) (0,44) 86240 1 x x 1-1/2 1.81 1.81 1.63 1.13 1.13 0.88 1.14 DN25 x 25 x 40 (46,0) (46,0) (41,4) (28.6) (28,6) (22,4) (0,52) 86241 1-1/4 x 1 x 1/2 1.94 1.25 1.56 0.63 0.56 1.00 0.81 DN32x25x15 (49,2) (31,8) (39,6) (15,9) (14,3) (25,4) (0.37) 86242 1-1/4 x x 3/4 1.44 1.38 1.62 0.75 0:69 1.06 0.90 DN32x25x20 (366) (35.1) (41,2) (19,0) (17,5) (27.0) (0,41) 86243 1-1/4 x 1 x 1.56 1.50 1.69 0.88 0.81 - 1.00 1.03 DN32 x 25 x 25 (39,6) (38,1) (42,9) (22,4) (20,6) (25,4) (0,47) 86244 1-1/4 x x 1-1/4 1.75 1.69 1.75 1.06 1.00 1.06 1.10 DN32 x 25 x 32 (44,4) (42,9) (44,4) (27.0) (25,4) (27,0) (0,50) 86245 1-1/4 x x 1-1/2 1.88 1.81 1.81 1.19 1.13 1.06 1.43 DN32 x 25 x 40 (47,6) (46,0) (46,0) (30,1) (28,6) (27,0) (0165) 86246 1-1/4 x 1-1/4 x 1/2 1.38 1.38 1.56 0.69 0.69 1.00 0.87 DN32x32x15 (35,1) (35.1) (39,6) (17.5) (17,5) (25,4) (0,39) 86247 1-1/4 x 1-1/4 x 3/4 1.44 1.44 1.63 0.75 0.75 1.06 0.96 DN32 x 32 x 20 (36.6) (36,6) (41,4) (19,0) (19,0) (27,0) (0,43) 86248 1-1/4x1-1/4x1 1.56 1.56 1.69 0.88 0.88 1.00 1.10 DN32 x 32 x 25 (39,6) (39,6) (42,9) (22,4) (22,4) (25,4) (0,50) 86249 1-1/4 x 1-1/4 x 1-1/2 1.88 1.88 1.81 1.81 1.81 1.06 1.50 DN32 x 32 x 40 (47,6) (47,6) (46,0) (46.0) (46,0) (27,0) (0,68) 86250 1-1/4 x 1-1/4 x 2 2.13 2.13 2.00 1.44 1.44 1.13 2.00 DN32x32x50 (54,1) (54,1) (50,8) (36.6) (36,6) (28,6) (0.91) 86251 1-1/2 x 1 x 1/2 1.44 1.31 1.69 0.69 0.63 1.13 0.97 DN40x25x15 (36.6) (33,3) (42,9) (17,5) (15,9) (28,6) (0,44) 86252 1-1/2 x 1 x 3/4 1.50 1.38 1.75 0.75 0.69 1.19 1.14 DN40 x 25 x 20 (38,1) (35,1) (44,4) (19,0) (17,5) (30,2) (0,52) 86253 1-1/2 x 1 x 1 1.63 1.50 1.81 0.88 0.81 1.13 1.14 DN40 x 25 x 25 (41,4) (38,1) (22,4) (20,6) (28,7) (0,52) 86254 1-1/2x 1 x 1-1/2 1.94 1.81 t(46,0) 4 1.19 1.13 1.19 1.52 DN4O x 25 x 40 (49,3) (46.0),2) (30.2) (28,6) (30,2) (0,69) 86255 TABLE 5(1 0F2) NOMINAL DIMENSIONS FIGURE 815 Page 7 of 10 TFPI7IO FIGURE 815 REDUCING TEE Nominal Pipe Size Figure 815 A B C D E F Approx. ANSI Inches Weight Part Inches Inches Inches Inches Inches Inches DN (mm) (mm) (mm) (mm) (mm) (mm) Lbs. Number (kg) 1-1/2 x 1-1/4 x 1/2 1.44 1.31 1.69 0.69 0.63 1.13 1.03 86257 DN40 x 32x 15 (36.6) 1 (33,3) (42,9) (17,5) (16,0) (28,7) (0,47) 1-1/2 x 1-1/4 x 3/4 1.50 1.44 1.75 0.75 0.75 1.19 1.10 86258 DN40x32x20 (38,1) (36.6) (44,5) (19.0) (19,0) (30,1) (0,50) 1-1/2 x 1-1/4 x 1 1.63 1.56 1.81 0.88 0.88 1.13 1.31 86259 DN40 x 32 x 25 (41,4) (39,7) (46,0) (22,4) (22,4) (28,7) (0,59) 1-1/2 x 1-1/4 x 2 2.19 2.13 2.00 1.44 1.44 1.25 1.94 86260 DN40 x 32 x 50 (55,6) (54,1) (50,8) (36,6) (36,6) (57,1) (0,88) 1-1/2 x 1-1/2 x 1/2 1.44 1.44 1.69 0.69 0.69 1.13 1.14 DN40 x 40 x 15 (36.6) (36,6) (42,9) (17,5) (17,5) (28,7) (0,52) 86261 1-1/2 x 1-1/2 x 3/4 1.50 1.50 1.75 0.75 0.75 1.19 1.23 86262 DN40x40x20 (38,1) (38,1) (44,4) (19,0) (19,0) (30,1) (0,56) 1-1/2x1-1/2x1 1.63 1.63 1.81 0.88 0.88 1.13 1.38 DN40x40x25 (41,2) (41,2) (46.0) (22,4) (22,4) (28,7) (0,62) 86263 1-1/2x1-1/2x1-1/4 1.81 1.81 1.88 1.06 1.06 1.19 1.50 86264 DN40 x 40 x 32 (46,0) (46.0) (47.6) (27,0) (27,0) (30,1) (0,68) 1-1/2x1-1/2x2 2.19 2.19 2.00 1.44 1.44 1.25 2.00 DN40 x 40 x 50 (55.5) (55,5) (50,8) (36,6) (36,6) (31,7) (0,91) 86265 2 x 1 x2 2.25 2.00 2.25 1.50 1.31 1.50 2.18 86266 DN50x25x50 (57,2) (50,8) (57,2) (38,1) (33,3) (38,1) (0,99) 2 x 1-1/4 x 2 2.25 2.13 2.25 1.50 1.44 1.50 2.31 86267 DN50x32x50 (57,2) (54,1) (57,2) (38,1) (36,6) (38,1) (1,05) 2 x 1-1/2 x 1/2 1.50 1.44 1.88 0.75 0.69 1.31 1.50 86268 DN50 X 40 X 15 (38,1) (36,6) (47,8) (19;0) (17,5) (33,3) (0,68) 2x1-1/2x3/4 1.63 1.50 1.94 0.88 0.75 1.38 1.61 DNSO x 40 x 20 (41,4) (38,1) (49,3) (22,4) (19.0) (35,0) (0173) 86269 2 x 1-1/2 x 1 1.75 1.63 2.00 1.00 0.88 1.31 1.65 DN50x40x25 (44,5) (41,4) (50,8) (25,4) (22,4) (33.3) (0,75) 86270 2 x 1-1/2 x 1-1/2 2.06 1.94 2.19 1.31 1.19 1.44 2.03 DN50 x 40 x 40 - (52,4) (49,2) (55,5) (33,3) (30,2) (36,6) (0,92) 86272 2x1-1/2x2 2.25 2.19 2.50 1.50 1.44 1.50 2.37 DN50x40x50 (57,1) (55,5) (63,5) (38,1) 1 (36,6) (38,1) (1,07) 86273 2x2x1/2 1.50 1.50 1.88 0.75 0.75 1.31 1.50 DN50 x 50 xiS (38,1) (38,1) (47,8) (19,0) (19,0) (33,3) (0168) 86222 2x2x3/4 1.63 1.63 1.94 0.88 0.88 1.38 1.67 DN50 x 50 x 20 (41,4) (41,4) (49,3) (22,4) (22,4) (35,0) (0,76) 86223 2 x 2 x 1 1.75 1.75 2.00 1.00 1.00 1.31 1.91 86224 DN50 x 50 x 25 (44,5) (44,5) (50.8) (25,4) (25,4) (33,3) (0,86) 2x2x1-114 1.88 1.88 2.13 1.13 1.13 1.44 2.05 86225 DNSO x 50 x 32 (47,8) (478) (54,1) (28,7) (28.7) (36,6) (0,93) 2 x 2 x 1-1/2 2.00 2.00 2.19 1.25 1.25 1.50 2.11 86226 DN50x50x40 (50,8) (50,8) (55,6) (31,8) (31,8) (38,1) (0,96) 2 x 2 x 2-1/2 2.63 2.63 2.38 1.75 1.88 1.44 3.67 86227 DN50x50x65 (66,8) (66,8) (60,5) (445) (47.8) (36.6) (1,66) 2-1/2 x 2 x 3/4 1.75 1.63 2.31 0.63 0.88 1.75 2.22 DN65 x 50 x 20 (44,5) (41,4) (58,7) (15,9) (22,4) (44,5) 86274 TABLE 5(2 0F2) NOMINAL DIMENSIONS FIGURE 815 Page 8 of 10 TFP171d F-i FIGURE 820 FIGURE 830 FIGURE 719 CAP BRASS SEAT UNION PLUG Nominal Pipe Size Figure 820 Figure 830 Figure 719 ANSI A Approx. A B Approx. A Approx. Inches Inches Weight Part Inches Inches Weight Part Inches Weight Part DN (mm) Lbs. Number (mm) (mm) Lbs. Number (mm) Lbs. Number (kg) (kg) (kg) 1/2 088 0.15 72776 1.88 0.81 0.47 86207 0.94 0.10 86292 DN15 (22,4) (0,06) (47,8) (20,6) (0,21) (23,9) (0,04) 3/4 1.00 0.22 72777 2.00 0.94 0.66 86275 1.13 0.18 86293 DN20 (25,4) (0,10) (50,8) (23,9) (0,30) (28,7) (0,08) 1 1.18 0.33 72824 2.19 0.81 1.08 86276 1.25 0.28 86294 DN25 (30,0) (0,15) (55,6) (20,6) (0,49) (31,7) (0,13) 1-1/4 1.31 0.54 72756 2.50 1.06 1.54 86277 1.38 0.50 86295 DN32 (33,3) (0,24) (63,5) (26,9) (0,70) (35,1) (0,23) 1-1/2 1.38 0.68 72822 2.63 1.19 2.03 86278 1.44 0.70 86296 DN40 (35,1) (0131) (66,8) (30,2) (0,92) (36,6) (0,32) 2 1.50 th96 72823 3.13 1.63 3.15 86279 1.50 0.90 DN50 (38,1) (0 (79,5) (41,4) 86297,43) (1,43) (38,1) (0,41) 2-1/2 1.75 1.80 72825 - - - - - - - DN65 (44,5) (0182) TABLE 6 NOMINAL DIMENSIONS FIGURES 820,830 & 719 TFPI7IO Page 9 of 10 - A - '.1 ____ AH +JTIjJ FIGURE 825 FIGURE 827 FIGURE 816 EXTENSION PIECE HEX BUSHING REDUCING COUPLING Nominal Pipe Figure 825 Figure 827 Figure 816 Size Extension Piece Hex Bushing Reducing Coupling A Approx. A Approx. A B Approx. ANSI Inches Inches Weight Part Inches Weight Part Inches Inches Weight Part DN (mm) Lbs. Number (mm) Lbs. Number (mm) (mm) Lbs. Number (kg) (kg) (kg) 1/2x1/2 1.50 0.20 72751 - - - - - - - DN15 x 15 (38,1) (0,09) 1/2x1/2 2.00 0.27 72980 - - - - - - - DN15 x 15 (50,8) (0,12) 3/4x3/4 1.50 0.22 DN20 x 20 (38,1) (0110) 3/4 x 3/4 2.00 0.31 73982 - - - - - - - DN20 x 20 (50,8) (0,14) 3/4 x 1/2 1.75 0.69 0.38 86772 DN20 x 15 - - - - - (43,2) (17,5) (0,17) 1 x 1/2 1.06 0.22 72726 1.69 0.50 0.38 86228 DN25 x 15 - - - (26,9) (0,10) (42,9) (12,7) (0,17) 1 x3/4 1.06 0.18 72762 1.75 0.50 0.53 86229 DN25 x 20 - - - (26,9) (0,08) (43,2) (12,7) (0,24) 1-1/4x1 1.19 0.31 72763 - - - - DN32 x 25 - - - (30,2) (0,14) 1-1/2x1 1.25 0.53 72757 - - - - DN40x25 - - (31,7) (0,24) 1-1/2x1-1/4 1.25 0.35 72764 - - - - DN40 x 32 - - (31,7) (0,10) 2x1 1.38 0.75 72759 - - - - DN50 x 25 - - (35,1) (0134) 2x1-1/4 1.38 0.69 DN50 x 32 - - - (35,1) (0131) 2x1-1/2 1.38 0.62 72775 - - - - DN50x40 - - - (35,1) (0,28) TABLE 7 NOMINAL DIMENSIONS FIGURE 825,827 & 816 Page 10 of 10 TFP171t Fr B---D-1] Fr -13-~7D-j IF L C I -V~ CALIFORNIA TEES TABLE 8 NOMINAL DIMENSIONS CALIFORNIA TEES California Tees A B C D Approx. Inches Inches Inches Inches Weight (mm) (mm) (mm) (mm) Lbs. (kg) 1.50 0.88 3.00 0.75 0.95 (38,1) (22,4) (76,2) (19,1) (0,43) 1.50 0.75 3.00 0.75 0.95 (38,1) (19,1) (76,2) (19,1) Nominal Pipe Size ANSI Inches Part DN Number I x-I/2 x 1 DN25x15x25 42000 I x 1 xl 42001 DN25 x 25 x 25 (0,43) STREET ELBOWS Nominal Pipe Street Elbows Size ANSI A B C Approx. Inches Inches Inches Inches Weight Part DN (mm) (mm) (mm) Lbs. Number (kg) 1 x 1/2 1.50 0.75 3.00 0.70 42003 DN25 x 15 (38,1) (19,1) (76,2) (0,32) 1 xl 1.50 0.75 3.00 0.90 42002 DN25x25 (38,1) (19,1) (76,2) (0,40) TABLE 9 NOMINAL DIMENSIONS STREET ELBOWS © 2008 TYCO FIRE & BUILDING PRODUCTS, 451 North Cannon Avenue, Lansdale Pennsylvania 19446 Fig. 25 - Surge Restrainer Size Range - One size fits 3/4 thru 2 pipe. Material - Pre-Galvanized Steel Function - Designed to be used in conjunction with TOLCO® Band Hangers to restrict the upward movement of piping as it occurs during sprinkler head activation or earthquake type activity. The surge restrainer is easily and efficient- ly installed by snapping into a locking position on the band hanger. This product is intended to satisfy the requirements as indicated in the National Fire Protection Association (NFPA 13, 1999 Edition), 6-2.3.3, 6-2.3.4 and A-61-2.3.3 Can be used to restrain either steel pipe or CPVC plastic Pipe. Approvals - Underwriters' Laboratories Listed qnly when used with TOLCO band hangers Fig. 2, 2NFPA and 200, in the USA (UL) and Canada (cUL). Finish - Pre-Galvanized Order By - Figure number and TOLCO band hanger, size from 3/4 thru 2. Patent #5,344,108 c®US LISTED / / : 41 I' .1 OFFICE/MANUFACTURING FACILITY • 1375 SAMPSON AVE. • CORONA, CA 92879 • PH: 951.737.5599 • FAX: 951.737.0330 CUSTOMER SERVICE • 800.786.5266 www.tolco.com M ai Fig. 200 - "Trimline" Adjustable Band Hanger Fig. 200R (Import) - "Trimline" Adjustable Band Hanger w/Retainer Ring C@ US USTED Size Range - 1/2" thru 8' pipe Material - Carbon Steel, Mil. Galvanized to G90 specifications Function - For fire sprinkler and other general piping purposes. Knurled swivel nut design permits hanger adjustment after installation. Features - (1/2" thru 2) Flared edges ease installation for all pipe types and protect CPVC plastic pipe from abrasion. Captured design keeps adjusting nut from separating with hanger. Hanger is eas- ily installed around pipe. (21/2" thru 8") Spring tension on nut holds it securely in hanger before installation. Adjusting nut is easily removed. Approvals - Underwriters' Laboratories listed (1/2" thru 8") in the USA (UL) and Canada (cUL) for steel and CPVC plastic pipe and Factory Mutual Engineering Approved (3/4" thru 8"). Conforms to Federal Specifications WW-H-171 E, Type 10 and Manufacturers Standardization Society SP-69, Type 10. Maximum Temperature - 650°F Finish - Mil. Galvanized. Stainless Steel materials will be supplied with (2) hex nuts in place of a knurl nub. Order By - Figure number and pipe size Note - Figure 200R (import) with retainer ring and non-captured knurl nut. Dimensions • Weights Pipe Rod Size Max. Rec. Approx. Size Inch Metric A B Load Lbs. WtJ100 1/2 3/8 8mm or 10mm 31/8 25/8 400 11 3/4 3/8 8mm or 10mm 31A 21/2 400 11 1 3/8 8mm or 10mm 33/8 25/a 400 12 11/4 3/8 8mm or 10mm 33/4 27/8 400 13 1½ 3/8 8mm or 10mm 3 /8 27/8 400 14 2 3/8 8mm or 10mm 41/2 3 400 15 21/2 3/8 10mm 55/s 41/8 600 27 3 3/8 10mm 5/8 4 600 29 31/2 3/8 10mm 7% 51/4 600 34 4 3/8 10mm 73/8 5 1000 35 5 1/2 12mm 91/8 61/4 1250 66 6 1/2 12mm 101/8 63/4 1250 73 8 1/2 12mm 131/8 83/4 1250 136 OFFICE/MANUFACTURING FACILITY • 1375 SAMPSON AVE. • CORONA, CA 92879 • PH: 951.737.5599 • FAX: 951.737.0330 CUSTOMER SERVICE • 800.786.5266 www.tolco.com Size Range - Secures 3/8 thru 7/8 rod in 1 "increments Material - Carbon Steel Maximum Temperature - 750°F Finish - Plain Note - Available in Electro-Galvanized and HDG finish or Stainless Steel materials. Order By - Figure number, rod diameter, rod length and finish Dimensions Rod Max. Rec. Load Lbs. Size For Service Temp 650°F 3/8 730 1/2 1350 5/8 2160 3/4 3230 7/8 4480 9&- Rod Stiffener Size Range - Sect thru 7/8 hanger rod Material - Carbon Steel Function - Secures channel to hang?dJorvertical seismic bracing. Approvals - Included in our Seismic Restraii aloci approved Component of State of California OSHPD Approved Seismic Restraints System information relating to OSHPD projects, please refer to the TOLCO Seismic Restraint Systems Guidelines Finish - Electro Galvanized Note - Available in HDG finish or Stainless Steel materials. Order By - Figure number Fig. 99 - All Thread Rod Cut to Length Fig. 100 - All Thread Rod Full Lengths Size Range - Secures 3/8 thru 11/2" rod in 10' lengths Material - Carbon Steel Maximum Temperature - 750°F Finish - Plain Note - Available in Electro-Galvanized and HDG finish or Stainless Steel materials. Order By - Figure number, rod diameter and finish Dimensions • Weights Max Rec. Load Lbs. Rod For Service Temps Approx. Size 650°F Wt./100 1/4 240 12 3/8 730 29 1/2 1350 53 5/8 2160 84 3/4 3230 123 7/8 4480 169 1 5900 222 11/4 9500 360 11/2 13800 510 OFFICE/MANUFACTURING FACIUTY • 1375 SAMPSON AVE. • CORONA, CA 92879 • PH: 951.737.5599 • FAX: 951.737.0330 I CUSTOMER SERVICE • 800.786.5266 www.toko.com 114" 8002957 GST 100 1/4 x1" 25 125 1/4" 8003957 GST 200 1/4 x 2 1760 (Fir) 25 125 1/4" 8004957 GST 30d 1/4 x 3" 2060 (Fir) 25 125 318" 8006957 - GST 75 1/4 x 3/4" - 044 )3t4 Ply) 25 125 3/8" 8007957 GST 10 1/4 x 1" 300 25 125 3/8" 8008957 - GST 20 114 x 2"' 1760 (Fir) 850 1475 25 125 .110 38" oUb02b 8009925 (n0l 4U- GST 25-380 /4 XL 3/8 x 2-1'2 1/00 /00) 213 1Fir) iOU 1500 .10 25 I40 125 318" 8010957 GST 30 1/4 x 3" 2060 (Fir) 1500 1475 25 125 1114 Black 3/8" 8 69925 GST 30-SS 1/4 x 3 2060 (Fir) - 25 125 Nut Driver Part# 8113910 3/8" 801925 GST 0 1/4 x4" 2180 (Fir) 25 125 3/8" 8012925 GST 60 1/4 x 6 2230 (Fir) 25 125 — 1/2 8013925 GST2 1/4x2" 1760 (Fir) 25 - 125 112" 8014925 GST 2,5-380 3/8 x 2-V2 2113 (Fir) 25 125 1/2" 8015925 3" 75 (Fir) 25 125 112 8016025 1 /4 80 (Fir) 25 125 1/2" 8017925 GST6 1/4 x 6" 230 (Fir) 25 125 #14 SW Red Nut Driver Part # 8114910 Product Features Eliminates distortion of threaded rod. Saves time from traditional methods. "Accommodates up to 3%" x 12 pitch roof. "Reduces installation cost. "Allows 17° deflection from vertical. Made in the U.S.A. Milli IF 3 8139957 SF1GST20 114x2" 1257 )Fir) 1050 1475 25 125 125 3/8" 8141957 SH-GST 30 1/4 x 3" 1720 (Fir) 1500 1475 25 125 #14 Black Nut Driver SPECIAL NUT DRIVER SYSTEM: The nut drivers were designed with a unique spin-off feature which provides a fast and safe installation each time. When the face of the driver comes into Part 11 8113910 contact with the material you are installing into, conrinue drilling until nut driver spins free. Installation is then complete. Warranty requires the use of the appropriate nut driver for installations. ais For the most information, ____________ MADE IN US.A IN Floor Joist No less than 2 nominal width (1-1i2" up to 3-1/2 pipe: not less than 3" (2-912") nominal width 4'& 5" pipe 4 Minimum 2-117 torn bottom for branch linen. Minimum 3" from bottom for main lines. Exception: This requirement shall not apply 1s2" or thicker nailing stops renting on top of steel beams. Product Features "No pre-drilling required. Quick to install using the Sammy Nut Driver with an 18V cordless drill/driver, Saves time from traditional methods. Reduces installation cost. Made in the U.S.A. 9'" - 1/4 8018957 SWG 100 14 xl 622 (Ftr) 25 125 1/4" nra 8019957 ertnnac SWG 200 mrer In 1/4 x2" iI I 1725 (Fir) F19 25 125 - j r 3/8" 8021957 SWG 20 1/4 x 2' 1725 (Fir) .3Q 1050 25 125 3187 8073925 - SWG 20-SS 14 x 2 1725 (Fir) 850 25 199 #14 SW Red /. 3/8" 8022925 SWG 25-380 3/8 x 2.1/2' 2249 (Fir) 1500 25 Nut Driver 38 8023925 SWG 30 V4 x 3 1884 1Fir) 25 125 Part!! 8114910 Insert the appropriate flut druer into a 3/8" or 1/2' portable drill. Insert the SAMMYS into the #14 (black) nut driver (p/n 8113910). Drill should be in a vertical position. Push the face of the nut drivor tight to the member. When the nut dii ver spins freely on the SAMMYS, stop drill and remove. The SAMMYS is now ready o receive 1/4', 3/8", 1/2'ormetric- all thread rod, bolt stock. (Tf.e 1/2' requires the !!14S W red nut driver) Note: When installing DSTR, fllow the above instructions, then add retainer nut and torqLe to 20 foot lbs. for maximum pullout in purlin steel. WROIF-41, - Insert the appropriate nut driver into a 318"or 1/2"portable drill. Insert the SAMMYS into the #I4SW(red) nut driver (p/n 8114910). With drill unit in a horizontal position and at a right angle to the structural member, begin installation. When the nut driver spins free on the SAMMYS, stop the drill and remove. The unit is now ready to receive 1/4', 3/8' or metric all thread rod or bolt stock. Note: When installing SWDR, follow the above instructions, then add retainer nut and torque to 20 foot lbs. for maximum pullout in purlin steel. SPECIAL NUT DRIVER SYSTEM: The nut drivers were designed with a unique spin-off feature which provides a fast and safe installation each time. When the face of the driver comes into contact with the material you are inchalling into continue drilling until nut driver spins free. Installation is then complete. Warranty requires the use of the appropriate nut driver for installations. APPROVED ®TOLCO Fig. 1001 - Sway Brace Attachment Size Range: Pipe size to be braced: 21/2' (65mm) thru 8' (200mm) IPS. * Pipe size used for bracing: 1(25mm) and 11/4" (32mm) Schedule 40 lPS. Material: Steel Function: For bracing pipe against sway and seismic disturbance. The pipe attachment component of a sway brace system: Fig. 1001 is used in conjunction with a Fig. 900 Series fitting and joined together with bracing pipe per NFPA 13, forming a complete sway brace assembly. Features: Can be used to brace schedules 7 through 40 lPS. Field adjustable, making critical pre-engineering of bracing pipe length unnecessary. Unique design requires no threading of bracing pipe. Can be used as a component of a four-way riser brace. Comes assembled and ready for installation. Fig. 1001 has built-in visual verification of correct installation. See installation note below. Installation Note: Position Fig. 1001 over the pipe to be braced and tighten two hex head cone point set bolts until heads bottom out. A minimum of 1 (25mm) pipe extension is recommended. Brace pipe can be installed on top or bottom of pipe to be braced. Approvals: Approved by Factory Mutual Engineering (FM). For UL Listed information refer to page 64. Finish: Plain. Contact Cooper B-Line for alternative finishes and materials. Order By: Order by figure number, pipe size to be braced, followed by pipe size used for bracing (1" (25mm) or 11/4" (32mm)) , and finish. Important Note: Fig. 1001 is precision manufactured to perform its function as a critical component of a complete bracing assembly. To ensure performance, the FM Approval requires that Fig. 1001 must be used only with other Cooper B-LineiTOLCO bracing products. Designed to meet or exceed requirements of FM DS 2-8. ** See load ratings in FM Approved Design Load chart. * The loads listed are axial loads on the brace. The horizontal load capacity, H, of the brace is: H = F x sin ?, where? is the installation angle measured from the vertical. FM Approved design loads are based on ASD design method. FM Approved Design Loads * 21/2" (65mm) pipe size - 1600 lbs. (7.11kN) 3" (75mm) to 4" (100mm) pipe size - 1700 lbs. (7.56kN) 5" (125mm) to 8" (200mm) pipe size - 1033 lbs. (4.59kN) All dimensions in charts and on drawings are in inches. Dimensions shown in parentheses are in millimeters unless otherwise specified. PP_ 00 COOPER B-Line ®TOLCO APP ROVO It' Set Bolt Included Mounting Hardware Is Not Included Pat. #6,273,372, Pat. #6,517,030, Pat. #6,953,174, Pat. #6,708,930, Pat. #7,191,987, Pat. #7,441,730, Pat. #7,669,806 Designed to meet or exceed requirements of FM DS 2-8. Fig. 980 Fig. 4L Longitudinal Brace Fig. 980 - Universal Swivel Sway Brace Attachment - /8" to 3/4" Size Range: One size fits bracing pipe 1(25mm) thru. 2" (50mm), Cooper B-Line 12 gauge (2.6mm) channel, and all structural steel up to 1/4" (31 .7mm) thick. Material: Steel Function: Multi-functional attachment to structure or braced pipe fitting. Features: This product's design incorporates a concentric attachment opening which is critical to the performance of structural seismic connections. NFPA 13 indicates clearly that fastener table load values are based only on concentric loading. Mounts to any surface angle. Break off bolt head assures verification of proper installation. Installation: Fig.980 is the structural or transitional attachment component of a longitudinal or lateral sway brace assembly. It is intended to be combined with the bracing pipe and Cooper B-Line/TOLCO 'braced pipe' attachment, Fig. 1000, 1001, 4L, or other TOLCO approved attachment to pipe to form a complete bracing assembly. NFPA 13 guidelines should be followed. To Install: Place the Fig. 980 onto the bracing pipe. Tighten the set bolt until the head breaks off. Attachment can pivot for adjustment to proper brace angle Approvals: —Approved by Factory Mutual Engineering (FM). For UL Listed information refer to page 60. Note: Fig. 980 Swivel Attachment and Fig. 1000, 1001, 4L or other TOLCO approved attachment to pipe that make up a sway brace system of UL Listed attachments and bracing materials which satisfies the requirements of Underwriters Laboratories and the National Fire Protection Association (NFPA) Finish: Plain. Contact Cooper B-Line for alternative finishes and materials. Order By: Figure number and finish. * Standard size. Mounting attachment hole size. Installed with 1" or 11/4" Schedule 40 brace pipe. FM Approved design loads are based on ASD design method. Cooper B-Line, Inc.'s ('Cooper B-Line") seismic bracing components are designed to be compatible only with other Cooper B-Line bracing components, resulting in a listed seismic bracing assembly. Cooper-B-Line's warranty for seismic bracing components will be the warranty provided in Cooper B-Line's standard terms and conditions of sale made available by Cooper B-Line, except that, in addition to the other exclusions from Cooper B-Line's warranty, Cooper B-line makes no warranty relating to Cooper B-Line's seismic bracing components that are combined with products not provided by Cooper B-Line. All dimensions in charts and on drawings are in inches. Dimensions shown in parentheses are in millimeters unless otherwise specified. COOPER B-Line 4-Way Riser Brace (plan view) Set Bolt & Hardware Included Fig. 41 - Longitudinal "In-Line" Sway Brace Attachment '®tOLCO Size Range: 21/2° (65mm) through 8" (200mm) IPS. Material: Steel APPROVED Function: For bracing pipe against sway and seismic disturbance. Approvals: Approved by Factory Mutual Engineering (FM), 21/2° (65mm) through 8(200mm) pipe. For UL Listed information refer to page 46. Installation Instructions: Fig. 4L is the "braced pipe' attachment component of a longitudinal sway brace assembly. It is intended to be combined with the "bracing pipe" and Cooper B-LinefrOLCO structural attachment component to form a complete bracing assembly. NFPA 13 and/or FM guidelines should be followed. To Install: Place the Fig. 4L over the pipe to be braced and tighten bolts. Then engage "bracing pipe" into jaw opening and tighten set bolt until head snaps off. Jaw attachment can pivot for adjustment to proper brace angle. Finish: Plain. Contact Cooper B-Line for alternative finishes and materials. Order By: Figure number, pipe size and finish. Designed to meet or exceed requirements of FM DS 2-8. Longitudinal Brace Part Pipe Size A I C D Bolt Size 30'-440 *Max. Design 450-590 Load (FM) 60*-74* 750-901 Approx. Wt/100 3" (80) 7" (177.8) 2/4" (69.8) 31/16" (77.8) 112"13 1030(4.58) 1180(524) 1420(6.31) 1590(7.07) 268 (1215) 4 (100) 81/2" (215.9) 3 /8"(85.7) 311/16' (937) l/2"..13 530(2.36) 730(3.25) 890(3.96) 990(4.40) 348 (157.8) [4L-5 5 (125) 93/4" (2476) 3 /8" (98.4) 43/ (111.1) 1/2"l3 530(2.36) 730(3.25) 890(3.96) 990(4.40) 380 (172.3) 6 (150) 11/2' (292.1) 5" (127.0) 51/8" (130.2) 1/2"..13 530(2.36) 730(3.25) 890(3.96) 990(4.40) 640 (290.3) 8" (00) 13/4 (3365) 5 /8" (142.8) 5/" (142.9) 1/2"..13 1 490(218) 1 680(3.02) 1 830(369) 1 930(4.13) 1728 (330.2) FM Approved when used with 1, 11/4", 1½' or 2' Sch. 40 brace pipe. FM Approved design loads are based on ASD design method. Cooper B-Line, Inc.'s ('Cooper B-Line") seismic bracing components are designed to be compatible only with other Cooper B-Line bracing components, resulting in a listed seismic bracing assembly. Cooper-B-Line's warranty for seismic bracing components will be the warranty provided in Cooper B-Line's standard terms and conditions of sale made available by Cooper B-Line, except that, in addition to the other exclusions from Cooper B-Line's warranty, Cooper B-line makes no warranty relating to Cooper B-Line's seismic bracing components that are combined with products not provided by Cooper B-Line. All dimensions in charts and on drawings are in inches. Dimensions shown in parentheses are in millimeters unless otherwise specified. COOPER B-Line SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.7 352.7 93.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 352.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 252.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 23.4 - - - 2 30.0 - - - - 23.0 3 33.5 - - - - 21.5 - - - 4 33.5 - - - - 21.5 - - - 5 29.0 - - - - 23.4 - - - 6 30.0 - - - - 23.0 - - - 7 33.5 - - - - 21.5 8 33.5 - - - - 21.5 9 33.5 - - - - 21.5 10 33.5 - - - - 21.5 - - - 11 30.0 - - - - 22.5 - - - 12 33.5 - - - - 21.9 - - - 13 33.5 - - - - 22.1 14 33.5 - - - - 23.8 - - - 15 33.5 - - - - 24.6 16 33.5 - - - - 34.3 - - - 17 33.5 - - - - 34.6 - - - 18 33.5 - - - - 34.9 - - - 19 33.5 - - - - 35T2 - - - 20 33.5 - - - - 35.5 21 33.5 - - - - 37.2 22 33.5 - - - - 47.7 - - - 23 30.0 - - - - 49.7 - - - 24 29.0 - - - - 22.4 - - - 25 30.0 - - - - 22.0 - - - 26 29.0 - - - - 22.4 - - - 27 30.0 - - - - 22.0 - - - 28 29.0 - - - - 22.4 - - - 29 30.0 - - - - 22.0 - - - 30 32.0 - - - - 21.1 - - - 31 32.0 - - - - 21.1 - - - 32 32.0 - - - - 21.1 - - - 33 30.0 - - - - 22.5 - - - 34 32.0 - - - - 17.6 - - - 35 32.0 - - - - 8.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GBAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 32.0 K= 5.60 7.3 15.2 37 32.0 K= 5.60 7.2 15.0 38 32.0 K= 5.60 7.0 14.8 39 32.0 K= 5.60 7.2 15.0 40 32.0 K= 5.60 8.0 15.8 41 32.0 - - - - 16.1 - - - 42 32.0 - - - - 47.5 - - - 43 30.0 - - - - 49.7 - - - 44 32.0 - - - - 21.6 - - - 45 30.0 - - - - 22.5 - - - 46 32.0 - - - - 18.1 - - - 47 32.0 K= 5.60 7.6 15.4 48 32.0 K= 5.60 7.4 15.2 49 32.0 K= 5.60 7.4 15.2 50 32.0 K= 5.60 7.6 15.5 51 32.0 K= 5.60 8.4 16.2 52 32.0 - - - - 14.2 - - - 53 32.0 - - - - 46.4 - - - 54 30.0 - - - - 48.6 - - - 55 32.0 - - - - 21.2 - - - 56 30.0 - - - - 22.5 - - - 57 32.0 - - - - 18.8 - - - 58 29.0 - - - - 12.3 - - - 59 32.0 - - - - 11.0 - - - 60 32.0 K= 5.60 10.3 18.0 61 29.0 - - - - 11.6 - - - 62 32.0 - - - - 10.3 - - - 63 29.0 - - - - 11.5 - - - 64 32.0 - - - - 10.2 - - - 65 32.0 K= 5.60 10.2 17.9 66 32.0 K= 5.60 10.3 18.0 67 29.0 - - - - 11.7 - - 68 32.0 - - - - 10.4 - - - 69 29.0 - - - - 12.3 - - - 70 32.0 - - - - 11.0 - - - 71 32.0 K= 5.60 11.0 18.6 72 32.0 - - - - 17.4 - - - 73 32.0 - - - - 46.1 - - - 74 30.0 - - - - 48.2 - - - 75 32.0 - - - - 21.8 76 30.0 - - - - 22.6 - - - 77 32.0 - - - - 22.0 - - - 78 32.0 K= 5.60 22.9 26.8 79 32.0 - - - - 29.7 - - - 80 32.0 - - - - 46.4 - - - 81 30.0 - - - - 48.0 - - - 82 32.0 - - - - 22.2 - - - 83 30.0 - - - - 22.6 - - - 84 32.0 - - - - 23.7 - - - 85 32.0 - - - - 35.2 - - - 86 32.0 - - - - 46.6 - - - 87 30.0 - - - - 48.0 - - - 88 33.5 - - - - 21.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 89 30.0 - - - - 22.7 - - - 90 33.5 - - - - 23.6 91 33.5 - - - - 35.2 92 33.5 - - - - 45.9 93 30.0 - - - - 48.0 - - - 94 30.0 - - - - 50.1 - - - 95 30.0 - - - - 56.0 - - - BOR 0.5 - - - - 87.2 - - - UG3 -3.0 - - - - 88.8 - - - UG2 -3.0 - - - - 89.2 - - - BF2 2.0 - - - - 87.1 - - - BF1 2.0 - - - - 91.1 - - - UG1 -3.0 - - - - 93.4 - - - SRC -3.0 SOURCE 93.5 252.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 23.4 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 23.0 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 23.0 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 21.5 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 0.0 21.5 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 PL 2.21 PF 0.0 4 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 7 33.5 0.0 21.5 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 23.4 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 23.0 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 PF 0.0 6 30.0 0.0 23.0 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 21.5 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 PF 0.0 7 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 8 33.5 0.0 21.5 0.0 0.000 TL 1.75 PV Pipe: 8 0.0 1.380 PL 4.00 PF 0.0 8 33.5 0.0 21.5 0.0 0.0 120 FTG ---- PE 0.0 9 33.5 0.0 21.5 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 PL 0.83 PF 0.0 9 33.5 0.0 21.5 0.0 0.0 120 FTG T PE 0.0 10 33.5 0.0 21.5 0.0 0.000 TL 6.83 PV Pipe: 10 24.7 1.380 PL 3.50 PF 0.5 10 33.5 0.0 21.5 0.0 5.3 120 FTG T PE 1.5 11 30.0 0.0 22.5 0.0 0.051 TL 9.50 PV Pipe: 11 -24.7 1.380 PL 3.17 PF 0.5 10 33.5 0.0 21.5 0.0 5.3 120 FTG T PE 0.0 12 33.5 0.0 21.9 0.0 0.051 TL 9.17 PV Pipe: 12 -24.7 1.380 PL 4.00 PF 0.2 12 33.5 0.0 21.9 0.0 5.3 120 FTG ---- PE 0.0 13 33.5 0.0 22.1 0.0 0.051 TL 4.00 PV Pipe: 13 -24.7 1.380 PL 30.25 PF 1.6 13 33.5 0.0 22.1 0.0 5.3 120 FTG L PE 0.0 14 33.5 0.0 23.8 0.0 0.051 TL 32.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 -24.7 1.380 PL 10.42 PF 0.8 14 33.5 0.0 23.8 0.0 5.3 120 FTG T PE 0.0 15 33.5 0.0 24.6 0.0 0.051 TL 16.42 PV Pipe: 15 -24.7 1.380 PL 177.46 PF 9.7 15 33.5 0.0 24.6 0.0 5.3 120 FTG 3ET PE 0.0 16 33.5 0.0 34.3 0.0 0.051 TL 192.46 PV Pipe: 16 -24.7 1.380 PL 6.00 PF 0.3 16 33.5 0.0 34.3 0.0 5.3 120 FTG ---- PE 0.0 17 33.5 0.0 34.6 0.0 0.051 TL 6.00 PV Pipe: 17 -24.7 1.380 PL 6.00 PF 0.3 17 33.5 0.0 34.6 0.0 5.3 120 FTG ---- PE 0.0 18 33.5 0.0 34.9 0.0 0.051 TL 6.00 PV Pipe: 18 -24.7 1.380 PL 6.00 PF 0.3 18 33.5 0.0 34.9 0.0 5.3 120 FTG ---- PE 0.0 19 33.5 0.0 35.2 0.0 0.051 TL 6.00 PV Pipe: 19 -24.7 1.380 FL 6.00 PP 0.3 19 33.5 0.0 35.2 0.0 5.3 120 FTG ---- PE 0.0 20 33.5 0.0 35.5 0.0 0.051 TL 6.00 PV Pipe: 20 -24.7 1.380 PL 26.42 PF 1.6 20 33.5 0.0 35.5 0.0 5.3 120 FTG 2E PE 0.0 21 33.5 0.0 37.2 0.0 0.051 TL 32.42 PV Pipe: 21 -24.7 1.380 PL 189.96 PF 10.5 21 33.5 0.0 37.2 0.0 5.3 120 FTG 4ET PE 0.0 22 33.5 0.0 47.7 0.0 0.051 TL 207.96 PV Pipe: 22 -24.7 1.380 PL 3.50 PF 0.5 22 33.5 0.0 47.7 0.0 5.3 120 FTG T PE 1.5 23 30.0 0.0 49.7 0.0 0.051 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PP 0.0 24 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PP 0.0 25 30.0 0.0 22.0 0.0 0.0 120 FTG ---- FE 0.0 27 30.0 0.0 22.0 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PP 0.0 26 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 27 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 26 0.0 1.380 PL 3.50 PP 0.0 27 30.0 0.0 22.0 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 22.0 0.0 0.000 TL 3.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 27 0.0 1.049 FL 35.00 PF 0.0 28 29.0 0.0 22.4 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 22.0 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 FL 8.12 PF 0.0 29 30.0 0.0 22.0 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 21.1 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 FE' 0.0 30 32.0 0.0 21.1 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 21.1 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 FL 0.96 PF 0.0 31 32.0 0.0 21.1 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 21.1 0.0 0.000 TL 6.96 PV Pipe: 31 -27.7 1.380 PL 2.00 PF 0.5 32 32.0 0.0 21.1 0.0 6.0 120 FTG T FE 0.9 33 30.0 0.0 22.5 0.0 0.063 TL 8.00 PV Pipe: 32 27.7 1.380 FL 47.58 PF 3.5 32 32.0 0.0 21.1 0.0 6.0 120 FTG TL PE 0.0 34 32.0 0.0 17.6 0.0 0.063 TL 55.58 PV Pipe: 33 27.7 1.380 PL 138.50 PF 9.2 34 32.0 0.0 17.6 0.0 6.0 120 FTG 3E PE 0.0 35 32.0 0.0 8.4 0.0 0.063 TL 147.50 PV Pipe: 34 27.7 1.380 FL 14.00 FE' 1.1 35 32.0 0.0 8.4 0.0 6.0 120 FTG E FE 0.0 36 32.0 5.6 7.3 15.2 0.063 TL 17.00 PV Pipe: 35 12.6 1.380 PL 10.00 PF 0.1 36 32.0 5.6 7.3 15.2 2.7 120 FTG ---- PE 0.0 37 32.0 5.6 7.2 15.0 0.015 TL 10.00 FV Pipe: 36 -2.4 1.380 PL 8.00 PF 0.0 37 32.0 5.6 7.2 15.0 0.5 120 FTG ---- PE 0.0 39 32.0 5.6 7.2 15.0 0.001 TL 8.00 PV Pipe: 37 -14.8 1.380 PL 10.00 FE' 0.2 38 32.0 5.6 7.0 14.8 3.2 120 FTG ---- FE 0.0 39 32.0 5.6 7.2 15.0 0.020 TL 10.00 PV Pipe: 38 -32.2 1.380 FL 10.00 PF 0.8 39 32.0 5.6 7.2 15.0 6.9 120 FTG ---- FE 0.0 40 32.0 5.6 8.0 15.8 0.083 TL 10.00 PV Pipe: 39 -48.1 1.380 FL 34.67 PF 8.1 40 32.0 5.6 8.0 15.8 10.3 120 FTG 4E FE 0.0 41 32.0 0.0 16.1 0.0 0.173 TL 46.67 PV C SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAM FILES\HRS SYSTENS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 40 -48.1 1.380 PL 175.12 PF 31.4 41 32.0 0.0 16.1 0.0 10.3 120 FTG T PE 0.0 42 32.0 0.0 47.5 0.0 0.173 TL 181.12 PV Pipe: 41 -48.1 1.380 PL 2.00 PF 1.4 42 32.0 0.0 47.5 0.0 10.3 120 FTG T PE 0.9 43 30.0 0.0 49.7 0.0 0.173 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 21.6 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 22.5 0.0 0.000 TL 8.00 PV Pipe: 43 29.9 1.380 PL 41.25 PF 3.6 45 30.0 0.0 22.5- 0.0 6.4 120 FTG TL PE -0.9 46 32.0 0.0 18.1 0.0 0.072 TL 49.25 PV Pipe: 44 29.9 1.380 PL 145.04 PF 10.5 46 32.0 0.0 18.1 0.0 6.4 120 FTG ---- PE 0.0 47 32.0 5.6 7.6 15.4 0.072 TL 145.04 PV Pipe: 45 14.5 1.380 PL 10.00 PF 0.2 47 32.0 5.6 7.6 15.4 3.1 120 FTG ---- BE 0.0 48 32.0 5.6 7.4 15.2 0.019 TL 10.00 PV Pipe: 46 -0.7 1.380 PL 8.00 PF 0.0 48 32.0 5.6 7.4 15.2 0.2 120 FTG ---- PE 0.0 49 32.0 5.6 7.4 15.2 0.000 TL 8.00 PV Pipe: 47 -16.0 1.380 PL 10.00 PF 0.2 49 32.0 5.6 7.4 15.2 3.4 120 FTG ---- PE 0.0 50 32.0 5.6 7.6 15.5 0.023 TL 10.00 PV Pipe: 48 -31.4 1.380 PL 10.00 PF 0.8 50 32.0 5.6 7.6 15.5 6.7 120 FTG ---- PE 0.0 51 32.0 5.6 8.4 16.2 0.079 TL 10.00 PV Pipe: 49 -47.7 1.380 FL 27.96 PF 5.8 51 32.0 5.6 8.4 16.2 10.2 120 FTG 2E PE 0.0 52 32.0 0.0 14.2 0.0 0.171 TL 33.96 PV Pipe: 50 -47.7 1.380 PL 182.33 PF 32.2 52 32.0 0.0 14.2 0.0 10.2 120 FTG T PE 0.0 53 32.0 0.0 46.4 0.0 0.171 TL 188.33 PV Pipe: 51 -47.7 1.380 PL 2.00 PF 1.4 53 32.0 0.0 46.4 0.0 10.2 120 FTG T PE 0.9 54 30.0 0.0 48.6 0.0 0.171 TL 8.00 PV Pipe: 52 -26.6 1.380 PL 2.00 PF 0.5 55 32.0 0.0 21.2 0.0 5.7 120 FTG T PE 0.9 56 30.0 0.0 22.5 0.0 0.058 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FTY SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 26.6 1.380 PL 38.17 PF 2.3 55 32.0 0.0 21.2 0.0 5.7 120 FTG L PE 0.0 57 32.0 0.0 18.8 0.0 0.058 TL 40.17 PV Pipe: 54 26.6 1.380 PL 134.70 PF 7.8 57 32.0 0.0 18.8 0.0 5.7 120 FTG ---- PE 0.0 59 32.0 0.0 11.0 0.0 0.058 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PP 0.0 58 29.0 0.0 12.3 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 11.0 0.0 0.000 TL 35.00 By Pipe: 56 26.6 1.380 PL 12.50 PF 0.7 59 32.0 0.0 11.0 0.0 5.7 120 FTG ---- BE 0.0 60 32.0 5.6 10.3 18.0 0.058 TL 12.50 PV Pipe: 57 8.6 1.380 PL 1.83 PF 0.0 60 32.0 5.6 10.3 18.0 1.9 120 FTG ---- PE 0.0 62 32.0 0.0 10.3 0.0 0.007 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PP 0.0 61 29.0 0.0 11.6 0.0 0.0 120 FTG ---- BE -1.3 62 32.0 0.0 10.3 0.0 0.000 TL 35.00 By Pipe: 59 8.6 1.380 PL 9.25 PF 0.1 62 32.0 0.0 10.3 0.0 1.9 120 FTG ---- PE 0.0 64 32.0 0.0 10.2 0.0 0.007 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PF 0.0 63 29.0 0.0 11.5 0.0 0.0 120 FTG ---- BE -1.3 64 32.0 0.0 10.2 0.0 0.000 TL 35.00 By Pipe: 61 8.6 1.380 PL 0.92 PP 0.0 64 32.0 0.0 10.2 0.0 1.9 120 FTG ---- BE 0.0 65 32.0 5.6 10.2 17.9 0.007 TL 0.92 By Pipe: 62 -9.3 1.380 PL 12.00 PP 0.1 65 32.0 5.6 10.2 17.9 2.0 120 FTG ---- PE 0.0 66 32.0 5.6 10.3 18.0 0.008 TL 12.00 By Pipe: 63 -27.2 1.380 PL 1.42 PF 0.1 66 32.0 5.6 10.3 18.0 5.8 120 FTG ---- PE 0.0 68 32.0 0.0 10.4 0.0 0.061 TL 1.42 PV Pipe: 64 0.0 1.049 PL 35.00 PF 0.0 67 29.0 0.0 11.7 0.0 0.0 120 FTG ---- BE -1.3 68 32.0 0.0 10.4 0.0 0.000 TL 35.00 By Pipe: 65 -27.2 1.380 PL 9.17 PF 0.6 68 32.0 0.0 10.4 0.0 5.8 120 FTG ---- BE 0.0 70 32.0 0.0 11.0 0.0 0.061 TL 9.17 By SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOE TITLE: La Costa Glen Building E Calc 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (ET) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 12.3 0.0 0.0 120 FTG ---- FE -1.3 70 32.0 0.0 11.0 0.0 0.000 TL 35.00 PV Pipe: 67 -27.2 1.380 PL 1.25 PF 0.1 70 32.0 0.0 11.0 0.0 5.8 120 FTG ---- PE 0.0 71 32.0 5.6 11.0 18.6 0.061 TL 1.25 PV Pipe: 68 -45.8 1.380 PL 30.80 PF 6.3 71 32.0 5.6 11.0 18.6 9.8 120 FTG ET PE 0.0 72 32.0 0.0 17.4 0.0 0.159 TL 39.80 PV Pipe: 69 -45.8 1.380 PL 175.00 PF 28.7 72 32.0 0.0 17.4 0.0 9.8 120 FTG. T PE 0.0 73 32.0 0.0 46.1 0.0 0.159 TL 181.00 PV Pipe: 70 -45.8 1.380 PL 2.00 PP 1.3 73 32.0 0.0 46.1 0.0 9.8 120 FTG T PE 0.9 74 30.0 0.0 48.2 0.0 0.159 TL 8.00 PV Pipe: 71 7.8 1.380 PL 2.00 PP 0.0 75 32.0 0.0 21.8 0.0 1.7 120 FTG T FE 0.9 76 30.0 0.0 22.6 0.0 0.006 TL 8.00 PV Pipe: 72 -7.8 1.380 PL 38.25 PF 0.2 75 32.0 0.0 21.8 0.0 1.7 120 FTG L PE 0.0 77 32.0 0.0 22.0 0.0 0.006 TL 40.25 PV Pipe: 73 -7.8 1.380 PL 150.42 FE' 0.9 77 32.0 0.0 22.0 0.0 1.7 120 FTG ---- PE 0.0 78 32.0 5.6 22.9 26.8 0.006 TL 150.42 PV Pipe: 74 -34.6 1.380 PL 65.83 PP 6.8 78 32.0 5.6 22.9 26.8 7.4 120 FTG 2E FE 0.0 79 32.0 0.0 29.7 0.0 0.095 TL 71.83 PV Pipe: 75 -34.6 1.380 FL 170.83 PF 16.7 79 32.0 0.0 29.7 0.0 7.4 120 FTG T PS 0.0 80 32.0 0.0 46.4 0.0 0.095 TL 176.83 PV Pipe: 76 -34.6 1.380 PL 2.00 PP 0.8 80 32.0 0.0 46.4 0.0 7.4 120 FTG T PE 0.9 81 30.0 0.0 48.0 0.0 0.095 TL 8.00 PV Pipe: 77 26.3 1.380 FL 2.00 PF 0.5 82 32.0 0.0 22.2 0.0 5.6 120 FTG T FE 0.9 83 30.0 0.0 22.6 0.0 0.057 TL 8.00 PV Pipe: 78 -26.3 1.380 PL 24.58 PP 1.5 82 32.0 0.0 22.2 0.0 5.6 120 FTG L FE 0.0 84 32.0 0.0 23.7 0.0 0.057 TL 26.58 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights PIPE TAG Q(GPM) BIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 79 -26.3 1.380 FL 190.50 PF 11.5 84 32.0 0.0 23.7 0.0 5.6 120 FTG 4E PE 0.0 85 32.0 0.0 35.2 0.0 0.057 TL 202.50 PV Pipe: 80 -26.3 1.380 FL 196.21 PF 11.4 85 32.0 0.0 35.2 0.0 5.6 120 FTG T PE 0.0 86 32.0 0.0 46.6 0.0 0.057 TL 202.21 PV Pipe: 81 -26.3 1.380 PL 2.00 PF 0.5 86 32.0 0.0 46.6 0.0 5.6 120 FTG T PE 0.9 87 30.0 0.0 48.0 0.0 0.057 TL 8.00 PV Pipe: 82 25.5 1.380 FL 3.50 PF 0.5 88 33.5 0.0 21.7 0.0 5.5 120 FTG T FE 1.5 89 30.0 0.0 22.7 0.0 0.054 TL 9.50 PV Pipe: 83 -25.5 1.380 PL 33.58 PP 1.9 88 33.5 0.0 21.7 0.0 5.5 120 FTG L PE 0.0 90 33.5 0.0 23.6 0.0 0.054 TL 35.58 PV Pipe: 84 -25.5 1.380 PL 202.38 PP 11.7 90 33.5 0.0 23.6 0.0 5.5 120 FTG 3ET FE 0.0 91 33.5 0.0 35.2 0.0 0.054 TL 217.38 PV Pipe: 85 -25.5 1.380 PL 193.96 PF 10.7 91 33.5 0.0 35.2 0.0 5.5 120 FTG T FE 0.0 92 33.5 0.0 45.9 0.0 0.054 TL 199.96 FV Pipe: 86 -25.5 1.380 FL 3.50 PF 0.5 92 33.5 0.0 45.9 0.0 5.5 120 FTG T FE 1.5 93 30.0 0.0 48.0 0.0 0.054 TL 9.50 PV Pipe: 87 24.7 2.635 PL 3.00 PP 0.0 11 30.0 0.0 22.5 0.0 1.5 120 FTG ---- PE 0.0 33 30.0 0.0 22.5 0.0 0.002 TL 3.00 PV Pipe: 88 -3.0 2.635 PL 8.50 PP 0.0 33 30.0 0.0 22.5 0.0 0.2 120 FTG ---- FE 0.0 45 30.0 0.0 22.5 0.0 0.000 TL 8.50 PV Pipe: 89 -33.0 2.635 FL 6.92 PP 0.0 45 30.0 0.0 22.5 0.0 1.9 120 FTG ---- FE 0.0 56 30.0 0.0 22.5 0.0 0.004 TL 6.92 PV Pipe: 90 -59.6 2.635 FL 7.42 PF 0.1 56 30.0 0.0 22.5 0.0 3.5 120 FTG ---- FE 0.0 76 30.0 0.0 22.6 0.0 0.011 TL 7.42 PV Pipe: 91 -51.7 2.635 PL 7.00 PP 0.1 76 30.0 0.0 22.6 0.0 3.0 120 FTG ---- FE 0.0 83 30.0 0.0 22.6 0.0 0.009 TL 7.00 PV ) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 92 -25.5 2.635 PL 3.92 PF 0.0 83 30.0 0.0 22.6 0.0 1.5 120 FTG ---- PE 0.0 89 30.0 0.0 22.7 0.0 0.002 TL 3.92 PV Pipe: 93 -24.7 2.635 PL 5.54 PF 0.0 23 30.0 0.0 49.7 0.0 1.5 120 FTG ---- PE 0.0 43 30.0 0.0 49.7 0.0 0.002 TL 5.54 PV Pipe: 94 -72.8 2.635 PL 8.96 PF 0.4 43 30.0 0.0 49.7 0.0 4.3 120 FTG T FE 0.0 94 30.0 0.0 50.1 0.0 0.016 TL 25.96 PV Pipe: 95 -25.5 2.635 PL 5.40 PF 0.0 93 30.0 0.0 48.0 0.0 1.5 120 FTG ---- PE 0.0 87 30.0 0.0 48.0 0.0 0.002 TL 5.40 PV Pipe: .96 -51.7 2.635 PL 9.50 PF 0.1 87 30.0 0.0 48.0 0.0 3.0 120 FTG ---- PE 0.0 81 30.0 0.0 48.0 0.0 0.009 TL 9.50 PV Pipe: 97 -86.4 2.635 PL 8.17 PF 0.2 81 30.0 0.0 48.0 0.0 5.1 120 FTG ---- PE 0.0 74 30.0 0.0 48.2 0.0 0.022 TL 8.17 PV Pipe: 98 -132.2 2.635 PL 7.96 PF 0.4 74 30.0 0.0 48.2 0.0 7.8 120 FTG ---- PE 0.0 54 30.0 0.0 48.6 0.0 0.048 TL 7.96 PV Pipe: 99 -179.9 2.635 PL 1.04 PF 1.5 54 30.0 0.0 48.6 0.0 10.6 120 FTG T FE 0.0 94 30.0 0.0 50.1 0.0 0.085 TL 18.04 PV Pipe: 100 -252.7 2.635 PL 20.38 PF 5.8 94 30.0 0.0 50.1 0.0 14.9 120 FTG 2E FE 0.0 95 30.0 0.0 56.0 0.0 0.160 TL 36.38 PV Pipe: 101 -252.7 2.635 PL 75.50 PF 18.5 95 30.0 0.0 56.0 0.0 14.9 120 FTG SE PE 12.8 BOR 0.5 0.0 87.2 0.0 0.160 TL 115.50 PV Pipe: 102 -252.7 6.280 PL 10.00 PF 0.1 BOR 0.5 0.0 87.2 0.0 2.6 140 FTG E FE 1.5 UG3 -3.0 0.0 88.8 0.0 0.002 TL 32.00 PV Pipe: 103 -252.7 6.080 PL 142.00 PF 0.4 UG3 -3.0 0.0 88.8 0.0 2.8 150 FTG 3E PE 0.0 UG2 -3.0 0.0 89.2 0.0 0.002 TL 208.00 PV Pipe: 104 -252.7 6.280 PL 5.00 PF 0.1 UG2 -3.0 0.0 89.2 0.0 2.6 140 FTG ET FE -2.2 BF2 2.0 0.0 87.1 0.0 0.002 TL 74.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRA14 FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Caic 1 - Standard Uprights PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 91.1 0.0 4.0 psi, 252.7 gpm SF2 2.0 0.0 87.1 0.0 Pipe: 106 -252.7 6.280 PL 5.00 PP 0.1 BF1 2.0 0.0 91.1 0.0 2.6 140 FTG 2E PE 2.2 UG1 -3.0 0.0 93.4 0.0 0.002 TL 49.00 PV Pipe: 107 -252.7 6.080 FL 16.00 PP 0.1 UG1 -3.0 0.0 93.4 0.0 2.8 150 FTG TG FE 0.0 SRC -3.0 SRCE 93.5 (N/A) 0.002 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.169 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.9 ft/sec at pipe 100. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.54 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC l.SDF JOB TITLE: La Costa Glen Building E Cab 1 - Standard Uprights PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ebb Tee LngEll ChkVbv BfyVlv GatVlv AbmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ebb Tee LngEll ChkVbv BfyViv GatVlv AbmChk DPVlv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVbv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVbv BfyVbv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 140.0 120.0 P100.0 R E S S 80.0 U R E A I WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm LEGEND 1- Availablepressure 154.70 psi @ 352.7 gpm---- 2 Required pressure 93.52 psi @ 352.7 gpm 1A Avail. OnSite Demand Press 154.70 psi 8 252.7 gpm 2A Req. OnSite Demand Press. 93.52 psi @ 252.7 gpm A. Source Supply Curve System Demand Curve Available at Source p 5 i 40.0 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) ished Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 1.SDF JOB TITLE: La Costa Glen Building E Calc 1 - Standard Uprights WATER SUPPLY CURVE I \\\\\\\\\\\\\\\\\\\\\\\\\\ I 149.0 psi 8 1790 gpm-> * Flow Test Point 143+ 130+ 117+ P104+ R E S IX S 91+ U I R E 78+ ( I P I S I I 65+ 52+ 39+ 26+ LEGEND I' I X = Required Water Supply I 93.52 psi 8 352.7 gpm 13+ I 0 = Available Water Supply I 154.70 psi 8 352.7 gpm I, 0++-+----+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS WATER SUPPLY DATA SOURCE STATIC NODE PRESS. TAG (PSI) SRC 155.0 RESID. FLOW PRESS. @ (PSI) (GPM) 149.0 1790.0 AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 154.9 226.1 123.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 226.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 126.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 91.2 - - - 2 30.0 - - - - 90.8 - - - 3 33.5 - - - - 89.3 - - - 4 33.5 - - - - 89.3 - - - 5 29.0 - - - - 91.2 - - - 6 30.0 - - - - 90.8 - - - 7 33.5 - - - - 89.3 - - - 8 33.5 - - - - 89.3 9 33.5 - - - - 89.3 - - - 10 33.5 - - - - 89.3 - - - 11 30.0 - - - - 93.4 - - - 12 33.5 - - - - 86.8 - - - 13 33.5 - - - - 85.7 - - - 14 33.5 - - - - 77.0 - - - 15 33.5 - - - - 72.6 - - - 16 33.5 K= 5.60 20.6 25.4 17 33.5 K= 5.60 20.0 25.0 18 33.5 K= 5.60 19.9 25.0 19 33.5 K= 5.60 20.0 25.1 20 33.5 K= 5.60 20.8 25.5 21 33.5 - - - - 30.6 - - - 22 33.5 - - - - 93.4 - - - 23 30.0 - - - - 97.8 - - - 24 29.0 - - - - 93.9 - - - 25 30.0 - - - - 93.5 - - - 26 29.0 - - - - 93.9 - - - 27 30.0 - - - - 93.5 - - - 28 29.0 - - - - 93.9 - - - 29 30.0 - - - - 93.5 - - - 30 32.0 - - - - 92.6 - - - 31 32.0 - - - - 92.6 - - - 32 32.0 - - - - 92.6 - - - 33 30.0 - - - - 93.4 - - - 34 32.0 - - - - 93.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 94.5 - - - 36 32.0 - - - - 94.6 - - - 37 32.0 - - - - 94.7 - - - 38 32.0 - - - - 94.8 - - - 39 32.0 - - - - 94.8 - - - 40 32.0 - - - - 94.9 - - - 41 32.0 - - - - 95.3 - - - 42 32.0 - - - - 96.9 - - - 43 30.0 - - - - 97.9 - - - 44 32.0 - - - - 92.6 - - - 45 30.0 - - - - 93.5 - - - 46 32.0 - - - - 93.1 - - - 47 32.0 - - - - 94.6 - - - 48 32.0 - - - - 94.7 - - - 49 32.0 - - - - 94.8 - - - 50 32.0 - - - - 94.9 - - - 51 32.0 - - - - 95.0 - - - 52 32.0 - - - - 95.3 53 32.0 - - - - 97.2 54 30.0 - - - - 98.2 - - - 55 32.0 - - - - 92.7 56 30.0 - - - - 93.5 - - - 57 32.0 - - - - 93.1 - - - 58 29.0 - - - - 95.8 - - - 59 32.0 - - - - 94.5 60 32.0 - - - - 94.6 - - - 61 29.0 - - - - 95.9 - - - 62 32.0 - - - - 94.6 - - - 63 29.0 - - - - 96.0 - - - 64 32.0 - - - - 94.7 - - - 65 32.0 - - - - 94.7 - - - 66 32.0 - - - - 94.9 - - - 67 29.0 - - - - 96.2 - - - 68 32.0 - - - - 94.9 - - - 69 29.0 - - - - 96.3 - - - 70 32.0 - - - - 95.0 - - - 71 32.0 - - - - 95.0 - - - 72 32.0 - - - - 95.4 - - - 73 32.0 - - - - 97.2 - - - 74 30.0 - - - - 98.1 - - - 75 32.0 - - - - 92.8 - - - 76 30.0 - - - - 93.5 - - - 77 32.0 - - - - 93.2 - - - 78 32.0 - - - - 94.7 - - - 79 32.0 - - - - 95.4 - - - 80 32.0 - - - - 97.2 - - - 81 30.0 - - - - 98.1 - - - 82 32.0 - - - - 92.8 - - - 83 30.0 - - - - 93.6 - - - 84 32.0 - - - - 93.0 - - - 85 32.0 - - - - 95.1 - - - 86 32.0 - - - - 97.1 - - - A SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 87 30.0 - - - - 98.1 - - - 88 33.5 - - - - 92.1 89 30.0 - - - - 93.6 - - - 90 33.5 - - - - 92.5 91 33.5 - - - - 94.6 - - - 92 33.5 - - - - 96.5 - - - 93 30.0 - - - - 98.1 - - - 94 30.0 - - - - 98.3 - - - 95 30.0 - - - - 99.9 - - - BOR 0.5 - - - - 117.8 UG3 -3.0 - - - - 119.3 - - - UG2 -3.0 - - - - 119.4 - - - BF2 2.0 - - - - 117.3 - - - BF1 2.0 - - - - 121.3 - - - UG1 -3.0 - - - - 123.5 SRC -3.0 SOURCE 123.5 126.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SD1 ATTIC HEADS PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 91.2 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 90.8 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 90.8 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 89.3 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 0.0 89.3 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 PL 2.21 PF 0.0 4 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 7 33.5 0.0 89.3 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 91.2 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 90.8 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 PF 0.0 6 30.0 0.0 90.8 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 89.3 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 PF 0.0 7 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 8 33.5 0.0 89.3 0.0 0.000 TL 1.75 PV Pipe: 8 0.0 1.380 PL 4.00 PF 0.0 8 33.5 0.0 89.3 0.0 0.0 120 FTG ---- PE 0.0 9 33.5 0.0 89.3 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 PL 0.83 PF 0.0 9 33.5 0.0 89.3 0.0 0.0 120 FTG T PE 0.0 10 33.5 0.0 89.3 0.0 0.000 TL 6.83 PV Pipe: 10 -61.1 1.380 PL 3.50 PF 2.6 10 33.5 0.0 89.3 0.0 13.1 120 FTG T PE 1.5 11 30.0 0.0 93.4 0.0 0.270 TL 9.50 PV Pipe: 11 61.1 1.380 PL 3.17 PF 2.5 10 33.5 0.0 89.3 0.0 13.1 120 FTG T PE 0.0 12 33.5 0.0 86.8 0.0 0.270 TL 9.17 PV Pipe: 12 61.1 1.380 PL 4.00 PF 1.1 12 33.5 0.0 86.8 0.0 13.1 120 FTG ---- PE 0.0 13 33.5 0.0 85.7 0.0 0.270 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 61.1 1.380 PL 30.25 PF 8.7 13 33.5 0.0 85.7 0.0 13.1 120 FTG L PE 0.0 14 33.5 0.0 77.0 0.0 0.270 TL 32.25 PV Pipe: 14 61.1 1.380 PL 10.42 PF 4.4 14 33.5 0.0 77.0 0.0 13.1 120 FTG T PE 0.0 15 33.5 0.0 72.6 0.0 0.270 TL 16.42 PV Pipe: 15 61.1 1.380 PL 177.46 PF 52.0 15 33.5 0..0 72.6 0.0 13.1 120 FTG 3ET PH 0.0 16 33.5 5.6 20.6 25.4 0.270 TL 192.46 PV Pipe: 16 35.7 1.380 PL 6.00 PF 0.6 16 33.5 5.6 20.6 25.4 7.7 120 FTG ---- PE 0.0 17 33.5 5.6 20.0 25.0 0.100 TL 6.00 PV Pipe: 17 10.7 1.380 PL 6.00 PF 0.1 17 33.5 5.6 20.0 25.0 2.3 120 FTG ---- PE 0.0 18 33.5 5.6 19.9 25.0 0.011 TL 6.00 PV Pipe: 18 -14.3 1.380 PL 6.00 PF 0.1 18 33.5 5.6 19.9 25.0 3.1 120 FTG ---- PE 0.0 19 33.5 5.6 20.0 25.1 0.019 TL 6.00. PV Pipe: 19 -39.4 1.380 PL 6.00 PF 0.7 19 33.5 5.6 20.0 25.1 8.5 120 FTG ---- PE 0.0 20 33.5 5.6 20.8 25.5 0.120 TL 6.00 PV Pipe: 20 -64.9 1.380 PL 26.42 PF 9.8 20 33.5 5.6 20.8 25.5 13.9 120 FTG 2E PE 0.0 21 33.5 0.0 30.6 0.0 0.302 TL 32.42 PV Pipe: 21 -64.9 1.380 PL 189.96 PF 62.9 21 33.5 0.0 30.6 0.0 13.9 120 FTG 4ET PE 0.0 22 33.5 0.0 93.4 0.0 0.302 TL 207.96 PV Pipe: 22 -64.9 1.380 PL 3.50 PF 2.9 22 33.5 0.0 93.4 0.0 13.9 120 FTG T PE 1.5 23 30.0 0.0 97.8 0.0 0.302 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PF 0.0 24 29.0 0.0 93.9 0.0 0.0 120 FTG ---- PE -0.4 25 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PF 0.0 25 30.0 0.0 93.5 0.0 0.0 120 FTG ---- FE 0.0 27 30.0 0.0 93.5 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PF 0.0 26 29.0 0.0 93.9 0.0 0.0 120 FTG ---- PE -0.4 27 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.380 PL 3.50 PF 0.0 27 30.0 0.0 93.5 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 93.5 0.0 0.000 TL 3.50 PV Pipe: 27 0.0 1.049 PL 35.00 PF 0.0 28 29.0 0.0 93.9 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 93.5 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 93.5 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 92.6 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PF 0.0 30 32.0 0.0 92.6 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 92.6 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PF 0.0 31 32.0 0.0 92.6 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 92.6 0.0 0.000 TL 6.96 PV Pipe: 31 9.8 1.380 PL 2.00 PF 0.1 32 32.0 0.0 92.6 0.0 2.1 120 FTG T PE 0.9 33 30.0 0.0 93.4 0.0 0.009 TL 8.00 PV Pipe: 32 -9.8 1.380 PL 47.58 PF 0.5 32 32.0 0.0 92.6 0.0 2.1 120 FTG TL PE 0.0 34 32.0 0.0 93.1 0.0 0.009 TL 55.58 PV Pipe: 33 -9.8 1.380 PL 138.50 PF 1.3 34 32.0 0.0 93.1 0.0 2.1 120 FTG 3E PE 0.0 35 32.0 0.0 94.5 0.0 0.009 TL 147.50 PV Pipe: 34 -9.8 1.380 PL 14.00 PF 0.2 35 32.0 0.0 94.5 0.0 2.1 120 FTG E PE 0.0 36 32.0 0.0 94.6 0.0 0.009 TL 17.00 PV Pipe: 35 -9.8 1.380 PL 10.00 PF 0.1 36 32.0 0.0 94.6 0.0 2.1 120 FTC ---- PE 0.0 37 32.0 0.0 94.7 0.0 0.009 TL 10.00 PV Pipe: 36 -9.8 1.380 PL 8.00 PF 0.1 37 32.0 0.0 94.7 0.0 2.1 120 FTC ---- PE 0.0 39 32.0 0.0 94.8 0.0 0.009 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 PF 0.0 38 32.0 0.0 94.8 0.0 0.0 120 FTC ---- PE 0.0 39 32.0 0.0 94.8 0.0 0.000 TL 10.00 PV Pipe: 38 -9.8 1.380 PL 10.00 PF 0.1 39 32.0 0.0 94.8 0.0 2.1 120 FTC ---- PE 0.0 40 32.0 0.0 94.9 0.0 0.009 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -9.8 1.380 PL 34.67 PP 0.4 40 32.0 0.0 94.9 0.0 2.1 120 FTG 4E PE 0.0 41 32.0 0.0 95.3 00 0.009 TL 46.67 PV Pipe: 40 -9.8 1.380 PL 175.12 PP 1.6 41 32.0 0.0 95.3 0.0 2.1 120 FTG T PE 0.0 42 32.0 0.0 96.9 0.0 0.009 TL 181.12 PV Pipe: 41 -9.8 1.380 PL 2.00 PF 0.1 42 32.0 0.0 96.9 0.0 2.1 120 FTG T PE 0.9 43 30.0 0.0 97.9 0.0 0.009 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 92.6 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 93.5 0.0 0.000 TL 8.00 PV Pipe: 43 -10.4 1.380 PL 41.25 PP 0.5 45 30.0 0.0 93.5 0.0 2.2 120 FTG TL PE -0.9 46 32.0 0.0 93.1 0.0 0.010 TL 49.25 PV Pipe: 44 -10.4 1.380 PL 145.04 PF 1.5 46 32.0 0.0 93.1 0.0 2.2 120 FTG ---- PE 0.0 47 32.0 0.0 94.6 0.0 0.010 TL 145.04 PV Pipe: 45 -10.4 1.380 PL 10.00 PF 0.1 47 32.0 0.0 94.6 0.0 2.2 120 FTG ---- PE 0.0 48 32.0 0.0 94.7 0.0 0.010 TL 10.00 PV Pipe: 46 -10.4 1.380 PL 8.00 PF 0.1 48 32.0 0.0 94.7 0.0 2.2 120 FTG ---- PE 0.0 49 32.0 0.0 94.8 0.0 0.010 TL 8.00 PV Pipe: 47 -10.4 1.380 PL 10.00 PP 0.1 49 32.0 0.0 94.8 0.0 2.2 120 FTG ---- PE 0.0 50 32.0 0.0 94.9 0.0 0.010 TL 10.00 PV Pipe: 48 -10.4 1.380 PL 10.00 PF 0.1 50 32.0 0.0 94.9 0.0 2.2 120 FTG ---- PS 0.0 51 32.0 0.0 95.0 0.0 0.010 TL 10.00 PV Pipe: 49 -10.4 1.380 PL 27.96 PF 0.3 51 32.0 0.0 95.0 0.0 2.2 120 FTG 2E PE 0.0 52 32.0 0.0 95.3 0.0 0.010 TL 33.96 PV Pipe: 50 -10.4 1.380 PL 182.33 PP 1.9 52 32.0 0.0 95.3 0.0 2.2 120 FTG T PE 0.0 53 32.0 0.0 97.2 0.0 0.010 TL 188.33 PV Pipe: 51 -10.4 1.380 PL 2.00 PF 0.1 53 32.0 0.0 97.2 0.0 2.2 120 FTG T PE 0.9 54 30.0 0.0 98.2 0.0 0.010 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Cab 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 10.3 1.380 FL 2.00 PF 0.1 55 32.0 0.0 92.7 0.0 2.2 120 FTG T PE 0.9 56 30.0 0.0 93.5 0.0 0.010 TL 8.00 PV Pipe: 53 -10.3 1.380 PL 38.17 PF 0.4 55 32.0 0.0 92.7 0.0 2.2 120 FTG L PE 0.0 57 32.0 0.0 93.1 0.0 0.010 TL 40.17 PV Pipe: 54 -10.3 1.380 FL 134.70 PF 1.3 57 32.0 0.0 93.1 0.0 2.2 120 FTG ---- FE 0.0 59 32.0 0.0 94.5 0.0 0.010 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 95.8 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 94.5 0.0 0.000 TL 35.00 PV Pipe: 56 -10.3 1.380 PL 12.50 PF 0.1 59 32.0 0.0 94.5 0.0 2.2 120 FTG ---- PE 0.0 60 32.0 0.0 94.6 0.0 0.010 TL 12.50 PV Pipe: 57 -10.3 1.380 PL 1.83 PF 0.0 60 32.0 0.0 94.6 0.0 2.2 120 FTG ---- FE 0.0 62 32.0 0.0 94.6 0.0 0.010 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PF 0.0 61 29.0 0.0 95.9 0.0 0.0 120 FTG ---- FE -1.3 62 32.0 0.0 94.6 0.0 0.000 TL 35.00 PV Pipe: 59 -10.3 1.380 FL 9.25 FE' 0.1 62 32.0 0.0 94.6 0.0 2.2 120 FTG ---- FE 0.0 64 32.0 0.0 94.7 0.0 0.010 TL 9.25 PV Pipe: 60 0.0 1.049 FL 35.00 FE' 0.0 63 29.0 0.0 96.0 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 94.7 0.0 0.000 TL 35.00 PV Pipe: 61 -10.3 1.380 PL 0.92 FE' 0.0 64 32.0 0.0 94.7 0.0 2.2 120 FTG ---- FE 0.0 65 32.0 0.0 94.7 0.0 0.010 TL 0.92 PV Pipe: 62 -10.3 1.380 FL 12.00 PF 0.1 65 32.0 0.0 94.7 0.0 2.2 120 FTG ---- FE 0.0 66 32.0 0.0 94.9 0.0 0.010 TL 12.00 PV Pipe: 63 -10.3 1.380 PL 1.42 PF 0.0 66 32.0 0.0 94.9 0.0 2.2 120 FTG ---- FE 0.0 68 32.0 0.0 94.9 0.0 0.010 TL 1.42 PV Pipe: 64 0.0 1.049 FL 35.00 PF 0.0 67 29.0 0.0 96.2 0.0 0.0 120 FTG ---- FE -1.3 68 32.0 0.0 94.9 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTENS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -10.3 1.380 PL 9.17 PP 0.1 68 32.0 0.0 94.9 0.0 2.2 120 FTG ---- PE 0.0 70 32.0 0.0 95.0 0.0 0.010 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 96.3 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 95.0 00 0.000 TL 35.00 PV Pipe: 67 -10.3 1.380 PL 1.25 PP 0.0 70 32.0 0.0 95.0 0.0 2.2 120 FTG ---- FE 0.0 71 32.0 0.0 95.0 0.0 0.010 TL 1.25 PV Pipe: 68 -10.3 1.380 PL 30.80 PF 0.4 71 32.0 0.0 95.0 0.0 2.2 120 FTG ET PE 0.0 72 32.0 0.0 95.4 0.0 0.010 TL 39.80 PV Pipe: 69 -10.3 1.380 FL 175.00 PF 1.-8 72 32.0 0.0 95.4 0.0 2.2 120 FTG T PE 0.0 73 32.0 0.0 97.2 0.0 0.010 TL 181.00 PV Pipe: 70 -10.3 1.380 PL 2.00 PF 0.1 73 32.0 0.0 97.2 0.0 2.2 120 FTG T PE 0.9 74 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 71 10.3 1.380 PL 2.00 PP 0.1 75 32.0 0.0 92.8 0.0 2.2 120 FTG T FE 0.9 76 30.0 0.0 93.5 0.0 0.010 TL 8.00 PV Pipe: 72 -10.3 1.380-PL 38.25 PP 0.4 75 32.0 0.0 92.8 0.0 2.2 120 FTG L PE 0.0 77 32.0 0.0 93.2 0.0 0.010 TL 40.25 PV Pipe: 73 -10.3 1.380 FL 150.42 PF 1.5 77 32.0 0.0 93.2 0.0 2.2 120 FTG ---- FE 0.0 78 32.0 0.0 94.7 0.0 0.010 TL 150.42 PV Pipe: 74 -10.3 1.380 FL 65.83 PP 0.7 78 32.0 0.0 94.7 0.0 2.2 120 FTG 2E PE 0.0 79 32.0 0.0 95.4 0.0 0.010 TL 71.83 PV Pipe: 75 -10.3 1.380 FL 170.83 FE' 1.8 79 32.0 0.0 95.4 0.0 2.2 120 FTG T FE 0.0 80 32.0 0.0 97.2 0.0 0.010 TL 176.83 PV Pipe: 76 -10.3 1.380 FL 2.00 PF 0.1 80 32.0 0.0 97.2 0.0 2.2 120 FTG T FE 0.9 81 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 77 10.4 1.380 PL 2.00 PP 0.1 82 32.0 0.0 92.8 0.0 2.2 120 FTG T FE 0.9 83 30.0 0.0 93.6 0.0 0.010 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -10.4 1.380 PL 24.58 PF 0.3 82 32.0 0.0 92.8 0.0 2.2 120 FTG L PE 0.0 84 32.0 0.0 93.0 0.0 0.010 TL 26.58 PV Pipe: 79 -10.4 1.380 PL 190.50 PF 2.0 84 32.0 0.0 93.0 0.0 2.2 120 FTG 4E PE 0.0 85 32.0 0.0 95.1 0.0 0.010 TL 202.50 PV Pipe: 80 -10.4 1.380 PL 196.21 PF 2.0 85 32.0 0.0 95.1 0.0 2.2 120 FTG T PE 0.0 86 32.0 0.0 97.1 0.0 0.010 TL 202.21 PV Pipe: 81 -10.4 1.380 PL 2.00 PF 0.1 86 32.0 0.0 97.1 0.0 2.2 120 FTG T PE 0.9 87 30.0 0.0 98.1 0.0 0.010 TL 8.00 PV Pipe: 82 10.1 1.380 PL 3.50 PF 0.1 88 33.5 0.0 92.1 0.0 2.2 120 FTG T PE 1.5 89 30.0 0.0 93.6 0.0 0.010 TL 9.50 PV Pipe: 83 -10.1 1.380 PL 33.58 PF 0.3 88 33.5 0.0 92.1 0.0 2.2 120 FTG L PE 0.0 90 33.5 0.0 92.5 0.0 0.010 TL 35.58 PV Pipe: 84 -10.1 1.380 PL 202.38 PF 2.1 90 33.5 0.0 92.5 0.0 2.2 120 FTG 3ET PE 0.0 91 33.5 0.0 94.6 0.0 0.010 TL 217.38 PV Pipe: 85 -10.1 1.380 PL 193.96 PF 1.9 91 33.5 0.0 94.6 0.0 2.2 120 FTG T PE 0.0 92 33.5 0.0 96.5 0.0 0.010 TL 199.96 PV Pipe: 86 -10.1 1.380 PL 3.50 PF 0.1 92 33.5 0.0 96.5 0.0 2.2 120 FTG T PE 1.5 93 30.0 0.0 98.1 0.0 0.010 TL 9.50 PV Pipe: 87 -61.1 2.635 PL 3.00 PF 0.0 11 30.0 0.0 93.4 0.0 3.6 120 FTG ---- PE 0.0 33 30.0 0.0 93.4 0.0 0.012 TL 3.00 PV Pipe: 88 -51.3 2.635 PL 8.50 PF 0.1 33 30.0 0.0 93.4 0.0 3.0 120 FTG ---- PE 0.0 45 30.0 0.0 93.5 0.0 0.008 TL 8.50 PV Pipe: 89 -41.0 2.635 PL 6.92 PF 0.0 45 30.0 0.0 93.5 0.0 2.4 120 FTG ---- PE 0.0 56 30.0 0.0 93.5 0.0 0.006 TL 6.92 PV Pipe: 90 -30.7 2.635 PL 7.42 PF 0.0 56 30.0 0.0 93.5 0.0 1.8 120 FTG ---- PE 0.0 76 30.0 0.0 93.5 0.0 0.003 TL 7.42 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -20.4 2.635 PL 7.00 PF 0.0 76 30.0 0.0 93.5 0.0 1.2 120 FTG ---- PE 0.0 83 30.0 0.0 93.6 0.0 0.002 TL 7.00 PV Pipe: 92 -10.1 2.635 PL 3.92 PF 0.0 83 30.0 0.0 93.6 0.0 0.6 120 FTC ---- PE 0.0 89 30.0 0.0 93.6 0.0 0.000 TL 3.92 PV Pipe: 93 -64.9 2.635 PL 5.54 PF 0.1 23 30.0 0.0 97.8 0.0 3.8 120 FTG ---- PE 0.0 43 30.0 0.0 97.9 0.0 0.013 TL 5.54 PV Pipe: 94 -74.7 2.635 PL 8.96 PF 0.4 43 30.0 0.0 97.9 0.0 4.4 120 FTG T PE 0.0 94 30.0 0.0 98.3 0.0 0.017 TL 25.96 PV Pipe: 95 -10.1 2.635 PL 5.40 PF 0.0 93 30.0 0.0 98.1 0.0 0.6 120 FTG ---- PE 0.0 87 30.0 0.0 98.1 0.0 0.000 TL 5.40 PV Pipe: 96 -20.4 2:635 PL 9.50 PF 0.0 87 30.0 0.0 98.1 0.0 1.2 120 FTG ---- PE 0.0 81 30.0 0.0 98.1 0.0 0.002 TL 9.50 PV Pipe: 97 -30.7 2.635 PL 8.17 PF 0.0 81 30.0 0.0 98.1 0.0 1.8 120 FTG ---- PE 0.0 74 30.0 0.0 98.1 0.0 0.003 TL 8.17 PV Pipe: 98 -41.0 2.635 PL 7.96 PF 0.0 74 30.0 0.0 98.1 0.0 2.4 120 FTG ---- PE 0.0 54 30.0 0.0 98.2 0.0 0.006 TL 7.96 PV Pipe: 99 -51.3 2.635 PL 1.04 PF 0.2 54 30.0 0.0 98.2 0.0 3.0 120 FTG T PE 0.0 94 30.0 0.0 98.3 0.0 0.008 TL 18.04 PV Pipe: 100 -126.0 2.635 PL 20.38 PF 1.6 94 30.0 0.0 98.3 0.0 7.4 120 FTG 2E PE 0.0 95 30.0 0.0 99.9 0.0 0.044 TL 36.38 PV Pipe: 101 -126.0 2.635 PL 75.50 PF 5.1 95 30.0 0.0 99.9 0.0 7.4 120 FTG SE PE 12.8 BOR 0.5 0.0 117.8 0.0 0.044 TL 115.50 PV Pipe: 102 -126.0 6.280 PL 10.00 PF 0.0 BOR 0.5 0.0 117.8 0.0 1.3 140 FTG E PE 1.5 UG3 -3.0 0.0 119.3 0.0 0.000 TL 32.00 PV Pipe: 103 -126.0 6.080 PL 142.00 PF 0.1 UG3 -3.0 0.0 119.3 0.0 1.4 150 FTG 3E PE 0.0 UG2 -3.0 0.0 119.4 0.0 0.000 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -126.0 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 119.4 0.0 1.3 140 FTG ET FE -2.2 BF2 2.0 0.0 117.3 0.0 0.000 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE EF1 2.0 0.0 121.3 0.0 4.0 psi, 126.0 gpm BF2 2.0 0.0 117.3 0.0 Pipe: 106 -126.0 6.280 PL 5.00 PF 0.0 BF1 2.0 0.0 121.3 0.0 1.3 140 FTG 2E PE 2.2 UG1 -3.0 0.0 123.5 0.0 0.000 TL 49.00 PV Pipe: 107 -126.1 6.080 PL 16.00 PF 0.0 UG1 -3.0 0.0 123.5 0.0 1.4 150 FTG TG PE 0.0 SRC -3.0 SRCE 123.5 (N/A) 0.000 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum. imbalance at any node of 0.114 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 13.9 ft/sec at pipe 22. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.85 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Calc 2 - SD1 ATTIC HEADS PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 1A 140.0 G A 2A U120. G E P100. 0 R E S S 80.0 U R E p S 40.0 WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm LEGEND 1Availab1e pressure 154.87 psi 8 226.1 gpm - 2 Required pressure 123.54 psi @ 226.1 gpm 1A Avail. OnSite Demand Press 154.87 psi @ 126.1 gpm 2A Req. OnSite Demand Press. 123.54 psi 8 126.1 gpm A. Source Supply Curve System Demand Curve Available at Source 20.0 B 0.0 -14.7 400 600 800 1000 1200 1400 1600 2000 FLOW (GPM) 3hed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRA.M FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 2.SDF JOB TITLE: La Costa Glen Building E Caic 2 - SDI ATTIC HEADS WATER SUPPLY CURVE 156* Q\ \\ \ \ \\ \\ \\ \ \ \ \\\ \ \ \\\ \\ \ I \\\\\\\\\\\\\\\\\\\\\\\\\\ 149.0 psi 8 1790 gpm-> * I Flow Test Point 143+ 130+ Ix 117+ P104+ R I E S S 91+ U I R I E I 78+ P I S I I 65+ ) I 52+ 39+ 26+ LEGEND 'I I X = Required Water Supply 123.54 psi 8 226.1 gpm 13+ I 0 = Available Water Supply I 154.87 psi 8 226.1 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 155.0 149.0 1790.0 154.9 215.0 100.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 215.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 115.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 72.9 - - - 2 30.0 - - - - 72.5 - - - 3 33.5 - - - - 71.0 - - - 4 33.5 - - - - 71.0 - - - 5 29.0 - - - - 72.9 - - - 6 30.0 - - - - 72.5 7 33.5 - - - - 71.0 - - - 8 33.5 - - - - 71.0 - - - 9 33.5 - - - - 71.0 10 33.5 - - - - 71.0 - - - 11 30.0 - - - - 72.4 - - - 12 33.5 - - - - 71.1 - - - 13 33.5 - - - - 71.1 - - - 14 33.5 - - - - 71.3 - - - 15 33.5 - - - - 71.5 - - - 16 33.5 - - - - 72.9 - - - 17 33.5 - - - - 72.9 - - - 18 33.5 - - - - 73.0 19 33.5 - - - - 73.0 - - - 20 33.5 - - - - 73.1 21 33.5 - - - - 73.3 - - - 22 33.5 - - - - 74.9 - - - 23 30.0 - - - - 76.4 - - - 24 29.0 - - - - 71.0 - - - 25 30.0 - - - - 70.5 - - - 26 29.0 - - - - 71.0 - - - 27 30.0 - - - - 70.5 - - - 28 29.0 - - - - 71.0 - - - 29 30.0 - - - - 70.5 - - - 30 32.0 - - - - 69.7 - - - 31 32.0 - - - - 69.7 - - - 32 32.0 - - - - 69.7 - - - 33 30.0 - - - - 72.4 - - - 34 32.0 - - - - 56.5 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAJ4 FILES\HRS SYSTENS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Cab 3 - 5 Head Corridor Calc NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 21.6 - - - 36 32.0 K= 5.60 17.5 23.5 37 32.0 K= 5.60 16.7 22.9 38 32.0 K= 5.60 16.1 22.5 39 32.0 K= 5.60 16.6 22.8 40 32.0 K= 5.60 17.5 23.4 41 32.0 - - - - 29.0 - - - 42 32.0 - - - - 73.6 - - - 43 30.0 - - - - 76.4 - - 44 32.0 - - - - 71.6 - - - 45 30.0 - - - - 72.5 - - - 46 32.0 - - - - 72.1 - - - 47 32.0 - - - - 73.4 - - - 48 32.0 - - - - 73.5 - - - 49 32.0 - - - - 73.5 - - - 50 32.0 - - - - 73.6 - - - 51 32.0 - - - - 73.7 - - - 52 32.0 - - - - 74.0 - - - 53 32.0 - - - - 75.7 - - - 54 30.0 - - - - 76.7 - - - 55 32.0 - - - - 71.7 - - - 56 30.0 - - - - 72.5 - - - 57 32.0 - - - - 72.1 - - - 58 29.0 - - - - 74.6 - - - 59 32.0 - - - - 73.3 60 32.0 - - - - 73.4 - - - 61 29.0 - - - - 74.7 - - - 62 32.0 - - - - 73.4 - - - 63 29.0 - - - - 74.8 - - - 64 32.0 - - - - 73.5 - - - 65 32.0 - - - - 73.5 - - - 66 32.0 - - - - 73.6 - - - 67 29.0 - - - - 74.9 - - - 68 32.0 - - - - 73.6 - - - 69 29.0 - - - - 75.0 - - - 70 32.0 - - - - 73.7 - - - 71 32.0 - - - - 73.7 - - - 72 32.0 - - - - 74.1 - - - 73 32.0 - - - - 75.7 - - - 74 30.0 - - - - 76.6 - - - 75 32.0 - - - - 71.8 - - - 76 30.0 - - - - 72.6 - - - 77 32.0 - - - - 72.1 - - - 78 32.0 - - - - 73.5 - - - 79 32.0 - - - - 74.1 - - - 80 32.0 - - - - 75.7 - - - 81 30.0 - - - - 76.6 - - - 82 32.0 - - - - 71.8 - - - 83 30.0 - - - - 72.6 - - - 84 32.0 - - - - 72.0 - - - 85 32.0 - - - - 73.8 - - - 86 32.0 - - - - 75.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Calc NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 87 30.0 - - - - 76.6 - - - 88 33.5 - - - - 71.1 - - - 89 30.0 - - - - 72.6 - - - 90 33.5 - - - - 71.4 - - - 91 33.5 - - - - 73.3 92 33.5 - - - - 75.0 93 30.0 - - - - 76.6 - - - 94 30.0 - - - - 76.8 - - - 95 30.0 - - - - 78.2 - - - BOR 0.5 - - - - 95.3 UG3 -3.0 - - - - 96.8 - - - UG2 -3.0 - - - - 96.9 BF2 2.0 - - - - 94.7 - - - BF1 2.0 - - - - 98.7 - - - UG1 -3.0 - - - - 100.9 - - - SRC -3.0 SOURCE 100.9 115.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Calc PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 72.9 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 72.5 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 72.5 0.0 0.0 120 FTG 2E PE -1.5 3 33.5 0.0 71.0 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 71.0 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 0.0 71.0 0.0 0.000 TL 2.50 PV Pipe: 4 0.0 1.380 PL 2.21 PF 0.0 4 33.5 0.0 71.0 0.0 0.0 120 FTG ---- PE 0.0 7 33.5 0.0 71.0 0.0 0.000 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 72.9 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 72.5 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 PF 0.0 6 30.0 0.0 72.5 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 71.0 0.0 0.000 TL 13.29 PV Pipe: 7 0.0 1.380 PL 1.75 PF 0.0 7 33.5 0.0 71.0 0.0 0.0 120 FTG ---- FE 0.0 8 33.5 0.0 71.0 0.0 0.000 TL 1.75 PV Pipe: 8 0.0 1.380 PL 4.00 PF 0.0 8 33.5 0.0 71.0 0.0 0.0 120 FTG ---- FE 0.0 9 33.5 0.0 71.0 0.0 0.000 TL 4.00 PV Pipe: 9 0.0 1.380 PL 0.83 PP 0.0 9 33.5 0.0 71.0 0.0 0.0 120 FTG T FE 0.0 10 33.5 0.0 71.0 0.0 0.000 TL 6.83 PV Pipe: 10 8.8 1.380 PL 3.50 PP 0.1 10 33.5 0.0 71.0 0.0 1.9 120 FTG T PE 1.5 11 30.0 0.0 72.4 0.0 0.007 TL 9.50 PV Pipe: 11 -8.8 1.380 PL 3.17 PF 0.1 10 33.5 0.0 71.0 0.0 1.9 120 FTG T PE 0.0 12 33.5 0.0 71.1 0.0 0.007 TL 9.17 PV Pipe: 12 -8.8 1.380 PL 4.00 PP 0.0 12 33.5 0.0 71.1 0.0 1.9 120 FTG ---- PE 0.0 13 33.5 0.0 71.1 0.0 0.007 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building B Calc 3 - 5 Head Corridor Cab PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -8.8 1.380 PL 30.25 PF 0.2 13 33.5 0.0 71.1 0.0 1.9 120 FTG L PE 0.0 14 33.5 0.0 71.3 0.0 0.007 TL 32.25 PV Pipe: 14 -8.8 1.380 PL 10.42 PF 0.1 14 33.5 0.0 71.3 0.0 1.9 120 FTG T PE 0.0 15 33.5 0.0 71.5 0.0 0.007 TL 16.42 PV Pipe: 15 -8.8 1.380 PL 177.46 PF 1.4 15 33.5 0.0 71.5 0.0 1.9 120 FTG 3ET PE 0.0 16 33.5 0.0 72.9 0.0 0.007 TL 192.46 PV Pipe: 16 -8.8 1.380 PL 6.00 PF 0.0 16 33.5 0.0 72.9 0.0 1.9 120 FTG ---- PE 0.0 17 33.5 0.0 72.9 0.0 0.007 TL 6.00 PV Pipe: 17 -8.8 1.380 PL 6.00 PF 0.0 17 33.5 0.0 72.9 0.0 1.9 120 FTG ---- PE 0.0 18 33.5 0.0 73.0 0.0 0.007 TL 6.00 PV Pipe: 18 -8.8 1.380 PL 6.00 PP 0.0 18 33.5 0.0 73.0 0.0 1.9 120 FTG ---- PE 0.0 19 33.5 0.0 73.0 0.0 0.007 TL 6.00 PV Pipe: 19 -8.8 1.380 PL 6.00 PF 0.0 19 33.5 0.0 73.0 0.0 1.9 120 FTG ---- PE 0.0 20 33.5 0.0 73.1 0.0 0.007 TL 6.00 PV Pipe: 20 -8.8 1.380 PL 26.42 PF 0.2 20 33.5 0.0 73.1 0.0 1.9 120 FTG 2E PE 0.0 21 33.5 0.0 73.3 0.0 0.007 TL 32.42 PV Pipe: 21 -8.8 1.380 PL 189.96 PP 1.5 21 33.5 0.0 73.3 0.0 1.9 120 FTG 4ET PE 0.0 22 33.5 0.0 74.9 0.0 0.007 TL 207.96 _PV Pipe: 22 -8.8 1.380 PL 3.50 PF 0.1 22 33.5 0.0 74.9 0.0 1.9 120 FTG T FE 1.5 23 30.0 0.0 76.4 0.0 0.007 TL 9.50 PV Pipe: 23 0.0 1.049 PL 35.00 PP 0.0 24 29.0 0.0 71.0 0.0 0.0 120 FTG ---- FE -0.4 25 30.0 0.0 70.5 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 PF 0.0 25 30.0 0.0 70.5 0.0 0.0 120 FTG ---- PE 0.0 27 30.0 0.0 70.5 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 PL 35.00 PF 0.0 26 29.0 0.0 71.0 0.0 0.0 120 FTG ---- FE -0.4 27 30.0 0.0 70.5 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.380 FL 3.50 PF 0.0 27 30.0 0.0 70.5 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 70.5 0.0 0.000 TL 3.50 PV Pipe: 27 0.0 1.049 FL 35.00 PF 0.0 28 29.0 0.0 71.0 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 70.5 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 70.5 0.0 0.0 120 FTG 2E FE -0.9 30 32.0 0.0 69.7 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PF 0.0 30 32.0 0.0 69.7 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 69.7 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PF 0.0 31 32.0 0.0 69.7 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 69.7 0.0 0.000 TL 6.96 PV Pipe: 31 -56.9 1.380 PL 2.00 PF 1.9 32 32.0 0.0 69.7 0.0 12.2 120 FTG T FE 0.9 33 30.0 0.0 72.4 0.0 0.237 TL 8.00 PV Pipe: 32 56.9 1.380 PL 47.58 FE' 13.2 32 32.0 0.0 69.7 0.0 12.2 120 FTG TL PE 0.0 34 32.0 0.0 56.5 0.0 0.237 TL 55.58 PV Pipe: 33 56.9 1.380 PL 138.50 PF 34.9 34 32.0 0.0 56.5 0.0 12.2 120 FTG 3E PE 0.0 35 32.0 0.0 21.6 0.0 0.237 TL 147.50 PV Pipe: 34 56.9 1.380 PL 14.00 PF 4.0 35 32.0 0.0 21.6 0.0 12.2 120 FTG E PE 0.0 36 32.0 5.6 17.5 23.5 0.237 TL 17.00 PV Pipe: 35 33.5 1.380 FL 10.00 PF 0.9 36 32.0 5.6 17.5 23.5 7.2 120 FTG ---- PE 0.0 37 32.0 5.6 16.7 22.9 0.089 TL 10.00 PV Pipe: 36 10.6 1.380 FL 8.00 PF 0.1 37 32.0 5.6 16.7 22.9 2.3 120 FTG ---- PE 0.0 39 32.0 5.6 16.6 22.8 0.011 TL 8.00 PV Pipe: 37 -22.5 1.380 PL 10.00 PF 0.4 38 32.0 5.6 16.1 22.5 4.8 120 FTG ---- FE 0.0 39 32.0 5.6 16.6 22.8 0.043 TL 10.00 PV Pipe: 38 -34.7 1.380 PL 10.00 FE' 0.9 39 32.0 5.6 16.6 22.8 7.4 120 FTG ---- FE 0.0 40 32.0 5.6 17.5 23.4 0.095 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building H Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GEM) FL/FT (PSI) Pipe: 39 -58.1 1.380 EL 34.67 PP 11.5 40 32.0 5.6 17.5 23.4 12.5 120 FTG 4E PE 0.0 41 32.0 0.0 29.0 0.0 0.246 TL 46.67 PV Pipe: 40 -58.1 1.380 PL 175.12 PF 44.6 41 32.0 0.0 29.0 0.0 12.5 120 FTG T PE 0.0 42 32.0 0.0 73.6 0.0 0.246 TL 181.12 PV Pipe: 41 -58.1 1.380 PL 2.00 PP 2.0 42 32.0 0.0 73.6 0.0 12.5 120 FTG T PE 0.9 43 30.0 0.0 76.4 0.0 0.246 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 71.6 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 72.5 0.0 0.000 TL 8.00 PV Pipe: 43 -9.7 1.380 FL 41.25 PF 0.4 45 30.0 0.0 72.5 0.0 2.1 120 FTG TL PE -0.9 46 32.0 0.0 72.1 0.0 0.009 TL 49.25 PV Pipe: 44 -9.7 1.380 PL 145.04 PF 1.3 46 32.0 0.0 72.1 0.0 2.1 120 FTG ---- PH 0.0 47 32.0 0.0 73.4 0.0 0.009 TL 145.04 PV Pipe: 45 -9.7 1.380 EL 10.00 PF 0.1 47 32.0 0.0 73.4 0.0 2.1 120 FTG ---- PH 0.0 48 32.0 0.0 73.5 0.0 0.009 TL 10.00 PV Pipe: 46 -9.7 1.380 EL 8.00 PP 0.1 48 32.0 0.0 73.5 0.0 2.1 120 FTG ---- FE 0.0 49 32.0 0.0 73.5 0.0 0.009 TL 8.00 PV Pipe: 47 -9.7 1.380 FL 10.00 PP 0.1 49 32.0 0.0 73.5 0.0 2.1 120 FTG ---- PH 0.0 50 32.0 0.0 73.6 0.0 0.009 TL 10.00 PV Pipe: 48 -9.7 1.380 PL 10.00 PP 0.1 50 32.0 0.0 73.6 0.0 2.1 120 FTG ---- PE 0.0 51 32.0 0.0 73.7 0.0 0.009 TL 10.00 PV Pipe: 49 -9.7 1.380 PL 27.96 PF 0.3 51 32.0 0.0 73.7 0.0 2.1 120 FTG 2E PE 0.0 52 32.0 0.0 74.0 0.0 0.009 TL 33.96 PV Pipe: 50 -9.7 1.380 FL 182.33 PF 1.7 52 32.0 0.0 74.0 0.0 2.1 120 FTG T PH 0.0 53 32.0 0.0 75.7 0.0 0.009 TL 188.33 PV Pipe: 51 -9.7 1.380 FL 2.00 PP 0.1 53 32.0 0.0 75.7 0.0 2.1 120 FTG T PH 0.9 54 30.0 0.0 76.7 0.0 0.009 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 9.7 1.380 PL 2.00 PF 0.1 55 32.0 0.0 71.7 0.0 2.1 120 FTG T PE 0.9 56 30.0 0.0 72.5 0.0 0.009 TL 8.00 PV Pipe: 53 -9.7 1.380 PL 38.17 PF 0.4 55 32.0 0.0 71.7 0.0 2.1 120 FTG L PE 0.0 57 32.0 0.0 72.1 0.0 0.009 TL 40.17 PV Pipe: 54 -9.7 1.380 FL 134.70 PF 1.2 57 32.0 0.0 72.1 0.0 2.1 120 FTG ---- PE 0.0 59 32.0 0.0 73.3 0.0 0.009 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 74.6 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 73.3 0.0 0.000 TL 35.00 PV Pipe: 56 -9.7 1.380 PL 12.50 PF 0.1 59 32.0 0.0 73.3 0.0 2.1 120 FTG ---- FE 0.0 60 32.0 0.0 73.4 0.0 0.009 TL 12.50 PV Pipe: 57 -9.7 1.380 FL 1.83 PF 0.0 60 32.0 0.0 73.4 0.0 2.1 120 FTG ---- PE 0.0 62 32.0 0.0 73.4 0.0 0.009 TL 1.83 PV Pipe: 58 0.0 1.049 FL 35.00 PF 0.0 61 29.0 0.0 74.7 0.0 0.0 120 FTG ---- FE -1.3 62 32.0 0.0 73.4 0.0 0.000 TL 35.00 PV Pipe: 59 -9.7 1.380 FL 925 PF 0.1 62 32.0 0.0 73.4 0.0 2.1 120 FTG ---- PE 0.0 64 32.0 0.0 73.5 0.0 0.009 TL 9.25 PV Pipe: 60 0.0 1.049 FL 35.00 PF 0.0 63 29.0 0.0 74.8 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 73.5 0.0 0.000 TL 35.00 PV Pipe: 61 -9.7 1.380 FL 0.92 PF 0.0 64 32.0 0.0 73.5 0.0 2.1 120 FTG ---- FE 0.0 65 32.0 0.0 73.5 0.0 0.009 TL 0.92 PV Pipe: 62 -9.7 1.380 FL 12.00 PF 0.1 65 32.0 0.0 73.5 0.0 2.1 120 FTG ---- PE 0.0 66 32.0 0.0 73.6 0.0 0.009 TL 12.00 PV Pipe: 63 -9.7 1.380 PL 1.42 PF 0.0 66 32.0 0.0 73.6 0.0 2.1 120 FTG ---- FE 0.0 68 32.0 0.0 73.6 0.0 0.009 TL 1.42 PV Pipe: 64 0.0 1.049 FL 35.00 PF 0.0 67 29.0 0.0 74.9 0.0 0.0 120 FTG ---- PE -1.3 68 32.0 0.0 73.6 0.0 0.000 TL 35.00 PV 4 p SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -9.7 1.380 PL 9.17 PF 0.1 68 32.0 0.0 73.6 0.0 2.1 120 FTG ---- PE 0.0 70 32.0 0.0 73.7 0.0 0.009 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 75.0 0.0 0.0 120 FTG ---- PE -1.3 70 32.0 0.0 73.7 0.0 0.000 TL 35.00 PV Pipe: 67 -9.7 1.380 PL 1.25 PP 0.0 70 32.0 0.0 73.7 0.0 2.1 120 FTG ---- PE 0.0 71 32.0 0.0 73.7 0.0 0.009 TL 1.25 PV Pipe: 68 -9.7 1.380 PL 30.80 PP 0.4 71 32.0 0.0 73.7 0.0 2.1 120 FTG ET PE 0.0 72 32.0 0.0 74.1 0.0 0.009 TL 39.80 PV Pipe: 69 -9.7 1.380 PL 175.00 PP 1.6 72 32.0 0.0 74.1 0.0 2.1 120 FTG T PE 0.0 73 32.0 0.0 75.7 0.0 0.009 TL 181.00 PV Pipe: 70 -9.7 1.380 PL 2.00 PP 0.1 73 32.0 0.0 75.7 0.0 2.1 120 FTG T PE 0.9 74 30.0 0.0 76.6 0.0 0.009 TL 8.00 PV Pipe: 71 9.6 1.380 PL 2.00 PP 0.1 75 32.0 0.0 71.8 0.0 2.1 120 FTG T PE 0.9 76 30.0 0.0 72.6 0.0 0.009 TL 8.00 PV Pipe: 72 -9.6 1.380 PL 38.25 PP 0.4 75 32.0 0.0 71.8 0.0 2.1 120 FTG L PE 0.0 77 32.0 0.0 72.1 0.0 0.009 TL 40.25 PV Pipe: 73 -9.6 1.380 PL 150.42 PP 1.3 77 32.0 0.0 72.1 0.0 2.1 120 FTG ---- PE 0.0 78 32.0 0.0 73.5 0.0 0.009 TL 150.42 PV Pipe: 74 -9.6 1.380 PL 65.83 PP 0.6 78 32.0 0.0 73.5 0.0 2.1 120 FTG 2E PE 0.0 79 32.0 0.0 74.1 0.0 0.009 TL 71.83 PV Pipe: 75 -9.6 1.380 PL 170.83 PP 1.6 79 32.0 0.0 74.1 0.0 2.1 120 FTG T PE 0.0 80 32.0 0.0 75.7 0.0 0.009 TL 176.83 PV Pipe: 76 -9.6 1.380 PL 2.00 PP 0.1 80 32.0 0.0 75.7 0.0 2.1 120 FTG T PE 0.9 81 30.0 0.0 76.6 0.0 0.009 TL 8.00 PV Pipe: 77 9.7 1.380 PL 2.00 PP 0.1 82 32.0 0.0 71.8 0.0 2.1 120 FTG T PE 0.9 83 30.0 0.0 72.6 0.0 0.009 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Calc PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -9.7 1.380 PL 24.58 PP 0.2 82 32.0 0.0 71.8 0.0 2.1 120 FTG L PE 0.0 84 32.0 0.0 72.0 0.0 0.009 TL 26.58 PV Pipe: 79 -9.7 1.380 FL 190.50 PF 1.8 84 32.0 0.0 72.0 0.0 2.1 120 FTG 4E FE 0.0 85 32.0 0.0 73.8 0.0 0.009 TL 202.50 PV Pipe: 80 -9.7 1.380 FL 196.21 PP 1.8 85 32.0 0.0 73.8 0.0 2.1 120 FTG T FE 0.0 86 32.0 0.0 75.7 0.0 0.009 TL 202.21 PV Pipe: 81 -9.7 1.380 FL 2.00 PP 0.1 86 32.0 0.0 75.7 0.0 2.1 120 FTG T PE 0.9 87 30.0 0.0 76.6 0.0 0.009 TL 8.00 PV Pipe: 82 9.4 1.380 PL 3.50 PP 0.1 88 33.5 0.0 71.1 0.0 2.0 120 FTG T PE 1.5 89 30.0 0.0 72.6 0.0 0.009 TL 9.50 PV Pipe: 83 -9.4 1.380 FL 33.58 PF 0.3 88 33.5 0.0 71.1 0.0 2.0 120 FTG L PE 0.0 90 33.5 0.0 71.4 0.0 0.009 TL 35.58 PV Pipe: 84 -9.4 1.380 PL 202.38 PF 1.9 90 33.5 0.0 71.4 0.0 2.0 120 FTG 3ET PE 0.0 91 33.5 0.0 73.3 0.0 0.009 TL 217.38 PV Pipe: 85 -9.4 1.380 PL 193.96 PF 1.7 91 33.5 0.0 73.3 0.0 2.0 120 FTG T FE 0.0 92 33.5 0.0 75.0 0.0 0.009 TL 199.96 PV Pipe: 86 -9.4 1.380 PL 3.50 PF 0.1 92 33.5 0.0 75.0 0.0 2.0 120 FTG T FE 1.5 93 30.0 0.0 76.6 0.0 0.009 TL 9.50 PV Pipe: 87 8.8 2.635 PL 3.00 PF 0.0 11 30.0 0.0 72.4 0.0 0.5 120 FTG ---- FE 0.0 33 30.0 0.0 72.4 0.0 0.000 TL 3.00 PV Pipe: 88 -48.2 2.635 PL 8.50 PP 0.1 33 30.0 0.0 72.4 0.0 2.8 120 FTG ---- PE 0.0 45 30.0 0.0 72.5 0.0 0.007 TL 8.50 PV Pipe: 89 -38.4 2.635 PL 6.92 PF 0.0 45 30.0 0.0 72.5 0.0 2.3 120 FTG ---- FE 0.0 56 30.0 0.0 72.5 0.0 0.005 TL 6.92 PV Pipe: 90 -28.8 2.635 PL 7.42 PF 0.0 56 30.0 0.0 72.5 0.0 1.7 120 FTG ---- PE 0.0 76 30.0 0.0 72.6 0.0 0.003 TL 7.42 PV k SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Cab 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -19.1 2.635 PL 7.00 PF 0.0 76 30.0 0.0 72.6 0.0 1.1 120 FTG ---- PE 0.0 83 30.0 0.0 72.6 0.0 0.001 TL 7.00 PV Pipe: 92 -9.4 2.635 PL 3.92 PF 0.0 83 30.0 0.0 72.6 0.0 0.6 120 FTG ---- PE 0.0 89 30.0 0.0 72.6 0.0 0.000 TL 3.92 PV Pipe: 93 -8.8 2.635 PL 5.54 PF 0.0 23 30.0 0.0 76.4 0.0 0.5 120 FTG ---- PE 0.0 43 30.0 0.0 76.4 0.0 0.000 TL 5.54 PV Pipe: 94 -66.9 2.635 PL 8.96 PF 0.4 43 30.0 0.0 76.4 0.0 3.9 120 FTG T PE 0.0 94 30.0 0.0 76.8 0.0 0.014 TL 25.96 PV Pipe: 95 -9.4 2.635 PL 5.40 PF 0.0 93 30.0 0.0 76.6 0.0 0.6 120 FTG ---- PE 0.0 87 30.0 0.0 76.6 0.0 0.000 TL 5.40 PV Pipe: 96 -19.1 2.635 PL 9.50 PF 0.0 87 30.0 0.0 76.6 0.0 1.1 120 FTG ---- PE 0.0 81 30.0 0.0 76.6 0.0 0.001 TL 9.50 PV Pipe: 97 -28.8 2.635 PL 8.17 PF 0.0 81 30.0 0.0 76.6 0.0 1.7 120 FTG ---- PE 0.0 74 30.0 0.0 76.6 0.0 0.003 TL 8.17 PV Pipe: 98 -38.4 2.635 PL 7.96 PF 0.0 74 30.0 0.0 76.6 0.0 2.3 120 FTG ---- PE 0.0 54 30.0 0.0 76.7 0.0 0.005 TL 7.96 PV Pipe: 99 -48.2 2.635 PL 1.04 PF 0.1 54 30.0 0.0 76.7 0.0 2.8 120 FTG T PE 0.0 94 30.0 0.0 76.8 0.0 0.007 TL 18.04 PV Pipe: 100 -115.0 2.635 PL 20.38 PF 1.4 94 30.0 0.0 76.8 0.0 6.8 120 FTG 2E PE 0.0 95 30.0 0.0 78.2 0.0 0.037 TL 36.38 PV Pipe: 101 -115.0 2.635 PL 75.50 FE' 4.3 95 30.0 0.0 78.2 0.0 6.8 120 FTG 5E PE 12.8 BOR 0.5 0.0 95.3 0.0 0.037 TL 115.50 PV Pipe: 102 -115.0 6.280 PL 10.00 PF 0.0 BOR 0.5 0.0 95.3 0.0 1.2 140 FTG E PE 1.5 UG3 -3.0 0.0 96.8 0.0 0.000 TL 32.00 PV Pipe: 103 -115.0 6.080 PL 142.00 PF 0.1 UG3 -3.0 0.0 96.8 0.0 1.3 150 FTG 3E PE 0.0 UG2 -3.0 0.0 96.9 0.0 0.000 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Calc 3 - 5 Head Corridor Caic PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -115.0 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 96.9 0.0 1.2 140 FTG ET PE -2.2 BF2 2.0 0.0 94.7 0.0 0.000 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 98.7 0.0 4.0 psi, 115.0 gpm BF2 2.0 0.0 94.7 0.0 Pipe: 106 -115.0 6.280 PL 5.00 PF 0.0 BF1 2.0 0.0 98.7 0.0 1.2 140 FTG 2E PE 2.2 UG1 -3.0 0.0 100.9 0.0 0.000 TL 49.00 PV Pipe: 107 -115.0 6.080 PL 16.00 PF 0.0 UG1 -3.0 0.0 100.9 0.0 1.3 150 FTG TG PE 0.0 SRC -3.0 SRCE 100.9 (N/A) 0.000 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.080 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.5 ft/sec at pipe 41. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.84 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Caic PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyVlv GatVlv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngE1l ChkVlv BfyVlv GatVlv AimChk DPViv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEli ChkViv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEil ChkViv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 t1 H 0 t1 Qj N) ocr) 0 (I) Cu Ct IXjU) (D t1F-1 oz c tri H Cl) aCi)C/) 0 CJ)CJ) iQ triL1 Cl) - x Cl) (-I) woo c-) (fI— :xz o Cl 01 (D Ci) Cl) OHH o II a ti oz II Cn 0 0 cli 00 160.0 1 140.0 G A U120 . 0 G E P100.0 2 R E S S 80.0 U R E p S i 40.0 20.0 MW WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) thed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 3.SDF JOB TITLE: La Costa Glen Building E Caic 3 - 5 Head Corridor Calc WATER SUPPLY CURVE I \\\\\\\\\\\\\\\\\\\\\\\\\\ 149.0 psi 8 1790 gpm-> * I Flow Test Point 143+ 130+ 117+ P104+ R IX E S 5 91+ U I R I E I 78+ P I S I I 65+ 52+ 39+ 26+ LEGEND 'I I X = Required Water Supply 100.95 psi 8 215.0 gpm 13+ I 0 = Available Water Supply 154.88 psi 8 215.0 gpm 7 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 155.0 149.0 1790.0 AVAIL. TOTAL REQ'D PRESS. 8 DEMAND PRESS. (PSI) (GPM) (PSI) 154.9 229.3 71.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 229.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 129.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 - - - - 21.9 - - - 2 30.0 - - - - 21.4 - - - 3 33.5 - - - - 19.9 - - - 4 33.5 K= 5.60 19.9 25.0 5 29.0 - - - - 22.0 - - - 6 30.0 - - - - 21.6 - - - 7 33.5 - - - - 20.0 8 33.5 K= 5.60 20.1 25.1 9 33.5 K= 5.60 20.9 25.6 10 33.5 - - - - 23.6 - - - 11 30.0 - - - - 32.4 - - - 12 33.5 K= 5.60 22.9 26.8 13 33.5 K= 5.60 22.9 26.8 14 33.5 - - - - 24.3 - - - 15 33.5 - - - - 24.9 - - - 16 33.5 - - - - 33.0 - - - 17 33.5 - - - - 33.3 18 33.5 - - - - 33.5 19 33.5 - - - - 33.8 - - - 20 33.5 - - - - 34.0 - - - 21 33.5 - - - - 35.4 - - - 22 33.5 - - - - 44.1 - - - 23 30.0 - - - - 46.0 - - - 24 29.0 - - - - 33.1 - - - 25 30.0 - - - - 32.7 - - - 26 29.0 - - - - 33.1 - - 27 30.0 - - - - 32.7 - - - 28 29.0 - - - - 33.1 - - - 29 30.0 - - - - 32.7 - - - 30 32.0 - - - - 31.8 - - - 31 32.0 - - - - 31.8 - - - 32 32.0 - - - - 31.8 - - - 33 30.0 - - - - 32.5 - - - 34 32.0 - - - - 33.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALO 4.SDF JOB TITLE: La Costa Glen Building E Cab 4 - SD1 Heads NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 37.4 - - - 36 32.0 - - - - 37.9 - - - 37 32.0 - - - - 38.2 - - - 38 32.0 - - - - 38.4 - - - 39 32.0 - - - - 38.4 - - - 40 32.0 - - - - 38.7 - - - 41 32.0 - - - - 39.9 - - - 42 32.0 - - - - 44.9 - - - 43 30.0 - - - - 46.0 - - - 44 32.0 - - - - 31.8 - - - 45 30.0 - - - - 32.7 - - - 46 32.0 - - - - 33.2 - - - 47 32.0 - - - - 37.3 48 32.0 - - - - 37.6 - - - 49 32.0 - - - - 37.8 - - - 50 32.0 - - - - 38.1 - - - 51 32.0 - - - - 38.4 - - - 52 32.0 - - - - 39.3 - - - 53 32.0 - - - - 44.6 - - - 54 30.0 - - - - 45.7 - - - 55 32.0 - - - - 32.1 56 30.0 - - - - 32.8 - - - 57 32.0 - - - - 33.3 58 29.0 - - - - 38.3 - - - 59 32.0 - - - - 37.0 - - - 60 32.0 - - - - 37.4 - - - 61 29.0 - - - - 38.7 - - - 62 32.0 - - - - 37.4 63 29.0 - - - - 39.0 - - - 64 32.0 - - - - 37.7 - - - 65 32.0 - - - - 37.7 - - - 66 32.0 - - - - 38.0 - - - 67 29.0 - - - - 39.4 - - - 68 32.0 - - - - 38.1 - - - 69 29.0 - - - - 39.6 - - - 70 32.0 - - - - 38.3 - - - 71 32.0 - - - - 38.4 - - - 72 32.0 - - - - 39.5 - - - 73 32.0 - - - - 44.5 - - - 74 30.0 - - - - 45.6 - - - 75 32.0 - - - - 32.2 76 30.0 - - - - 32.9 - - - 77 32.0 - - - - 33.3 - - - 78 32.0 - - - - 37.5 - - - 79 32.0 - - - - 39.5 - - - 80 32.0 - - - - 44.4 - - - 81 30.0 - - - - 45.5 - - - 82 32.0 - - - - 32.2 - - - 83 30.0 - - - - 32.9 - - - 84 32.0 - - - - 33.0 - - - 85 32.0 - - - - 38.7 - - - 86 32.0 - - - - 44.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 87 30.0 - - - - 45.5 - - - 88 33.5 - - - - 31.6 - - - 89 30.0 - - - - 32.9 - - - 90 33.5 - - - - 32.6 - - - 91 33.5 - - - - 38.4 - - - 92 33.5 - - - - 43.7 - - - 93 30.0 - - - - 45.5 - - - 94 30.0 - - - - 46.1 - - - 95 30.0 - - - - 47.8 - - - BOR 0.5 - - - - 66.0 - - - UG3 -3.0 - - - - 67.5 UG2 -3.0 - - - - 67.6 BF2 2.0 - - - - 65.5 BF1 2.0 - - - - 69.5 - - - UG1 -3.0 - - - - 71.7 - - - SRC -3.0 SOURCE 71.7 129.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.049 PL 35.00 PF 0.0 1 29.0 0.0 21.9 0.0 0.0 120 FTG ---- PE -0.4 2 30.0 0.0 21.4 0.0 0.000 TL 35.00 PV Pipe: 2 0.0 1.380 PL 5.00 PF 0.0 2 30.0 0.0 21.4 0.0 0.0 120 FTG 2E FE -1.5 3 33.5 0.0 19.9 0.0 0.000 TL 11.00 PV Pipe: 3 0.0 1.380 PL 2.50 PF 0.0 3 33.5 0.0 19.9 0.0 0.0 120 FTG ---- PE 0.0 4 33.5 5.6 19.9 25.0 0.000 TL 2.50 PV Pipe: 4 -25.0 1.380 FL 2.21 PF 0.1 4 33.5 5.6 19.9 25.0 5.4 120 FTG ---- PE 0.0 7 33.5 0.0 20.0 0.0 0.052 TL 2.21 PV Pipe: 5 0.0 1.049 FL 35.00 PF 0.0 5 29.0 0.0 22.0 0.0 0.0 120 FTG ---- FE -0.4 6 30.0 0.0 21.6 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 FL 4.29 PF 0.0 6 30.0 0.0 21.6 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 20.0 0.0 0.000 TL 13.29 PV Pipe: 7 -25.0 1.380 FL 1.75 PF 0.1 7 33.5 0.0 20.0 0.0 5.4 120 FTG ---- FE 0.0 8 33.5 5.6 20.1 25.1 0.052 TL 1.75 PV Pipe: 8 -50.1 1.380 FL 4.00 PF 0.7 8 33.5 5.6 20.1 25.1 10.8 120 FTG ---- FE 0.0 9 33.5 5.6 20.9 25.6 0.187 TL 4.00 PV Pipe: 9 -75.7 1.380 FL 0.83 PF 2.7 9 33.5 5.6 20.9 25.6 16.2 120 FTG T FE 0.0 10 33.5 0.0 23.6 0.0 0.402 TL 6.83 PV Pipe: 10 -107.0 1.380 FL 3.50 PF 7.2 10 33.5 0.0 23.6 0.0 23.0 120 FTG T PE 1.5 11 30.0 0.0 32.4 0.0 0.762 TL 9.50 PV Pipe: 11 31.3 1.380 FL 3.17 PF 0.7 10 33.5 0.0 23.6 0.0 6.7 120 FTG T FE 0.0 12 33.5 5.6 22.9 26.8 0.078 TL 9.17 PV Pipe: 12 4.5 1.380 FL 4.00 PF 0.0 12 33.5 5.6 22.9 26.8 1.0 120 FTG ---- FE 0.0 13 33.5 5.6 22.9 26.8 0.002 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -22.3 1.380 PL 30.25 PF 1.4 13 33.5 5.6 22.9 26.8 4.8 120 FTG L PE 0.0 14 33.5 0.0 24.3 0.0 0.042 TL 32.25 PV Pipe: 14 -22.3 1.380 FL 10.42 PF 0.7 14 33.5 0.0 24.3 0.0 4.8 120 FTG T PE 0.0 15 33.5 0.0 24.9 0.0 0.042 TL 16.42 PV Pipe: 15 -22.3 1.380 PL 177.46 PF 8.1 15 33.5 0.0 24.9 0.0 4.8 120 FTG 3ET PE 0.0 16 33.5 0.0 33.0 0.0 0.042 TL 192.46 PV Pipe: 16 -22.3 1.380 FL 6.00 FE' 0.3 16 33.5 0.0 33.0 0.0 4.8 120 FTG ---- FE 0.0 17 33.5 0.0 33.3 0.0 0.042 TL 6.00 PV Pipe: 17 -22.3 1.380 PL 6.00 PF 0.3 17 33.5 0.0 33.3 0.0 4.8 120 FTG ---- PE 0.0 18 33.5 0.0 33.5 0.0 0.042 TL 6.00 PV Pipe: 18 -22.3 1.380 PL 6.00 PF 0.3 18 33.5 0.0 33.5 0.0 4.8 120 FTG ---- PE 0.0 19 33.5 0.0 33.8 0.0 0.042 TL 6.00 PV Pipe: 19 -22.3 1.380 PL 6.00 PF 0.3 19 33.5 0.0 33.8 0.0 4.8 120 FTG ---- FE 0.0 20 33.5 0.0 34.0 0.0 0.042 TL 6.00 PV Pipe: 20 -22.3 1.380 PL 26.42 FE' 1.4 20 33.5 0.0 34.0 0.0 4.8 120 FTG 2E PE 0.0 21 33.5 0.0 35.4 0.0 0.042 TL 32.42 PV Pipe: 21 -22.3 1.380 FL 189.96 PF 8.7 21 33.5 0.0 35.4 0.0 4.8 120 FTG 4ET PE 0.0 22 33.5 0.0 44.1 0.0 0.042 TL 207.96 PV Pipe: 22 -22.3 1.380 FL 3.50 PF 0.4 22 33.5 0.0 44.1 0.0 4.8 120 FTG T FE 1.5 23 30.0 0.0 46.0 0.0 0.042 TL 9.50 PV Pipe: 23 0.0 1.049 FL 35.00 FE' 0.0 24 29.0 0.0 33.1 0.0 0.0 120 FTG ---- FE -0.4 25 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV Pipe: 24 0.0 1.380 PL 2.75 FE' 0.0 25 30.0 0.0 32.7 0.0 0.0 120 FTG ---- FE 0.0 27 30.0 0.0 32.7 0.0 0.000 TL 2.75 PV Pipe: 25 0.0 1.049 FL 35.00 PF 0.0 26 29.0 0.0 33.1 0.0 0.0 120 FTG ---- FE -0.4 27 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GPAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.380 PL 3.50 PF 0.0 27 30.0 0.0 32.7 0.0 0.0 120 FTG ---- PE 0.0 29 30.0 0.0 32.7 0.0 0.000 TL 3.50 PV Pipe: 27 0.0 1.049 PL 35.00 PF 0.0 28 29.0 0.0 33.1 0.0 0.0 120 FTG ---- PE -0.4 29 30.0 0.0 32.7 0.0 0.000 TL 35.00 PV Pipe: 28 0.0 1.380 PL 8.12 PF 0.0 29 30.0 0.0 32.7 0.0 0.0 120 FTG 2E PE -0.9 30 32.0 0.0 31.8 0.0 0.000 TL 14.12 PV Pipe: 29 0.0 1.380 PL 8.00 PP 0.0 30 32.0 0.0 31.8 0.0 0.0 120 FTG ---- PE 0.0 31 32.0 0.0 31.8 0.0 0.000 TL 8.00 PV Pipe: 30 0.0 1.380 PL 0.96 PF 0.0 31 32.0 0.0 31.8 0.0 0.0 120 FTG T PE 0.0 32 32.0 0.0 31.8 0.0 0.000 TL 6.96 PV Pipe: 31 17.8 1.380 PL 2.00 PF 0.2 32 32.0 0.0 31.8 0.0 3.8 120 FTG T PE 0.9 33 30.0 0.0 32.5 0.0 0.027 TL 8.00 PV Pipe: 32 -17.8 1.380 PL 47.58 PF 1.5 32 32.0 0.0 31.8 0.0 3.8 120 FTG TL PE 0.0 34 32.0 0.0 33.4 0.0 0.027 TL 55.58 PV Pipe: 33 -17.8 1.380 PL 138.50 PF 4.1 34 32.0 0.0 33.4 0.0 3.8 120 FTG 3E PE 0.0 35 32.0 0.0 37.4 0.0 0.027 TL 147.50 PV Pipe: 34 -17.8 1.380 PL 14.00 PF 0.5 35 32.0 0.0 37.4 0.0 3.8 120 FTG E PE 0.0 36 32.0 0.0 37.9 0.0 0.027 TL 17.00 PV Pipe: 35 -17.8 1.380 PL 10.00 PF 0.3 36 32.0 0.0 37.9 0.0 3.8 120 FTG ---- PE 0.0 37 32.0 0.0 38.2 0.0 0.027 TL 10.00 PV Pipe: 36 -17.8 1.380 PL 8.00 PP 0.2 37 32.0 0.0 38.2 0.0 3.8 120 FTG ---- PE 0.0 39 32.0 0.0 38.4 0.0 0.027 TL 8.00 PV Pipe: 37 0.0 1.380 PL 10.00 PP 0.0 38 32.0 0.0 38.4 0.0 0.0 120 FTG ---- SE 0.0 39 32.0 0.0 38.4 0.0 0.000 TL 10.00 PV Pipe: 38 -17.8 1.380 PL 10.00 PF 0.3 39 32.0 0.0 38.4 0.0 3.8 120 FTG ---- PE 0.0 40 32.0 0.0 38.7 0.0 0.027 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/201EGRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Cab 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -17.8 1.380 PL 34.67 PF 1.3 40 32.0 0.0 38.7 0.0 3.8 120 FTG 4E PE 0.0 41 32.0 0.0 39.9 0.0 0.027 TL 46.67 PV Pipe: 40 -17.8 1.380.PL 175.12 PF 5.0 41 32.0 0.0 39.9 0.0 3.8 120 FTG T PE 0.0 42 32.0 0.0 44.9 0.0 0.027 TL 181.12 PV Pipe: 41 -17.8 1.380 PL 2.00 PP 0.2 42 32.0 0.0 44.9 0.0 3.8 120 FTG T PE 0.9 43 30.0 0.0 46.0 0.0 0.027 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PP 0.0 44 32.0 0.0 31.8 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 32.7 0.0 0.000 TL 8.00 PV Pipe: 43 -18.0 1.380 PL 41.25 PF 1.4 45 30.0 0.0 32.7 0.0 3.9 120 FTG TL PH -0.9 46 32.0 0.0 33.2 0.0 0.028 TL 49.25 PV Pipe: 44 -18.0 1.380 PL 145.04 PF 4.1 46 32.0 0.0 33.2 0.0 3.9 120 FTG ---- PE 0.0 47 32.0 0.0 37.3 0.0 0.028 TL 145.04 PV Pipe: 45 -18.0 1.380 PL 10.00 PP 0.3 47 32.0 0.0 37.3 0.0 3.9 120 FTG ---- PE 0.0 48 32.0 0.0 37.6 0.0 0.028 TL 10.00 PV Pipe: 46 -18.0 1.380 PL 8.00 PF 0.2 48 32.0 0.0 37.6 0.0 3.9 120 FTG ---- PE 0.0 49 32.0 0.0 37.8 0.0 0.028 TL 8.00 PV Pipe: 47 -18.0 1.380 PL 10.00 PP 0.3 49 32.0 0.0 37.8 0.0 3.9 120 FTG ---- PE 0.0 50 32.0 0.0 38.1 0.0 0.028 TL 10.00 PV Pipe: 48 -18.0 1.380 PL 10.00 PP 0.3 50 32.0 0.0 38.1 0.0 3.9 120 FTG ---- PE 0.0 51 32.0 0.0 38.4 0.0 0.028 TL 10.00 PV Pipe: 49 -18.0 1.380 PL 27.96 PP 1.0 51 32.0 0.0 38.4 0.0 3.9 120 FTG 2E PE 0.0 52 32.0 0.0 39.3 0.0 0.028 TL 33.96 PV Pipe: 50 -18.0 1.380 PL 182.33 PF 5.3 52 32.0 0.0 39.3 0.0 3.9 120 FTG T PE 0.0 53 32.0 0.0 44.6 0.0 0.028 TL 188.33 PV Pipe.: 51 -18.0 1.380 PL 2.00 PF 0.2 53 32.0 0.0 44.6 0.0 3.9 120 FTG T PE 0.9 54 30.0 0.0 45.7 0.0 0.028 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 17.9 1.380 FL 2.00 PF 0.2 55 32.0 0.0 32.1 0.0 3.8 120 FTG T FE 0.9 56 30.0 0.0 32.8 0.0 0.028 TL 8.00 PV Pipe: 53 -17.9 1.380 FL 38.17 FE' 1.1 55 32.0 0.0 32.1 0.0 3.8 120 FTG L FE 0.0 57 32.0 0.0 33.3 0.0 0.028 TL 40.17 PV Pipe: 54 -17.9 1.380 PL 134.70 PF 3.7 57 32.0 0.0 33.3 0.0 3.8 120 FTG ---- PE 0.0 59 32.0 0.0 37.0 0.0 0.028 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PP 0.0 58 29.0 0.0 38.3 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 37.0 0.0 0.000 TL 35.00 PV Pipe: 56 -17.9 1.380 FL 12.50 PF 0.3 59 32.0 0.0 37.0 0.0 3.8 120 FTG ---- FE 0.0 60 32.0 0.0 37.4 0.0 0.028 TL 12.50 PV Pipe: 57 -17.9 1.380 FL 1.83 PF 0.1 60 32.0 0.0 37.4 0.0 3.8 120 FTG ---- FE 0.0 62 32.0 0.0 37.4 0.0 0.028 TL 1.83 PV Pipe: 58 0.0 1.049 FL 35.00 PF 0.0 61 29.0 0.0 38.7 0.0 0.0 120 FTG ---- FE -1.3 62 32.0 0.0 37.4 0.0 0.000 TL 35.00 PV Pipe: 59 -17.9 1.380 FL 9.25 PP 0.3 62 32.0 0.0 37.4 0.0 3.8 120 FTG ---- FE 0.0 64 32.0 0.0 37.7 0.0 0.028 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PP 0.0 63 29.0 0.0 39.0 0.0 0.0 120 FTG ---- FE -1.3 64 32.0 0.0 37.7 0.0 0.000 TL 35.00 PV Pipe: 61 -17.9 1.380 FL 0.92 FE' 0.0 64 32.0 0.0 37.7 0.0 3.8 120 FTG ---- FE 0.0 65 32.0 0.0 37.7 0.0 0.028 TL 0.92 PV Pipe: 62 -17.9 1.380 FL 12.00 PP 0.3 65 32.0 0.0 37.7 0.0 3.8 120 FTG ---- PE 0.0 66 32.0 0.0 38.0 0.0 0.028 TL 12.00 PV Pipe: 63 -17.9 1.380 FL 1.42 PF 0.0 66 32.0 0.0 38.0 0.0 3.8 120 FTG ---- FE 0.0 68 32.0 0.0 38.1 0.0 0.028 TL 1.42 PV Pipe: 64 0.0 1.049 FL 35.00 PF 0.0 67 29.0 0.0 39.4 0.0 0.0 120 FTG ---- FE -1.3 68 32.0 0.0 38.1 0.0 0.000 TL 35.00 PV * SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -17.9 1.380 FL 9.17 PF 0.3 68 32.0 0.0 38.1 0.0 3.8 120 FTG ---- FE 0.0 70 32.0 0.0 38.3 0.0 0.028 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PF 0.0 69 29.0 0.0 39.6 0.0 0.0 120 FTG ---- FE -1.3 70 32.0 0.0 38.3 0.0 0.000 TL 35.00 PV Pipe: 67 -17.9 1.380 PL 1.25 PF 0.0 70 32.0 0.0 38.3 0.0 3.8 120 FTG ---- PE 0.0 71 32.0 0.0 38.4 0.0 0.028 TL 1.25 PV Pipe: 68 -17.9 1.380 FL 30.80 PF 1.1 71 32.0 0.0 38.4 0.0 3.8 120 FTG ET PE 0.0 72 32.0 0.0 39.5 0.0 0.028 TL 39.80 PV Pipe: 69 -17.9 1.380 PL 175.00 PF 5.0 72 32.0 0.0 39.5 0.0 3.8 120 FTG T PE 0.0 73 32.0 0.0 44.5 0.0 0.028 TL 181.00 PV Pipe: 70 -17.9 1.380 PL 2.00 PF 0.2 73 32.0 0.0 44.5 0.0 3.8 120 FTG T PE 0.9 74 30.0 0.0 45.6 0.0 0.028 TL 8.00 PV Pipe: 71 17.9 1.380 PL 2.00 PF 0.2 75 32.0 0.0 32.2 0.0 3.8 120 FTG T PE 0.9 76 30.0 0.0 32.9 0.0 0.028 TL 8.00 PV Pipe: 72 -17.9 1.380 PL 38.25 PF 1.1 75 32.0 0.0 32.2 0.0 3.8 120 FTG L PE 0.0 77 32.0 0.0 33.3 0.0 0.028 TL 40.25 PV Pipe: 73 -17.9 1.380 PL 150.42 PF 4.2 77 32.0 0.0 33.3 0.0 3.8 120 FTG ---- PE 0.0 78 32.0 0.0 37.5. 0.0 0.028 TL 150.42 PV Pipe: 74 -17.9 1.380 PL 65.83 FE' 2.0 78 32.0 0.0 37.5 0.0 3.8 120 FTG 2E PE 0.0 79 32.0 0.0 39.5 0.0 0.028 TL 71.83 PV Pipe: 75 -17.9 1.380 PL 170.83 FE' 4.9 79 32.0 0.0 39.5 0.0 3.8 120 FTG T PE 0.0 80 32.0 0.0 44.4 0.0 0.028 TL 176.83 PV Pipe: 76 -17.9 1.380 PL 2.00 PF 0.2 80 32.0 0.0 44.4 0.0 3.8 120 FTG T FE 0.9 81 30.0 0.0 45.5 0.0 0.028 TL 8.00 PV Pipe: 77 18.0 1.380 FL 2.00 PF 0.2 82 32.0 0.0 32.2 0.0 3.9 120 FTC T PE 0.9 83 30.0 0.0 32.9 0.0 0.028 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -18.0 1.380 PL 24.58 PF 0.7 82 32.0 0.0 32.2 0.0 3.9 120 FTG L FE 0.0 84 32.0 0.0 33.0 0.0 0.028 TL 26.58 PV Pipe: 79 -18.0 1.380 FL 190.50 PF 5.7 84 32.0 0.0 33.0 0.0 3.9 120 FTG 4E FE 0.0 85 32.0 0.0 38.7 0.0 0.028 TL 202.50 PV Pipe: 80 -18.0 1.380 PL 196.21 PF 5.7 85 32.0 0.0 38.7 0.0 3.9 120 FTG T PE 0.0 86 32.0 0.0 44.4 0.0 0.028 TL 202.21 PV Pipe: 81 -18.0 1.380 PL 2.00 PF 0.2 86 32.0 0.0 44.4 0.0 3.9 120 FTG T PE 0.9 87 30.0 0.0 45.5 0.0 0.028 TL 8.00 PV Pipe: 82 17.5 1.380 PL 3.50 PF 0.3 88 33.5 0.0 31.6 0.0 3.7 120 FTG T FE 1.5 89 30.0 0.0 32.9 0.0 0.027 TL 9.50 PV Pipe: 83 -17.5 1.380 PL 33.58 PF 0.9 88 33.5 0.0 31.6 0.0 3.7 120 FTG L PE 0.0 90 33.5 0.0 32.6 0.0 0.027 TL 35.58 By Pipe: 84 -17.5 1.380 PL 202.38 PF 5.8 90 33.5 0.0 32.6 0.0 3.7 120 FTG 3ET BE 0.0 91 33.5 0.0 38.4 0.0 0.027 TL 217.38 PV Pipe: 85 -17.5 1.380 PL 193.96 PF 5.3 91 33.5 0.0 38.4 0.0 3.7 120 FTG T FE 0.0 92 33.5 0.0 43.7 0.0 0.027 TL 199.96 By Pipe: 86 -17.5 1.380 PL 3.50 PF 0.3 92 33.5 0.0 43.7 0.0 3.7 120 FTG T FE 1.5 93 30.0 0.0 45.5 0.0 0.027 TL 9.50 PV Pipe: 87 -107.0 2.635 PL 3.00 PF 0.1 11 30.0 0.0 32.4 0.0 6.3 120 FTG ---- FE 0.0 33 30.0 0.0 32.5 0.0 0.033 TL 3.00 PV Pipe: 88 -89.3 2.635 PL 8.50 PF 0.2 33 30.0 0.0 32.5 0.0 5.3 120 FTG ---- PE 0.0 45 30.0 0.0 32.7 0.0 0.023 TL 8.50 PV Pipe: 89 -71.2 2.635 PL 6.92 PF 0.1 45 30.0 0.0 32.7 0.0 4.2 120 FTG ---- BE 0.0 56 30.0 0.0 32.8 0.0 0.015 TL 6.92 By Pipe: 90 -53.4 2.635 PL 7.42 PF 0.1 56 30.0 0.0 32.8 0.0 3.1 120 FTG ---- BE 0.0 76 30.0 0.0 32.9 0.0 0.009 TL 7.42 By SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Caic 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. FT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) PSI) (GPM) FL/FT (PSI) Pipe: 91 -35.5 2.635 PL 7.00 PF 0.0 76 30.0 0.0 32.9 0.0 2.1 120 FTG ---- PE 0.0 83 30.0 0.0 32.9 0.0 0.004 TL 7.00 PV Pipe: 92 -17.5 2.635 PL 3.92 PF 0.0 83 30.0 0.0 32.9 0.0 1.0 120 FTG ---- PE 0.0 89 30.0 0.0 32.9 0.0 0.001 TL 3.92 PV Pipe: 93 -22.3 2.635 PL 5.54 PF 0.0 23 30.0 0.0 46.0 0.0 1.3 120 FTG ---- PE 0.0 43 30.0 0.0 46.0 0.0 0.002 TL 5.54 PV Pipe: 94 -40.1 2.635 PL 8.96 PF 0.1 43 30.0 0.0 46.0 0.0 2.4 120 FTG T PE 0.0 94 30.0 0.0 46.1 0.0 0.005 TL 25.96 PV Pipe: 95 -17.5 2.635 PL 5.40 PF 0.0 93 30.0 0.0 45.5 0.0 1.0 120 FTG ---- PE 0.0 87 30.0 0.0 45.5 0.0 0.001 TL 5.40 PV Pipe: 96 -35.5 2.635 FL 9.50 PF 0.0 87 30.0 0.0 45.5 0.0 2.1 120 FTG ---- PE 0.0 81 30.0 0.0 45.5 0.0 0.004 TL 9.50 PV Pipe: 97 -53.4 2.635 PL 8.17 PF 0.1 81 30.0 0.0 45.5 0.0 3.1 120 FTG ---- PE 0.0 74 30.0 0.0 45.6 0.0 0.009 TL 8.17 PV Pipe: 98 -71.2 2.635 PL 7.96 PF 0.1 74 30.0 0.0 45.6 0.0 4.2 120 FTG ---- PE 0.0 54 30.0 0.0 45.7 0.0 0.015 TL 7.96 PV Pipe: 99 -89.3 2.635 PL 1.04 PF 0.4 54 30.0 0.0 45.7 0.0 5.3 120 FTG T FE 0.0 94 30.0 0.0 46.1 0.0 0.023 TI- 18.04 PV Pipe: 100 -129.3 2.635 PL 20.38 PF 1.7 94 30.0 0.0 46.1 0.0 7.6 120 FTG 2E PE 0.0 95 30.0 0.0 47.8 0.0 0.046 TL 36.38 PV Pipe: 101 -129.3 2.635 PL 75.50 PF 5.4 95 30.0 0.0 47.8 0.0 7.6 120 FTG SE PE 12.8 BOR 0.5 0.0 66.0 0.0 0.046 TL 115.50 PV Pipe: 102 -129.3 6.280 PL 10.00 PF 0.0 BOR 0.5 0.0 66.0 0.0 1.3 140 FTG E PE 1.5 UG3 -3.0 0.0 67.5 0.0 0.001 TL 32.00 PV Pipe: 103 -129.3 6.080 PL 142.00 PF 0.1 UG3 -3.0 0.0 67.5 0.0 1.4 150 FTG 3E FE 0.0 UG2 -3.0 0.0 67.6 0.0 0.001 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Calc 4 - SD1 Heads PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -129.3 6.280 PL 5.00 PF 0.0 UG2 -3.0 0.0 67.6 0.0 1.3 140 FTG ET PE -2.2 3F2 2.0 0.0 65.5 0.0 0.001 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE EF1 2.0 0.0 69.5 0.0 4.0 psi, 129.3 gpm BF2 2.0 0.0 65.5 0.0 Pipe: 106 -129.3 6.280 PL 5.00 PF 0.0 EF1 2.0 0.0 69.5 0.0 1.3 140 FTG 2E PE 2.2 UG1 -3.0 0.0 71.7 0.0 0.001 TL 49.00 PV Pipe: 107 -129.3 6.080 PL 16.00 PF 0.0 UG1 -3.0 0.0 71.7 0.0 1.4 150 FTG TG PE 0.0 SRC -3.0 SRCE 71.7 (N/A) 0.001 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.114 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 23.0 ft/sec at pipe 10. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.76 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building H Calc 4 - SD1 Heads PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) H T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: H MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 160.0 140.0 G A l2O . 0 G E P100. 0 R E S S 80.0 U R E p S 40.0 20.0 -14 WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm 400 600 800 1000 1200 1400 1600 2000 FLOW (GPM) 3hed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 4.SDF JOB TITLE: La Costa Glen Building E Cab 4 - 5Db Heads WATER SUPPLY CURVE 156*0\\\\\\\\\\\\\\\\\\\\\\\\\ I \\\\\\\\\\\\\\\\\\\\\\\\\\ I 149.0 psi 8 1790 gpm-> * I Flow Test Point 143+ 130+ 117+ P104+ R I E I S I S 91+ U R E I 78+ P IX S I I 65+ 52+ 39+ 26+ LEGEND 'I I X = Required Water Supply I 71.69 psi 8 229.3 gpm 13+ I 0 = Available Water Supply I 154.87 psi 8 229.3 gpm I, +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SRC 155.0 149.0 1790.0 AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 154.8 271.3 138.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 271.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 171.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 29.0 K= 6.90 53.4 50.4 2 30.0 - - - - 78.1 - - - 3 33.5 - - - - 78.7 4 33.5 - - - - 79.2 - - - 5 29.0 - - - - 81.5 - - - 6 30.0 - - - - 81.1 - - - 7 33.5 - - - - 79.6 - - - 8 33.5 - - - - 79.9 - - - 9 33.5 - - - - 80.7 - - - 10 33.5 - - - - 82.0 - - - 11 30.0 - - - - 84.1 - - - 12 33.5 - - - - 82.4 - - - 13 33.5 - - - - 82.6 14 33.5 - - - - 84.1 - - - 15 33.5 - - - - 84.8 - - - 16 33.5 - - - - 93.7 - - - 17 33.5 - - - - 94.0 - - - 18 33.5 - - - - 94.2 - - - 19 33.5 - - - - 94.5 - - - 20 33.5 - - - - 94.8 - - - 21 33.5 - - - - 96.3 - - - 22 33.5 - - - - 105.9 - - - 23 30.0 - - - - 107.8 - - - 24 29.0 K= 6.90 33.6 40.0 25 30.0 - - - - 49.6 - - - 26 29.0 K= 6.90 33.8 40.1 27 30.0 - - - - 49.9 - - - 28 29.0 K= 6.90 34.9 40.8 29 30.0 - - - - 51.5 - - - 30 32.0 - - - - 64.1 - - - 31 32.0 - - - - 71.8 - - - 32 32.0 - - - - 78.4 - - - 33 30.0 - - - - 84.1 - - - 34 32.0 - - - - 81.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building H Caic 5 - Res. Heads 20x20 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 35 32.0 - - - - 90.4 - - - 36 32.0 - - - - 91.4 - - - 37 32.0 - - - - 92.0 - - - 38 32.0 - - - - 92.4 - - - 39 32.0 - - - - 92.4 - - - 40 32.0 - - - - 93.0 - - - 41 32.0 - - - - 95.8 - - - 42 32.0 - - - - 106.5 - - - 43 30.0 - - - - 107.8 - - - 44 32.0 - - - - 83.5 - - - 45 30.0 - - - - 84.4 - - - 46 32.0 - - - - 86.0 - - - 47 32.0 - - - - 93.2 - - - 48 32.0 - - - - 93.7 - - - 49 32.0 - - - - 94.0 - - - 50 32.0 - - - - 94.5 - - - 51 32.0 - - - 95.0 - - 52 32.0 - - - - 96.7 - - - 53 32.0 - - - - 106.0 - - - 54 30.0 - - - - 107.3 - - - 55 32.0 - - - - 84.1 - - - 56 30.0 - - - - 84.6 - - - 57 32.0 - - - - 86.1 - - - 58 29.0 - - - - 94.0 - - - 59 32.0 - - - - 92.7 - - - 60 32.0 - - - - 93.3 - - - 61 29.0 - - - - 94.7 - - - 62 32.0 - - - - 93.4 - - - 63 29.0 - - - - 95.1 - - - 64 32.0 - - - - 93.8 - - - 65 32.0 - - - - 93.9 - - - 66 32.0 - - - - 94.5 - - - 67 29.0 - - - - 95.8 - - - 68 32.0 - - - - 94.5 - - - 69 29.0 - - - - 96.3 - - - 70 32.0 - - - - 95.0 - - - 71 32.0 - - - - 95.0 - - - 72 32.0 - - - - 97.0 - - - 73 32.0 - - - - 105.8 - - - 74 30.0 - - - - 107.1 - - - 75 32.0 - - - - 84.2 - - - 76 30.0 - - - - 84.7 - - - 77 32.0 - - - - 86.2 - - - 78 32.0 - - - - 93.6 - - - 79 32.0 - - - - 97.1 - - - 80 32.0 - - - - 105.7 - - - 81 30.0 - - - - 106.9 - - - 82 32.0 - - - - 84.3 - - - 83 30.0 - - - - 84.8 - - - 84 32.0 - - - - 85.6 - - - 85 32.0 - - - - 95.6 - - - 86 32.0 - - - - 105.6 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 87 30.0 - - - - 106.9 - - - 88 33.5 - - - - 83.7 - - - 89 30.0 - - - - 84.8 - - - 90 33.5 - - - - 85.4 - - - 91 33.5 - - - - 95.5 92 33.5 - - - - 104.9 - - - 93 30.0 - - - - 106.9 - - - 94 30.0 - - - - 108.0 - - - 95 30.0 - - - - 110.9 - - - BOR 0.5 - - - - 132.7 UG3 -3.0 - - - - 134.2 UG2 -3.0 - - - - 134.4 - - - BF2 2.0 - - - - 132.3 BF1 2.0 - - - - 136.3 - - - UG1 -3.0 - - - - 138.5 - - - SRC -3.0 SOURCE 138.5 171.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 -50.4 1.049 PL 35.00 PF 25.2 1 29.0 6.9 53.4 50.4 18.7 120 FTG ---- PE -0.4 2 30.0 0.0 78.1 0.0 0.720 TL 35.00 PV Pipe: 2 -50.4 1.380 PL 5.00 PF 2.1 2 30.0 0.0 78.1 0.0 10.8 120 FTG 2E PE -1.5 3 33.5 0.0 78.7 0.0 0.189 TL 11.00 PV Pipe: 3 -50.4 1.380 PL 2.50 PF 0.5 3 33.5 0.0 78.7 0.0 10.8 120 FTG ---- PE 0.0 4 33.5 0.0 79.2 0.0 0.189 TL 2.50 PV Pipe: 4 -50.4 1.380 PL 2.21 PF 0.4 4 33.5 0.0 79.2 0.0 10.8 120 FTG ---- PE 0.0 7 33.5 0.0 79.6 0.0 0.189 TL 2.21 PV Pipe: 5 0.0 1.049 PL 35.00 PF 0.0 5 29.0 0.0 81.5 0.0 0.0 120 FTG ---- PE -0.4 6 30.0 0.0 81.1 0.0 0.000 TL 35.00 PV Pipe: 6 0.0 1.380 PL 4.29 FE' 0.0 6 30.0 0.0 81.1 0.0 0.0 120 FTG ET PE -1.5 7 33.5 0.0 79.6 0.0 0.000 TL 13.29 PV Pipe: 7 -50.4 1.380 PL 1.75 PF 0.3 7 33.5 0.0 79.6 0.0 10.8 120 FTG ---- PE 0.0 8 33.5 0.0 79.9 0.0 0.189 TL 1.75 PV Pipe: 8 -50.4 1.380 PL 4.00 PF 0.8 8 33.5 0.0 79.9 0.0 10.8 120 FTG ---- PE 0.0 9 33.5 0.0 80.7 0.0 0.189 TL 4.00 PV Pipe: 9 -50.4 1.380 FL 0.83 FE' 1.3 9 33.5 0.0 80.7 0.0 10.8 120 FTG T FE 0.0 10 33.5 0.0 82.0 0.0 0.189 TL 6.83 PV Pipe: 10 -26.9 1.380 PL 3.50 PF 0.6 10 33.5 0.0 82.0 0.0 5.8 120 FTG T PE 1.5 11 30.0 0.0 84.1 0.0 0.059 TL 9.50 PV Pipe: 11 -23.5 1.380 PL 3.17 PF 0.4 10 33.5 0.0 82.0 0.0 5.0 120 FTG T PE 0.0 12 33.5 0.0 82.4 0.0 0.046 TL 9.17 PV Pipe: 12 -23.5 1.380 PL 4.00 PF 0.2 12 33.5 0.0 82.4 0.0 5.0 120 FTG ---- FE 0.0 13 33.5 0.0 82.6 0.0 0.046 TL 4.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 -23.5 1.380 PL 30.25 PF 1.5 13 33.5 0.0 82.6 0.0 5.0 120 FTG L PE 0.0 14 33.5 0.0 84.1 0.0 0.046 TL 32.25 PV Pipe: 14 -23.5 1.380 PL 10.42 PP 0.8 14 33.5 0.0 84.1 0.0 5.0 120 FTG T PE 0.0 15 33.5 0.0 84.8 0.0 0.046 TL 16.42 PV Pipe: 15 -23.5 1.380 PL 177.46 PP 8.9 15 33.5 0.0 84.8 0.0 5.0 120 FTG 3ET PE 0.0 16 33.5 0.0 93.7 0.0 0.046 TL 192.46 PV Pipe: 16 -23.5 1.380 PL 6.00 PF 0.3 16 33.5 0.0 93.7 0.0 5.0 120 FTG ---- PE 0.0 17 33.5 0.0 94.0 0.0 0.046 TL 6.00 PV Pipe: 17 -23.5 1.380 PL 6.00 PP 0.3 17 33.5 0.0 94.0 0.0 5.0 120 FTG ---- PE 0.0 18 33.5 0.0 94.2 0.0 0.046 TL 6.00 PV Pipe: 18 -23.5 1.380 PL 6.00 PF 0.3 18 33.5 0.0 94.2 0.0 5.0 120 FTG ---- PE 0.0 19 33.5 0.0 94.5 0.0 0.046 TL 6.00 PV Pipe: 19 -23.5 1.380 PL 6.00 PF 0.3 19 33.5 0.0 94.5 0.0 5.0 120 FTG ---- PE 0.0 20 33.5 0.0 94.8 0.0 0.046 TL 6.00 PV Pipe: 20 -23.5 1.380 PL 26.42 PF 1.5 20 33.5 0.0 94.8 0.0 5.0 120 FTG 2E PE 0.0 21 33.5 0.0 96.3 0.0 0.046 TL 32.42 PV Pipe: 21 -23.5 1.380 PL 189.96 PF 9.6 21 33.5 0.0 96.3 0.0 5.0 120 FTG 4ET PE 0.0 22 33.5 0.0 105.9 0.0 0.046 TL 207.96 PV Pipe: 22 -23.5 1.380 PL 3.50 PP 0.4 22 33.5 0.0 105.9 0.0 5.0 120 FTG T PE 1.5 23 30.0 0.0 107.8 0.0 0.046 TL 9.50 PV Pipe: 23 -40.0 1.049 PL 35.00 PP 16.4 24 29.0 6.9 33.6 40.0 14.8 120 FTG ---- PE -0.4 25 30.0 0.0 49.6 0.0 0.469 TL 35.00 PV Pipe: 24 -40.0 1.380 PL 2.75 PF 0.3 25 30.0 0.0 49.6 0.0 8.6 120 FTG ---- PE 0.0 27 30.0 0.0 49.9 0.0 0.123 TL 2.75 PV Pipe: 25 -40.1 1.049 PL 35.00 PF 16.5 26 29.0 6.9 33.8 40.1 14.9 120 FTG ---- PE -0.4 27 30.0 0.0 49.9 0.0 0.472 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 8/25/2016GPAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 -80.1 1.380 PL 3.50 PF 1.6 27 30.0 0.0 49.9 0.0 17.2 120 FTG ---- PE 0.0 29 30.0 0.0 51.5 0.0 0.446 TL 3.50 PV Pipe: 27 -40.8 1.049 PL 35.00 PP 17.0 28 29.0 6.9 34.9 40.8 15.1 120 FTG ---- PE -0.4 29 30.0 0.0 51.5 0.0 0.486 TL 35.00 PV Pipe: 28 -120.9 1.380 PL 8.12 PF 13.5 29 30.0 0.0 51.5 0.0 25.9 120 FTG 2E PE -0.9 30 32.0 0.0 64.1 0.0 0.955 TL 14.12 PV Pipe: 29 -120.9 1.380 PL 8.00 PF 7.6 30 32.0 0.0 64.1 0.0 25.9 120 FTG ---- FE 0.0 31 32.0 0.0 71.8 0.0 0.955 TL 8.00 PV Pipe: 30 -120.9 1.380 PL 0.96 PF 6.6 31 32.0 0.0 71.8 0.0 25.9 120 FTG T PE 0.0 32 32.0 0.0 78.4 0.0 0.955 TL 6.96 PV Pipe: 31 -94.1 1.380 PL 2.00 PP 4.8 32 32.0 0.0 78.4 0.0 20.2 120 FTG T FE 0.9 33 30.0 0.0 84.1 0.0 0.600 TL 8.00 PV Pipe: 32 -26.9 1.380 FL 47.58 PF 3.3 32 32.0 0.0 78.4 0.0 5.8 120 FTG TL PE 0.0 34 32.0 0.0 81.7 0.0 0.059 TL 55.58 PV Pipe: 33 -26.9 1.380 PL 138.50 PF 8.7 34 32.0 0.0 81.7 0.0 5.8 120 FTG 3E PE 0.0 35 32.0 0.0 90.4 0.0 0.059 TL 147.50 PV Pipe: 34 -26.9 1.380 PL 14.00 PF 1.0 35 32.0 0.0 90.4 0.0 5.8 120 FTG E PE 0.0 36 32.0 0.0 91.4 0.0 0.059 TL 17.00 PV Pipe: 35 -26.9 1.380 PL 10.00 PF 0.6 36 32.0 0.0 91.4 0.0 5.8 120 FTG ---- FE 0.0 37 32.0 0.0 92.0 0.0 0.059 TL 10.00 PV Pipe: 36 -26.9 1.380 PL 8.00 PF 0.5 37 32.0 0.0 92.0 0.0 5.8 120 FTG ---- FE 0.0 39 32.0 0.0 92.4 0.0 0.059 TL 8.00 PV Pipe: 37 0.0 1.380 FL 10.00 PF 0.0 38 32.0 0.0 92.4 0.0 0.0 120 FTG ---- PE 0.0 39 32.0 0.0 92.4 0.0 0.000 TL 10.00 PV Pipe: 38 -26.9 1.380 PL 10.00 PF 0.6 39 32.0 0.0 92.4 0.0 5.8 120 FTG ---- FE 0.0 40 32.0 0.0 93.0 0.0 0.059 TL 10.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -26.9 1.380 PL 34.67 PF 2.8 40 32.0 0.0 93.0 0.0 5.8 120 FTG 4E PE 0.0 41 32.0 0.0 95.8 0.0 0.059 TL 46.67 RV Pipe: 40 -26.9 1.380 PL 175.12 PF 10.7 41 32.0 0.0 95.8 0.0 5.8 120 FTG T PE 0.0 42 32.0 0.0 106.5 0.0 0.059 TL 181.12 PV Pipe: 41 -26.9 1.380 PL 2.00 PF 0.5 42 32.0 0.0 106.5 0.0 5.8 120 FTG T PE 0.9 43 30.0 0.0 107.8 0.0 0.059 TL 8.00 PV Pipe: 42 0.0 1.380 PL 2.00 PF 0.0 44 32.0 0.0 83.5 0.0 0.0 120 FTG T PE 0.9 45 30.0 0.0 84.4 0.0 0.000 TL 8.00 PV Pipe: 43 -24.4 1.380 PL 41.25 PF 2.4 45 30.0 0.0 84.4 0.0 5.2 120 FTG TL PE -0.9 46 32.0 0.0 86.0 0.0 0.049 TL 49.25 PV Pipe: 44 -24.4 1.380 PL 145.04 PF 7.2 46 32.0 0.0 86.0 0.0 5.2 120 FTG ---- PE 0.0 47 32.0 0.0 93.2 0.0 0.049 TL 145.04 PV Pipe: 45 -24.4 1.380 PL 10.00 PF 0.5 47 32.0 0.0 93.2 0.0 5.2 120 FTG ---- PE 0.0 48 32.0 0.0 93.7 0.0 0.049 TL 10.00 PV Pipe: 46 -24.4 1.380 PL 8.00 PF 0.4 48 32.0 0.0 93.7 0.0 5.2 120 FTG ---- PE 0.0 49 32.0 0.0 94.0 0.0 0.049 TL 8.00 PV Pipe: 47 -24.4 1.380 PL 10.00 PF 0.5 49 32.0 0.0 94.0 0.0 5.2 120 FTG ---- PE 0.0 50 32.0 0.0 94.5 0.0 0.049 TL 10.00 PV Pipe: 48 -24.4 1.380 PL 10.00 PF 0.5 50 32.0 0.0 94.5 0.0 5.2 120 FTG ---- PE 0.0 51 32.0 0.0 95.0 0.0 0.049 TL 10.00 PV Pipe: 49 -24.4 1.380 PL 27.96 PF 1.7 51 32.0 0.0 95.0 0.0 5.2 120 FTG 2E PE 0.0 52 32.0 0.0 96.7 0.0 0.049 TL 33.96 PV Pipe: 50 -24.4 1.380 PL 182.33 PF 9.3 52 32.0 0.0 96.7 0.0 5.2 120 FTG T FE 0.0 53 32.0 0.0 106.0 0.0 0.049 TL 188.33 PV Pipe: 51 -24.4 1.380 FL 2.00 PF 0.4 53 32.0 0.0 106.0 0.0 5.2 120 FTG T PE 0.9 54 30.0 0.0 107.3 0.0 0.049 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 8/25/2016GRA.M FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOE TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 24.2 1.380 PL 2.00 PF 0.4 55 32.0 0.0 84.1 0.0 5.2 120 FTG T PE 0.9 56 30.0 0.0 84.6 0.0 0.049 TL 8.00 PV Pipe: 53 -24.2 1.380 PL 38.17 PF 2.0 55 32.0 0.0 84.1 0.0 5.2 120 FTG L PE 0.0 57 32.0 0.0 86.1 0.0 0.049 TL 40.17 PV Pipe: 54 -24.2 1.380 PL 134.70 PF 6.6 57 32.0 0.0 86.1 0.0 5.2 120 FTG ---- PE 0.0 59 32.0 0.0 92.7 0.0 0.049 TL 134.70 PV Pipe: 55 0.0 1.049 PL 35.00 PF 0.0 58 29.0 0.0 94.0 0.0 0.0 120 FTG ---- PE -1.3 59 32.0 0.0 92.7 0.0 0.000 TL 35.00 PV Pipe: 56 -24.2 1.380 PL 12.50 PF 0.6 59 32.0 0.0 92.7 0.0 5.2 120 FTG ---- PE 0.0 60 32.0 0.0 93.3 0.0 0.049 TL 12.50 PV Pipe: 57 -24.2 1.380 PL 1.83 PF 0.1 60 32.0 0.0 93.3 0.0 5.2 120 FTG ---- PE 0.0 62 32.0 0.0 93.4 0.0 0.049 TL 1.83 PV Pipe: 58 0.0 1.049 PL 35.00 PF 0.0 61 29.0 0.0 94.7 0.0 0.0 120 FTG' ---- PE -1.3 62 32.0 0.0 93.4 0.0 0.000 TL 35.00 PV Pipe: 59 -24.2 1.380 PL 9.25 PF 0.5 62 32.0 0.0 93.4 0.0 5.2 120 FTG ---- PE 0.0 64 32.0 0.0 93.8 0.0 0.049 TL 9.25 PV Pipe: 60 0.0 1.049 PL 35.00 PF 0.0 63 29.0 0.0 95.1 0.0 0.0 120 FTG ---- PE -1.3 64 32.0 0.0 93.8 0.0 0.000 TL 35.00 PV Pipe: 61 -24.2 1.380 PL 0.92 PF 0.0 64 32.0 0.0 93.8 0.0 5.2 120 FTG ---- PE 0.0 65 32.0 0.0 93.9 0.0 0.049 TL 0.92 PV Pipe: 62 -24.2 1.380 PL 12.00 PF 0.6 65 32.0 0.0 93.9 0.0 5.2 120 FTG ---- PE 0.0 66 32.0 0.0 94.5 0.0 0.049 TL 12.00 PV Pipe: 63 -24.2 1.380 PL 1.42 PF 0.1 66 32.0 0.0 94.5 0.0 5.2 120 FTG ---- PE 0.0 68 32.0 0.0 94.5 0.0 0.049 TL 1.42 PV Pipe: 64 0.0 1.049 PL 35.00 PF 0.0 67 29.0 0.0 95.8 0.0 0.0 120 FTG ---- PE -1.3 68 32.0 0.0 94.5 0.0 0.000 TL 35.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (PT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 65 -24.2 1.380 PL 9.17 PP 0.4 68 32.0 0.0 94.5 0.0 5.2 120 FTG ---- PE 0.0 70 32.0 0.0 95.0 0.0 0.049 TL 9.17 PV Pipe: 66 0.0 1.049 PL 35.00 PP 0.0 69 29.0 0.0 96.3 0.0 0.0 120 FTG ---- FE -1.3 70 32.0 0.0 95.0 0.0 0.000 TL 35.00 PV Pipe: 67 -24.2 1.380 PL 1.25 PF 0.1 70 32.0 0.0 95.0 0.0 5.2 120 FTG ---- PE 0.0 71 32.0 0.0 95.0 0.0 0.049 TL 1.25 PV Pipe: 68 -24.2 1.380 PL 30.80 PP 1.9 71 32.0 0.0 95.0 0.0 5.2 120 FTG ET PE 0.0 72 32.0 0.0 97.0 0.0 0.049 TL 39.80 PV Pipe: 69 -24.2 1.380 PL 175.00 PP 8.8 72 32.0 0.0 97.0 0.0 5.2 120 FTG T FE 0.0 73 32.0 0.0 105.8 0.0 0.049 TL 181.00 PV Pipe: 70 -24.2 1.380 PL 2.00 PP 0.4 73 32.0 0.0 105.8 0.0 5.2 120 FTG T PE 0.9 74 30.0 0.0 107.1 0.0 0.049 TL 8.00 PV Pipe: 71 24.2 1.380 PL 2.00 PP 0.4 75 32.0 0.0 84.2 0.0 5.2 120 FTG T FE 0.9 76 30.0 0.0 84.7 0.0 0.049 TL 8.00 PV Pipe: 72 -24.2 1.380 PL 38.25 PP 2.0 75 32.0 0.0 84.2 0.0 5.2 120 FTG L FE 0.0 77 32.0 0.0 86.2 0.0 0.049 TL 40.25 PV Pipe: 73 -24.2 1.380 PL 150.42 PP 7.3 77 32.0 0.0 86.2 0.0 5.2 120 FTG ---- FE 0.0 78 32.0 0.0 93.6 0.0 0.049 TL 150.42 PV Pipe: 74 -24.2 1.380 PL 65.83 PP 3.5 78 32.0 0.0 93.6 0.0 5.2 120 FTG 2E PE 0.0 79 32.0 0.0 97.1 0.0 0.049 TL 71.83 PV Pipe: 75 -24.2 1.380 PL 170.83 PP 8.6 79 32.0 0.0 97.1 0.0 5.2 120 FTG T FE 0.0 80 32.0 0.0 105.7 0.0 0.049 TL 176.83 PV Pipe: 76 -24.2 1.380 FL 2.00 PP 0.4 80 32.0 0.0 105.7 0.0 5.2 120 FTG T FE 0.9 81 30.0 0.0 106.9 0.0 0.049 TL 8.00 PV Pipe: 77 24.4 1.380 PL 2.00 PF 0.4 82 32.0 0.0 84.3 0.0 5.2 120 FTG T FE 0.9 83 30.0 0.0 84.8 0.0 0.049 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building B Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -24.4 1.380 PL 24.58 PF 1.3 82 32.0 0.0 84.3 0.0 5.2 120 FTG L PE 0.0 84 32.0 0.0 85.6 0.0 0.049 TL 26.58 PV Pipe: 79 -24.4 1.380 PL 190.50 PF 10.0 84 32.0 0.0 85.6 0.0 5.2 120 FTG 4E PE 0.0 85 32.0 0.0 95.6 0.0 0.049 TL 202.50 PV Pipe: 80 -24.4 1.380 PL 196.21 PF 10.0 85 32.0 0.0 95.6 0.0 5.2 120 FTG T PE 0.0 86 32.0 0.0 105.6 0.0 0.049 TL 202.21 PV Pipe: 81 -24.4 1.380 PL 2.00 PF 0.4 86 32.0 0.0 105.6 0.0 5.2 120 FTG T PE 0.9 87 30.0 0.0 106.9 0.0 0.049 TL 8.00 PV Pipe: 82 23.7 1.380 PL 3.50 PF 0.4 88 33.5 0.0 83.7 0.0 5.1 120 FTG T PE 1.5 89 30.0 0.0 84.8 0.0 0.047 TL 9.50 PV Pipe: 83 -23.7 1.380 PL 33.58 FE' 1.7 88 33.5 0.0 83.7 0.0 5.1 120 FTG L PE 0.0 90 33.5 0.0 85.4 0.0 0.047 TL 35.5S PV Pipe: 84 -23.7 1.380 PL 202.38 PF 10.2 90 33.5 0.0 85.4 0.0 5.1 120 FTG 3ET PE 0.0 91 33.5 0.0 95.5 0.0 0.047 TL 217.38 PV Pipe: 85 -23.7 1.380 PL 193.96 PF 9.4 91 33.5 0.0 95.5 0.0 5.1 120 FTG T PE 0.0 92 33.5 0.0 104.9 0.0 0.047 TL 199.96 PV Pipe: 86 -23.7 1.380 PL 3.50 PF 0.4 92 33.5 0.0 104.9 0.0 5.1 120 FTG T PE 1.5 93 30.0 0.0 106.9 0.0 0.047 TL 9.50 PV Pipe: 87 -26.9 2.635 PL 3.00 PF 0.0 11 30.0 0.0 84.1 0.0 1.6 120 FTG ---- PE 0.0 33 30.0 0.0 84.1 0.0 0.003 TL 3.00 PV Pipe: 88 -121.0 2.635 PL 8.50 PF 0.3 33 30.0 0.0 84.1 0.0 7.1 120 FTG ---- PE 0.0 45 30.0 0.0 84.4 0.0 0.041 TL 8.50 PV Pipe: 89 -96.6 2.635 PL 6.92 PF 0.2 45 30.0 0.0 84.4 0.0 5.7 120 FTG ---- PE 0.0 56 30.0 0.0 84.6 0.0 0.027 TL 6.92 PV Pipe: 90 -72.3 2.635 PL 7.42 PF 0.1 56 30.0 0.0 84.6 0.0 4.3 120 FTG ---- FE 0.0 76 30.0 0.0 84.7 0.0 0.016 TL 7.42 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 8/25/2016GRAN FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -48.1 2.635 PL 7.00 PF 0.1 76 30.0 0.0 84.7 0.0 2.8 120 FTG ---- PE 0.0 83 30.0 0.0 84.8 0.0 0.007 TL 7.00 PV Pipe: 92 -23.7 2.635 PL 3.92 PF 0.0 83 30.0 0.0 84.8 0.0 1.4 120 FTG ---- PE 0.0 89 30.0 0.0 84.8 0.0 0.002 TL 3.92 PV Pipe: 93 -23.5 2.635 PL 5.54 PF 0.0 23 30.0 0.0 107.8 0.0 1.4 120 FTG ---- PE 0.0 43 30.0 0.0 107.8 0.0 0.002 TL 5.54 PV Pipe: 94 -50.3 2.635 PL 8.96 PF 0.2 43 30.0 0.0 107.8 0.0 3.0 120 FTG T PE 0.0 94 30.0 0.0 108.0 0.0 0.008 TL 25.96 PV Pipe: 95 -23.7 2.635 PL 5.40 PF 0.0 93 30.0 0.0 106.9 0.0 1.4 120 FTG ---- PE 0.0 87 30.0 0.0 106.9 0.0 0.002 TL 5.40 PV Pipe: 96 -48.1 2.635 PL 9.50 PF 0.1 87 30.0 0.0 106.9 0.0 2.8 120 FTG ---- PE 0.0 81 30.0 0.0 106.9 0.0 0.007 TL 9.50 PV Pipe: 97 -72.3 2.635 PL 8.17 PF 0.1 81 30.0 0.0 106.9 0.0 4.3 120 FTG ---- PE 0.0 74 30.0 0.0 107.1 0.0 0.016 TL 8.17 PV Pipe: 98 -96.6 2.635 PL 7.96 PF 0.2 74 30.0 0.0 107.1 0.0 5.7 120 FTG ---- PE 0.0 54 30.0 0.0 107.3 0.0 0.027 TL 7.96 PV Pipe: 99 -121.0 2.635 PL 1.04 PF 0.7 54 30.0 0.0 107.3 0.0 7.1 120 FTG T PE 0.0 94 30.0 0.0 108.0 0.0 0.041 TL 18.04 PV Pipe: 100 -171.3 2.635 PL 20.38 PF 2.8 94 30.0 0.0 108.0 0.0 10.1 120 FTG 2E PE 0.0 95 30.0 0.0 110.9 0.0 0.078 TL 36.38 PV Pipe: 101 -171.3 2.635 PL 75.50 PF 9.0 95 30.0 0.0 110.9 0.0 10.1 120 FTG 5E PE 12.8 BOR 0.5 0.0 132.7 0.0 0.078 TL 115.50 PV Pipe: 102 -171.3 6.280 PL 10.00 PF 0.0 BOR 0.5 0.0 132.7 0.0 1.8 140 FTG E FE 1.5 UG3 -3.0 0.0 134.2 0.0 0.001 TL 32.00 PV Pipe: 103 -171.3 6.080 PL 142.00 PF 0.2 UG3 -3.0 0.0 134.2 0.0 1.9 150 FTG 3E FE 0.0 UG2 -3.0 0.0 134.4 0.0 0.001 TL 208.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 104 -171.3 6.280 PL 5.00 PF 0.1 UG2 -3.0 0.0 134.4 0.0 1.8 140 FTG ET FE -2.2 BF2 2.0 0.0 132.3 0.0 0.001 TL 74.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE BF1 2.0 0.0 136.3 0.0 4.0 psi, 171.3 gpm BF2 2.0 0.0 132.3 0.0 Pipe: 106 -171.3 6.280 FL 5.00. FE' 0.0 BF1 2.0 0.0 136.3 0.0 1.8 140 FTG 2E FE 2.2 UG1 -3.0 0.0 138.5 0.0 0.001 TL 49.00 PV Pipe: 107 -171.3 6.080 FL 16.00 FF 0.1 UG1 -3.0 0.0 138.5 0.0 1.9 150 FTG TG FE 0.0 SRC -3.0 SRCE 138.5 (N/A) 0.001 TL 67.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 2707013234 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.067 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 25.9 ft/sec at pipe 30. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SRC under full flow conditions is 154.80 psi compared to the minimum required pressure of 20.00 psi. FIFE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Caic 5 - Res. Heads 20x20 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: B MATERIAL: THNWL HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyVlv GatVlv AimChk DPViv NPTee 2.635 8.00 17.00 6.00 19.00 10.00 1.00 14.00 14.00 17.00 PAGE: D MATERIAL: DIRON HC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEii ChkViv BfyVlv GatVlv NPTee 6.280 22.00 47.00 14.00 51.00 16.00 5.00 47.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEli ChkViv BfyVlv GatVlv NPTee 6.080 22.00 46.00 14.00 49.00 15.00 5.00 46.00 WATER SUPPLY ANALYSIS Static: 155.00 psi Resid: 149.00 psi Flow: 1790.0 gpm 160.0 1 140.02 G A U120 . 0 G E P100 . 0 R E S S 80.0 U R E P S 40.0 20.0 Aws -14. 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) shed Lines indicate extrapolated values from Test Results SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 8/25/2016GRAM FILES\HRS SYSTEMS\HASSDATA\LA COSTA GLEN - CALC 5.SDF JOB TITLE: La Costa Glen Building E Calc 5 - Res. Heads 20x20 WATER SUPPLY CURVE I 149.0 psi 8 1790 gpm-> * I Flow Test Point 143+ Ix 130+ 117+ P104+ R I E S I S 91+ U I R I E I 78+ ( I P I S I 65+ 52+ 39+ 26+ LEGEND X = Required Water Supply I 138.55 psi @ 271.3 gpm 13+ 0 = Available Water Supply I 154.82 psi @ 271.3 gpm 'V 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)