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3301 LINCOLN ST; ; AS160077; Permit
3/2/22, 10:03 AM AS160077 Permit Data City of Carlsbad Sprinkler Permit Job Address: 3301 LINCOLN ST Permit Type: SPRINK Parcel No: 2041311701 Lot #: 0 Permit No: A5160077 Status: ISSUED Applied 3/30/2016 Approved: 3/30/2016 Reference No.: . Issued: 3/30/2016 PC #: Inspector: Project Title: 3301 LINCOLN ST UNIT Al: 2,138 SF LIV! 447 SF GAR! 131 SF DECK Applicant: Owner: RESIDENTIAL FIRE SYSTEMS, INC 8085 E. CRYSTAL DR ANAHEIM, CA 92807 Fees ($) Add'l Fees ($) I Total ($) Balance ($) 213 0 L 213 0 1/1 RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. 'CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 1 - 1ST FLOOR GARAGE FILE NUMBER: 9301 DATE: FEB 19, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED TOTAL SPRINKLER MATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (8 BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: ORDINARY (GROUP 1) HAZARD 0.15 gpm/sq. ft. 520 sq. ft. 130 sq. ft. 4 sprinklers 84.3 gpm 184.4 gpm 84.3 gpm 8 46.9 psi 1/2 inch RESIDENTIAL FIRE SYSTEMS, INC. RAFAEL E. CARLSBAD FIRE DEPARTMENT C-16 #786965 CALCULATIONS BY HASS COMPUTER 'PROGRAM (LICENSE # ' 38061304 HRS SYSTEMS, INC. 7hei phtn hits, ' l\llI It rt if, lue uh heLIPOHI IrpIIcahk 1,s and III ttce .li the mlnMitctlm ill. IL ll\ let lltk Ii ills 1111/. III lmmIl I all tj ft.a150 tm j I-lIlt rt i dl IIIItL i S II II \ll\ lClil Ine 0%%11121 of LlllltLlIr III Fir iai tlm elClae mr aijilteal tlt .lIe re'Ii biim lid IiiljiIi_llli.L itlt dill codes alld sIdlidliT l ilicilatllls 111C hiiililiita LIII II lilt dtt\ 11)lillsihIIt\ tIlt (IL licililCIe'. II 11115. l)lIliSlmtt' of leLilemilLe Ill pt:iii II ticiliel hF not itiliCli Ill E lio, revel; ),I 77' i ems at R (t )NI Ml-.Nl) APIl<l tV-li [J IN I lit<tt\. s NI lii fl Au 5CTJ SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOE TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. 8 TAG (PSI) (PSI) (GPM) SRC 85.5 20.0 1500.0 AVAIL. TOTAL REQTD PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 84.1 184.4 58.8., AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 184.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 84.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 13.8 - - - 2 30.0 - - - - 13.8 - - - 3 30.0 - - - - 13.7 - - - 4 30.0 - - - - 14.1 - - - 5 30.0 - - - - 14.1 - - - 6 30.0 - - - - 14.1 - - - 7 33.0 - - - - 12.8 - - - 8 30.0 - - - - 14.1 - - - 9 30.0 - - - - 14.1 - - - 10 30.0 - - - - 14.1 - - - 11 30.0 - - - 14.2 - - - 12 30.0 - - - - 14.2 - - - 13 30.0 - - - - 14.2 - - - 14 30.0 - - - - 14.2 - - - 15 30.0 - - - - 14.2 - - - 16 30.0 - - - - 14.2 - - - 17 ... .30.0 . - - - - .. 14.2 - - 18 30.0 - - - - 14.2 - - - 19 33.0 - - - 12.9 - - - 20 30.0 - - - - 14.3 - - - 21 30.0 - - - - 14.2 - - - 22 30.0 - - - - 14.5 - - - 23 30.0 - - - - 14.5 - - - 24 30.0 - - - - 14.9 - - 25 30.0 - - - - 17.9 26 30.0 - - - - 20.8 - - - 27 30.0 - - - - 23.6 - - - 28 30.0 - - - - 26.5 - - - 29 30.0 - - - - 29.1 - - - 30 30.0 - - - - 30.3 - - - 31 30.0 - - - - 29.3 - - - 32 30.0 - - - - 29.5 - - - 33 20.0 - - - - 34.1 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 20.0 - - - 34.6 - - - 35 20.0 - - - - 35.1 - - - 36 30.0 - - - - 31.0 - - - 37 30.0 - - - - 31.3 - - - 38 30.0 - - - - 32.4 - - - 39 20.0 - - - - 37.1 - - - 40 20.0 - - - - 37.3 - - - 41 20.0 - - - - 34.9 - - - 42 20.0 - - - - 18.5 - - - 43 20.0 - - - - 18.5 - - - 44 20.0 - - - 18.6 - - - 45 20.0 - - - - 18.6 - - - 46 20.0 - - - - 18.6 - - - 47 20.0 - - - - 18.6 - - - 48 20.0 - - - 18.3 - - - 49 20.0 - - - - 18.1 - - - 50 20.0 - - - - 18.1 - - - 51 20.0 - - - - 18.0 - - - 52 20.0 - - - - 18.0 - - - 53 22.5 - - - - 16.9 - - - 54 20.0 - - - - 17.8 - - - 55 20.0 - - - 17.8 - - - 56 22.5 - - - - 16.7 - - - 57 20.0 - - - - 17.8 - - - 58 20.0 - - - - 17.8 - - - 59 22.5 - - - - 16.7 - - - 60 20.0 - - - - 17.5 - - - 61 20.0 - - - - 17.5 - - - 62 22.5 - - - - 16.5 - - - 63 20.0 - - - - 17.4 - - - 64 20.0 - - - - 17.5 - - - 65 20.0 - - - - 16.9 - - - 66 9.5 - - - - 19.3 - - - 67 9.5 - - - - 19.1 - - - 68 10.0 - - - - 17.4 - - - 69 10.0 K= 5.60 16.7 22.9 70 10.0 K= 5.60 15.4 22.0 71 9.5 - - - - 19.3 - - - 72 10.0 - - - - 16.6 - - - 73 10.0 - - - - 13.8 - - - 74 10.0 K= 5.60 12.8 20.0 75 10.0 K= 5.60 12.1 19.5 76 9.5 - - - - 24.2 - - - 77 9.5 - - - - 28.5 - - - 78 9.5 - - - - 32.8 - - - 79 9.5 - - - - 37.1 - - - 80 9.5 - - - - 43.0 - - - 81 9.5 - - - - 42.8 - - - 82 10.0 - - - - 42.4 - - - 83 10.0 - - - - 41.9 - - - 84 10.0 - - - - 39.7 - - - 85 9.5 - - - - 42.6 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 86 9.5 - - - - 42.5 - - - 87 9.5 - - - - 42.4 - - - TOP 9.5 - - - - 44.0 - - - MID 4.0 - - - - 46.9 - - - BTM 1.0 - - - - 48.3 - - Ui -4.0 - - - - 50.5 - - - U2 -4.0 - - - - 50.6 - - - U3 -4.0 - - - - 50.6 - - - U4 3.0 - - - - 47.7 - - - U5 3.0 - - - - 55.7 - - - U6 -4.0 - - - - 58.7 - - - SRC -4.0 SOURCE 58.8 84.4 4 4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 1.101 PL 2.25 PF 0.0 1 30.0 0.0 13.8 0.0 0.0 150 FTG E PE 0.0 2 30.0 0.0 13.8 0.0 0.000 TL 9.25 PV Pipe: 2 11.4 1.101 PL 2.25 PF 0.1 2 30.0 0.0 13.8 0.0 3.8 150 FTG ---- PE 0.0 3 30.0 0.0 13.7 0.0 0.024 TL 2.25 PV Pipe: 3 -11.4 1.101 PL 8.00 PF 0.4 2 30.0 0.0 13.8 0.0 3.8 150 FTG 2FT PE 0.0 4 30.0 0.0 14.1 0.0 0.024 TL 15.00 PV Pipe: 4 0.0 1.101 PL 10.00 PF 0.0 4 30.0 0.0 14.1 0.0 0.0 150 FTG T PE 0.0 5 30.0 0.0 14.1 0.0 0.000 TL 15.00 PV Pipe: 5 0.0 1.101 PL 0.75 PF 0.0 5 30.0 0.0 14.1 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 14.1 0.0 0.000 TL 5.75 PV Pipe: 6 0.0 1.101 PL 3.00 PF 0.0 6 30.0 0.0 14.1 0.0 0.0 150 FTG E PE -1.3 7 33.0 0.0 12.8 0.0 0.000 TL 10.00 PV Pipe: 7 0.0 1.101 PL 8.50 PF 0.0 5 30.0 0.0 14.1 0.0 0.0 150 FTG ---- PE 0.0 8 30.0 0.0 14.1 0.0 0.000 TL 8.50 PV Pipe: 8 0.0 1.101 FL 8.75 PF 0.0 8 30.0 0.0 14.1 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 14.1 0.0 0.000 TL 13.75 PV Pipe: 9 0.0 1.101 PL 7.75 PF 0.0 8 30.0 0.0 14.1 0.0 0.0 150 FTG ---- PE 0.0 10 30.0 0.0 14.1 0.0 0.000 TL 7.75 PV Pipe: 10 -11.4 1.101 PL 3.75 PF 0.1 4 30.0 0.0 14.1 0.0 3.8 150 FTG ---- PE 0.0 11 30.0 0.0 14.2 0.0 0.024 TL 3.75 PV Pipe: 11 0.0 1.101 PL 16.25 PF 0.011, 11 30.0 0.0 14.2 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 14.2 0.0 0.000 TL 21.25 PV Pipe: 12 0.0 1.101 PL 7.25 PF 0.0 12 30.0 0.0 14.2 0.0 0.0 150 FTG E PE 0.0 13 30.0 0.0 14.2 0.0 0.000 TL 14.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOE TITLE: 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 0.0 1.101 PL 2.00 PF 0.0 12 30.0 0.0 14.2 0.0 0.0 150 FTG T PE 0.0 14 30.0 0.0 14.2 0.0 0.000 TL 7.00 PV Pipe: 14 -11.4 1.101 PL 0.50 PF 0.0 11 30.0 0.0 14.2 0.0 3.8 150 FTG ---- PE 0.0 15 30.0 0.0 14.2 0.0 0.024 TL 0.50 PV Pipe: 15 0.0 1.101 PL 4.00 PF 0.0 15 30.0 0.0 14.2 0.0 0.0 150 FTG T PE 0.0 16 30.0 0.0 14.2 0.0 0.000 TL 9.00 PV Pipe: 16 0.0 1.101 PL 2.25 PF 0.0 16 30.0 0.0 14.2 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 14.2 0.0 0.000 TL 7.25 PV Pipe: 17 0.0 1.101 PL 6.50 PF 0.0 16 30.0 0.0 14.2 0.0 0.0 150 FTG E PE 0.0 18 30.0 0.0 14.2 0.0 0.000 TL 13.50 PV Pipe: 18 0.0 1.101 PL 3.00 PF 0.0 18 30.0 0.0 14.2 0.0 0.0 150 FTG F PE -1.3 19 33.0 0.0 12.9 0.0 0.000 TL 10.00 PV Pipe: 19 -11.4 1.101 PL 1.50 PF 0.0 15 30.0 0.0 14.2 0.0 3.8 150 FTG ---- PE 0.0 20 30.0 0.0 14.3 0.0 0.024 TL 1.50 PV Pipe: 20 8.6 1.101 PL 2.25 PF 0.1 20 30.0 0.0 14.3 0.0 2.9 150 FTG T PE 0.0 21 30.0 0.0 14.2 0.0 0.014 TL 7.25 PV Pipe: 21 -20.0 1.101 PL 3.00 PF 0.2 20 30.0 0.0 14.3 0.0 6.7 150 FTG ---- PE 0.0 22 30.0 0.0 14.5 0.0 0.068,. TL 3.00 PV Pipe: 22 0.0 1.101 PL 1.50 PF 0.0 22 30.0 0.0 14.5 0.0 0.0 150 FTG T PE 0.0 23 30.0 0.0 14.5 0.0 0.000 TL 6.50 PV Pipe: 23 -20.0 1.101 PL 4.00 PF 0.4 22 30.0 0.0 14.5 0.0 6.7 150 FTG 2F PE 0.0 24 30.0 0.0 14.9 0.0 0.068 TL 6.00 PV Pipe: 24 -20.0 1.101 PL 28.50 PF 3.0 24 30.0 0.0 14.9 0.0 6.7 150 FTG 2F2E PE 0.0 25 30.0 0.0 17.9 0.0 0.068 TL 44.50 PV Pipe: 25 -20.0 1.101 PL 26.00 PF 2.9 25 30.0 0.0 17.9 0.0 6.7 150 FTG 2F2E PE 0.0 26 30.0 0.0 20.8 0.0 0.068 TL 42.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 -20.0 1.101 PL 26.00 PF 2.9 26 30.0 0.0 20.8 0.0 6.7 150 FTG 2F2E PE 0.0 27 30.0 0.0 23.6 0.0 0.068 TL 42.00 PV Pipe: 27 -20.0 1.101 PL 26.00 PF 2.9 27 30.0 0.0 23.6 0.0 6.7 150 FTG 2F2E PE 0.0 28 30.0 0.0 26.5 0.0 0.068 TL 42.00 PV Pipe: 28 -20.0 1.101 PL 22.50 PF 2.6 28 30.0 0.0 26.5 0.0 6.7 150 FTG 2F2E PE 0.0 29 30.0 0.0 29.1 0.0 0.068 TL 38.50 PV Pipe: 29 -10.1 1.101 PL 36.25 PF 1.2 29 30.0 0.0 29.1 0.0 3.4 150 FTG 2E2T PE 0.0 30 30.0 0.0 30.3 0.0 0.019 TL 60.25 PV Pipe: 30 -9.9 1.101 PL 7.75 PF 0.2 29 30.0 0.0 29.1 0.0 3.3 150 FTG 2F PE 0.0 31 30.0 0.0 29.3 0.0 0.019 TL 9.75 PV Pipe: 31 -9.9 1.101 PL 3.50 PF 0.2 31 30.0 0.0 29.3 0.0 3.3 150 FTG T PE 0.0 32 30.0 0.0 29.5 0.0 0.019 TL 8.50 PV Pipe: 32 -9.9 1.101 PL 10.00 PF 0.3 32 30.0 0.0 29.5 0.0 3.3 150 FTG E PE 4.3 33 20.0 0.0 34.1 0.0 0.019 TL 17.00 PV Pipe: 33 -9.9 1.101 PL 21.25 PF 0.5 33 20.0 0.0 34.1 0.0 3.3 150 FTG 4F PE 0.0 34 20.0 0.0 34.6 0.0 0.019 TL 25.25 PV Pipe: 34 -9.9 1.101 FL 21.25 PF 0.5 34 20.0 0.0 34.6 0.0 3.3 150 FTG 4F PE 0.0 35 20.0 0.0 35.1 0.0 0.019 TL 25.25 PV Pipe: 35 -9.9 1.101 PL 10.00 PF 0.3 35 20.0 0.0 35.1 0.0 3.3 150 FTG E PE -4.3 36 30.0 0.0 31.0 0.0 0.019 TL 17.00 PV Pipe: 36 -9.9 1.101 PL 6.50 PF 0.3 36 30.0 0.0 31.0 0.0 3.3 150 FTG E PE 0.0 37 30.0 0.0 31.3 0.0 0.019 TL 13.50 PV Pipe: 37 -9.9 1.101 FL 38.75 PF 1.1 37 30.0 0.0 31.3 0.0 3.3 150 FTG E3T PE 0.0 38 30.0 0.0 32.4 0.0 0.019 TL 60.75 PV Pipe: 38 -9.9 1.101 FL 10.00 PF 0.3 38 30.0 0.0 32.4 0.0 3.3 150 FTG E PE 4.3 39 20.0 0.0 37.1 0.0 0.019 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 -9.9 1.101 PL 5.25 PF 0.2 39 20.0 0.0 37.1 0.0 3.3 150 FTG E FE 0.0 40 20.0 0.0 37.3 0.0 0.019 TL 12.25 PV Pipe: 40 -10.1 1.101 PL 10.00 PF 0.3 30 30.0 0.0 30.3 0.0 3.4 150 FTG E PE 4.3 41 20.0 0.0 34.9 0.0 0.019 TL 17.00 PV Pipe: 41 0.0 1.101 PL 10.00 PF 0.0 10 30.0 0.0 14.1 0.0 0.0 150 FTG E PE 4.3 42 20.0 0.0 18.5 0.0 0.000 TL 17.00 PV Pipe: 42 0.0 1.101 FL 5.00 PF 0.0 42 20.0 0.0 18.5 0.0 0.0 150 FTG 2E FE 0.0 43 20.0 0.0 18.5 0.0 0.000 TL 19.00 PV Pipe: 43 0.0 1.101 PL 10.00 PF 0.0 14 30.0 0.0 14.2 0.0 0.0 150 FTG E PE 4.3 44 20.0 0.0 18.6 0.0 0.000 TL 17.00 PV Pipe: 44 0.0 1.101 PL 8.00 PF 0.0 44 20.0 0.0 18.6 0.0 0.0 150 FTG 2E PE 0.0 45 20.0 0.0 18.6 0.0 0.000 TL 22.00 PV Pipe: 45 0.0 1.101 PL 10.00 PF 0.0 17 30.0 0.0 14.2 0.0 0.0 150 FTG E PE 4.3 46 20.0 0.0 18.6 0.0 0.000 TL 17.00 PV Pipe: 46 0.0 1.101 PL 3.50 PF 0.0 46 20.0 0.0 18.6 0.0 0.0 150 FTG 2E PE 0.0 47 20.0 0.0 18.6 0.0 0.000 TL 17.50 PV Pipe: 47 8.6 1.101 PL 10.00 PF 0.2 21 30.0 0.0 14.2 0.0 2.9 150 FTG E PE 4.3 48 20.0 0.0 18.3 0.0 0.014 TI 17.00 PV Pipe: 48 8.6 1.101 PL 1.25 PF 0.1 48 20.0 0.0 18.3 0.0 2.9 150 FTG E FE 0.0 49 20.0 0.0 18.1 0.0 0.014 TL 8.25 PV Pipe: 49 0.0 1.101 FL 4.00 PF 0.0 49 20.0 0.0 18.1 0.0 0.0 150 FTG ET FE 0.0 50 20.0 0.0 18.1 0.0 0.000 TL 16.00 PV Pipe: 50 8.6 1.101 PL 9.25 PF 0.1 49 20.0 0.0 18.1 0.0 2.9 150 FTG ---- PE 0.0 51 20.0 0.0 18.0 0.0 0.014 TL 9.25 PV Pipe: 51 0.0 1.101 FL 2.50 PF 0.0 51 20.0 0.0 18.0 0.0 0.0 150 FTG ET FE 0.0 52 20.0 0.0 18.0 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 0.0 1.101 PL 2.50 PF 0.0 52 20.0 0.0 18.0 0.0 0.0 150 FTG E PE -1.1 53 22.5 0.0 16.9 0.0 0.000 TL 9.50 PV Pipe: 53 8.6 1.101 PL 5.75 PF 0.2 51 20.0 0.0 18.0 0.0 2.9 150 FTG E PE 0.0 54 20.0 0.0 17.8 0.0 0.014 TL 12.75 PV Pipe: 54 0.0 1.101 PL 2.25 PF 0.0 54 20.0 0.0 17.8 0.0 0.0 150 FTG T PE 0.0 55 20.0 0.0 17.8 0.0 0.000 TL 7.25 PV Pipe: 55 0.0 1.101 PL 2.50 PF 0.0 55 20.0 0.0 17.8 0.0 0.0 150 FTG K PE -1.1 56 22.5 0.0 16.7 0.0 0.000 TL 9.50 PV Pipe: 56 8.6 1.101 PL 5.00 PF 0.1 54 20.0 0.0 17.8 0.0 2.9 150 FTG ---- PE 0.0 57 20.0 0.0 17.8 0.0 0.014 TL 5.00 PV Pipe: 57 0.0 1.101 PL 2.25 PF 0.0 57 20.0 0.0 17.8 0.0 0.0 150 FTG T PE 0.0 58 20.0 0.0 17.8 0.0 0.000 TL 7.25 PV Pipe: 58 0.0 1.101 PL 2.50 PF 0.0 58 20.0 0.0 17.8 0.0 0.0 150 FTG E PE -1.1 59 22.5 0.0 16.7 0.0 0.000 TL 9.50 PV Pipe: 59 8.6 1.101 PL 7.75 PF 0.2 57 20.0 0.0 17.8 0.0 2.9 150 FTG E PE 0.0 60 20.0 0.0 17.5 0.0 0.014 TL 14.75 PV Pipe: 60 0.0 1.101 PL 0.50 PF 0.0 60 20.0 0.0 17.5 0.0 0.0 150 FTG T PE 0.0 61 20.0 0.0 17.5 0.0 0.000 TL 5.50 PV Pipe: 61 0.0 1.101 PL 2.50 PF 0.0 61 20.0 0.0 17.5 0.0 0.0 150 FTG E PE -1.1 62 22.5 0.0 16.5 0.0 0.000 TL 9.50 PV Pipe: 62 8.6 1.101 PL 8.50 PP 0.1 60 20.0 0.0 17.5 0.0 2.9 150 FTG ---- PE 0.0 63 20.0 0.0 17.4 0.0 0.014 TL 8.50 PV Pipe: 63 -11.4 1.101 PL 2.50 PF 0.1 63 20.0 0.0 17.4 0.0 3.8 150 FTG ---- PE 0.0 64 20.0 0.0 17.5 0.0 0.024 TL 2.50 PV Pipe: 64 11.4 1.101 PL 10.00 PF 0.6 3 30.0 0.0 13.7 0.0 3.8 150 FTG 2E PE 4.3 64 20.0 0.0 17.5 0.0 0.024 TL 24.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 20.0 1.101 PL 2.75 PF 0.5 63 20.0 0.0 17.4 0.0 6.7 150 FTG T PE 0.0 65 20.0 0.0 16.9 0.0 0.068 TL 7.75 PV Pipe: 66 20.0 1.101 PL 10.50 PF 2.1 65 20.0 0.0 16.9 0.0 6.7 150 FTG 3E PE 4.5 66 9.5 0.0 19.3 0.0 0.068 TL 31.50 PV Pipe: 67 20.0 1.654 PL 7.00 PF 0.2 66 9.5 0.0 19.3 0.0 3.0 120 FTG T PE 0.0 67 9.5 0.0 19.1 0.0 0.014 TL 16.12 PV Pipe: 68 44.8 1.083 PL 0.50 PF 1.4 67 9.5 0.0 19.1 0.0 15.6 120 FTG E PE -0.2 68 10.0 0.0 17.4 0.0 0.496 TL 2.84 PV Pipe: 69 44.8 1.083 PL 1.50 PF 0.7 68 10.0 0.0 17.4 0.0 15.6 120 FTG ---- PE 0.0 69 10.0 5.6 16.7 22.9 0.496 TL 1.50 PV Pipe: 70 22.0 1.083 PL 10.00 PF 1.3 69 10.0 5.6 16.7 22.9 7.6 120 FTG ---- PE 0.0 70 10.0 5.6 15.4 22.0 0.132 TL 10.00 PV Pipe: 71 -24.8 1.654 PL 13.25 PF 0.3 67 9.5 0.0 19.1 0.0 3.7 120 FTG ---- PE 0.0 71 9.5 0.0 19.3 0.0 0.021 TL 13.25 PV Pipe: 72 39.5 1.083 PL 0.50 PF 2.5 71 9.5 0.0 19.3 0.0 13.8 120 FTG T PE -0.2 72 10.0 0.0 16.6 0.0 0.393 TL 6.34 PV Pipe: 73 39.5 1.083 PL 1.50 PF 2.9 72 10.0 0.0 16.6 0.0 13.8 120 FTG T PE 0.0 73 10.0 0.0 13.8 0..0 1 1 0.393 TL 7.34 .PV Pipe: 74 20.0 1.083 PL 3.00 PF 1.0 73 10.0 0.0 13.8 0.0 7.0 120 FTG T PE 0.0 74 10.0 5.6 12.8 20.0 0.112 TL 8.84 PV Pipe: 75 19.5 1.083 PL 13.00 PF 1.6 73 10.0 0.0 13.8 0.0 6.8 120 FTG E PE 0.0 75 10.0 5.6 12.1 19.5 0.106 TL 15.34 PV Pipe: 76 -64.3 1.654 PL 30.00 PF 4.8 71 9.5 0.0 19.3 0.0 9.6 120 FTG 2E PE 0.0 76 9.5 0.0 24.2 0.0 0.123 TL 39.12 PV Pipe: 77 -64.3 1.654 PL 26.00 PF 4.3 76 9.5 0.0 24.2 0.0 9.6 120 FTG 2E PE 0.0 77 9.5 0.0 28.5 0.0 0.123 TL 35.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 -64.3 1.654 PL 26.00 PF 4.3 77 9.5 0.0 28.5 0.0 9.6 120 FTG 2E FE 0.0 78 9.5 0.0 32.8 0.0 0.123 TL 35.12 PV Pipe: 79 -64.3 1.654 PL 26.00 PF 4.3 78 9.5 0.0 32.8 0.0 9.6 120 FTG 2E FE 0.0 79 9.5 0.0 37.1 0.0 0.123 TL 35.12 PV Pipe: 80 -64.3 1.654 PL 29.75 PF 5.9 79 9.5 0.0 37.1 00 9.6 120 FTG 4E PE 0.0 80 9.5 0.0 43.0 0.0 0.123 TL 47.99 PV Pipe: 81 20.0 1.654 FL 4.25 PF 0.2 80 9.5 0.0 43.0 0.0 3.0 120 FTG T FE 0.0 81 9.5 0.0 42.8 0.0 0.014 TL 13.37 PV Pipe: 82 10.1 1.083 PL 0.50 PF 0.2 81 9.5 0.0 42.8 0.0 3.5 120 FTG T FE -0.2 82 10.0 0.0 42.4 0.0 0.032 TL 6.34 PV Pipe: 83 10.1 1.083 FL 6.75 PF 0.5 82 10.0 0.0 42.4 0.0 3.5 120 FTG ET FE 0.0 83 10.0 0.0 41.9 0.0 0.032 TL 14.93 PV Pipe: 84 10.1 1.101 PL 57.25 PF 2.2 83 10.0 0.0 41.9 0.0 3.4 120 FTG 2E3T FE 0.0 84 10.0 0.0 39.7 0.0 0.029 TL 76.44 PV Pipe: 85 -10.1 1.101 FL 10.00 PF 0.4 41 20.0 0.0 34.9 0.0 3.4 120 FTG E FE 4.3 84 10.0 0.0 39.7 0.0 0.029 TL 14.63 PV Pipe: 86 9.9 1.654 FL 37.00 PF 0.2 81 9.5 0.0 42.8 0.0 1.5 120 FTG 4E FE 0.0 85 9.5 0.0 42.6 0.0 0.004 TL 55.24 PV Pipe: 87 9.9 1.654 FL 31.50 PF 0.1 85 9.5 0.0 42.6 0.0 1.5 120 FTG E FE 0.0 86 9.5 0.0 42.5 0.0 0.004 TL 36.06 PV Pipe: 88 9.9 1.654 FL 16.75 PF 0.1 86 9.5 0.0 42.5 0.0 1.5 120 FTG E FE 0.0 87 9.5 0.0 42.4 0.0 0.004 TL 21.31 pv Pipe: 89 -9.9 1.101 FL 10.50 PF 0.6 40 20.0 0.0 37.3 0.0 3.3 120 FTG 2E FE 4.5 87 9.5 0.0 42.4 0.0 0.028 TL 19.76 PV Pipe: 90 -84.3 2.705 FL 17.75 PF 1.0 80 9.5 0.0 43.0 0.0 4.7 120 FTG 2ET FE 0.0 TOP 9.5 0.0 44.0 0.0 0.018 TL 55.19 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 -84.3 2.705 PL 5.50 PF 0.5 TOP 9.5 0.0 44.0 0.0 4.7 120 FTG C FE 2.4 MID 4.0 0.0 46.9 0.0 0.018 TL 27.34 PV Pipe: 92 -84.3 2.705 PL 3.00 PF 0.1 MID 4.0 0.0 46.9 0.0 4.7 120 FTG ---- FE 1.3 BTM 1.0 0.0 48.3 0.0 0.018 TL 3.00 PV Pipe: 93 -84.3 4.026 PL 10.00 PF 0.1 BTM 1.0 0.0 48.3 0.0 2.1 120 FTG E PE 2.2 Ui -4.0 0.0 50.5 0.0 0.003 TL 20.00 PV Pipe: 94 -84.3 4.240 PL 43.80 PF 0.1 Ui -4.0 0.0 50.5 0.0 1.9 150 FTG 3E PE 0.0 U2 -4.0 0.0 50.6 0.0 0.001 TL 103.80 PV Pipe: 95 -84.3 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 50.6 0.0 1.9 150 FTG ---- PE 0.0 U3 -4.0 0.0 50.6 0.0 0.001 TL 3.50 PV Pipe: 96 -84.3 4.220 PL 7.00 PF 0.1 U3 -4.0 0.0 50.6 0.0 1.9 140 FTG 2E PE -3.0 U4 3.0 0.0 47.7 0.0 0.002 TL 41.00 PV Pipe: 97 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 55.7 0.0 8.0 psi, 84.3 gpm U4 3.0 0.0 47.7 0.0 Pipe: 98 -84.3 4.220 FL 7.00 PF 0.0 U5 3.0 0.0 55.7 0.0 1.9 140 FTG E FE 3.0 U6 -4.0 0.0 58.7 0.0 0.002 TL 24.00 PV Pipe: 99 -84.4 4.240 PL 22.50 PF 0.1 U6 -4.0 0.0 58.7 0.0 1.9 150 FTG E FE 0.0 SRC -4.0 SRCE 58.8 (N/A) 0.001 TL 42.50 ,PV. NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.197 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 15.6 ft/sec at pipe 69. A SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 83.83 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd 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 NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 2/19/20165PR1NKLER5\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: PAGE: X MATERIAL: EdFlw HHC: 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 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: E 1) 000 Q) u_ 0 c-0E W OQ)Q) co 0 04 - i)-1 -)E( tOl)- W0.-44J- -HC0> -- 0c0c0 0'• a) I I. 4. 4. .4 I I I I I I I I / 4. S / I 4. / I 4p1 / I / 0 0 0 0 CD co kD C 0 0 0 0 0 0 C 0 0 0 W (N 0 0 7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 2/19/2016SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 1ST FLOOR GARAGE.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ *\ I0\ I \ 80+ \ I \ \\ 72+ \ \ \ P 64+ \ R \ E I \\ S IX \ S 56+ \ U I \ R E I \ 48+ \\ I \ P I \ S I \ I 40+ \ \ I \\ 32+ .24+ . I * <-20.0 psi 8 1500 gpm I ============================== Flow Test Point 16+ LEGEND I X = Required Water Supply I 58.80 psi 0 184.4 gpm 8+ I 0 = Available Water Supply I 84.14 psi @ 184.4 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 1 - 2ND FLOOR ATTIC FILE NUMBER: 9301 DATE: FEB 19, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 480 sq. ft. COVERAGE PER SPRINKLER: 120 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 53.0 gpm TOTAL WATER REQUIRED (including hose) : 153.0 gpm FLOW AND PRESSURE (8 BOR) : 53.0 gpm 8 39.2 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC. DESIGN/LAYOUT BY: RAFAEL E. AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C-16 #786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\EUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 85.5 20.0 1500.0 84.5 153.0 49.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 153.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 53.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 9.6 - - - 2 30.0 - - - - 9.6 - - - 3 30.0 - - - - 9.6 - - - 4 30.0 - - - - 9.6 - - - 5 30.0 - - - 9.6 - - - 6 30.0 - - - - 9.6 - - - 7 33.0 - - - - 8.3 - - - 8 30.0 - - - - 9.6 - - - 9 30.0 - - - - 9.6 - - - 10 30.0 - - - - 9.6 - - - 11 30.0 - - - - 9.6 - - - 12 30.0 - - - - 9.6 - - - 13 30.0 - - - - 9.6 - - - 14 30.0 - - - - 9.6 - - - 15 30.0 - - - - 9.6 - - - 16 30.0 - - - - 9.6 - - - 17 30.0 - - - - 9.6 -- - 18 30.0 - - - - 9.6 - - - 19 33.0 - - - - 8.3 - - - 20 30.0 - - - - 9.6 - - - 21 30.0 - - - - 9.2 - - - 22 30.0 - - - - 9.8 - - - 23 30.0 - - - - 9.8 - - - 24 30.0 - - - - 10.1 - - - 25 30.0 - - - - 12.6 - - - 26 30.0 - - - - 15.0 - - - 27 30.0 - - - - 17.3 - - - 28 30.0 - - - - 19.7 - - - 29 30.0 - - - - 21.9 - - - 30 30.0 - - - - 22.8 - - - 31 30.0 - - - - 22.0 - - - 32 30.0 - - - - 22.1 - - - 33 20.0 - - - - 26.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 20.0 - - - - 27.1 - - - 35 20.0 - - - - 27.5 - - - 36 30.0 - - - - 23.4 - - - 37 30.0 - - - - 23.6 - - - 38 30.0 - - - - 24.6 - - - 39 20.0 - - - - 29.1 - - - 40 20.0 - - - - 29.3 - - - 41 20.0 - - - - 27.4 - - - 42 20.0 - - - - 13.9 - - - 43 20.0 - - - - 13.9 - - - 44 20.0 - - - - 13.9 - - - 45 20.0 - - - - 13.9 - - - 46 20.0 - - - - 13.9 - - - 47 20.0 - - - - 13.9 - - - 48 20.0 - - - - 12.5 - - - 49 20.0 - - - - 12.0 - - - 50 20.0 - - - - 12.0 - - 51 20.0 - - - - 11.4 - - 52 20.0 - - - - 11.0 - - - 53 22.5 K= 4.20 9.6 13.0 54 20.0 - - - - 11.3 - - - 55 20.0 - - - - 11.1 - - - 56 22.5 K= 4.20 9.7 13.1 57 20.0 - - - - 11.4 - - - 58 20.0 - - - - 11.1 - - - 59 22.5 K= 4.20 9.8 13.1 60 20.0 - - - - 12.4 - - - 61 20.0 - - - - 12.2 - - - 62 22.5 K= 4.20 10.8 13.8 63 20.0 - - - - 14.0 - - - 64 20.0 - - - - 14.0 - - - 65 20.0 - - - - 15.4 - - - 66 9.5 - - - - 26.0 - - - 67 9.5 - - - - 26.7 - - - 68 10.0 - - - - 26.4 - - - 69 10.0 - - - - 26.4 - - - - 70 10.0 - - - - 26.4 - - - 71 9.5 - - - - 27.2 - - - 72 10.0 - - - - 27.0 - - - 73 10.0 - - - - 27.0 - - - 74 10.0 - - - 27.0 - - - 75 10.0 - - - - 27.0 - - - 76 9.5 - - - - 28.7 - - - 77 9.5 - - - - 30.1 - - - 78 9.5 - - - - 31.5 - - - 79 9.5 - - - - 32.9 - - - 80 9.5 - - - - 34.9 - - - 81 9.5 - - - - 34.7 - - - 82 10.0 - - - - 34.3 - - - 83 10.0 - - - - 33.9 - - - 84 10.0 - - - - 32.1 - - - 85 9.5 - - - - 34.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\EUILDING 1 - 2ND FLOOR ATTIC.SDF JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 86 9.5 - - - - 34.4 - - 87 9.5 - - - - 34.3 - - - TOP 9.5 - - - - 35.3 - - - MID 4.0 - - - - 37.9 - - - BTM 1.0 - - - - 39.2 - - - Ui -4.0 - - - - 41.4 - - - U2 -4.0 - - - - 41.5 - - - U3 -4.0 - - - - 41.5 - - - U4 3.0 - - - - 38.5 - - - U5 3.0 - - - - 46.5 - - - U6 -4.0 - - - - 49.5 - - - SRC -4.0 SOURCE 49.5 53.0 Ii SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 1.101 PL 2.25 PF 0.0 1 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 0.0 2 30.0 0.0 9.6 0.0 0.000 TL 9.25 PV Pipe: 2 -0.8 1.101 PL 2.25 PF 0.0 2 30.0 0.0 9.6 0.0 0.3 150 FTG ---- PE 0.0 3 30.0 0.0 9.6 0.0 0.000 TL 2.25 PV Pipe: 3 0.8 1.101 PL 8.00 PF 0.0 2 30.0 0.0 9.6 0.0 0.3 150 FTG 2FT PE 0.0 4 30.0 0.0 9.6 0.0 0.000 TL 15.00 PV Pipe: 4 0.0 1.101 PL 10.00 PF 0.0 4 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 5 30.0 0.0 9.6 0.0 0.000 TL 15.00 PV Pipe: 5 0.0 1.101 PL 0.75 PF 0.0 5 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 9.6 0.0 0.000 TL 5.75 PV Pipe: 6 0.0 1.101 PL 3.00 PF 0.0 6 30.0 0.0 9.6 0.0 0.0 150 FTG B PE -1.3 7 33.0 0.0 8.3 0.0 0.000 TL 10.00 PV Pipe: 7 0.0 1.101 PL 8.50 PF 0.0 5 30.0 0.0 9.6 0.0 0.0 150 FTG ---- PE 0.0 8 30.0 0.0 9.6 0.0 0.000 TL 8.50 PV Pipe: 8 0.0 1.101 PL 8.75 PF 0.0 8 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 9.6 0.0 0.000 TL 13.75 PV Pipe: 9 0.0 1.101 PL 7.75 PF 0.0 30.0 0.0 9.6 0.0 0.0 150 FTG ---- PE 0.0 10 30.0 0.0 9.6 0.0 0.000 TL 7.75 PV Pipe: 10 0.8 1.101 PL 3.75 PF 0.0 4 30.0 0.0 9.6 0.0 0.3 150 FTG ---- PE 0.0 11 30.0 0.0 9.6 0.0 0.000 TL 3.75 PV Pipe: 11 0.0 1.101 PL 16.25 PP 0-.0- 11 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 9.6 0.0 0.000 TL 21.25 PV Pipe: 12 0.0 1.101 PL 7.25 PF 0.0 12 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 0.0 13 30.0 0.0 9.6 0.0 0.000 TL 14.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\EUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 13 0.0 1.101 PL 2.00 PF 0.0 12 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 14 30.0 0.0 9.6 0.0 0.000 TL 7.00 PV Pipe: 14 0.8 1.101 PL 0.50 PF 0.0 11 30.0 0.0 9.6 0.0 0.3 150 FTG ---- PE 0.0 15 30.0 0.0 9.6 0.0 0.000 TL 0.50 PV Pipe: 15 0.0 1.101 PL 4.00 PF 0.0 15 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 16 30.0 0.0 9.6 0.0 0.000 TL 9.00 PV Pipe: 16 0.0 1.101 PL 2.25 PF 0.0 16 30.0 0.0 9.6 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 9.6 0.0 0.000 TL 7.25 PV Pipe: 17 0.0 1.101 PL 6.50 PF 0.0 16 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 0.0 18 30.0 0.0 9.6 0.0 0.000 TL 13.50 PV Pipe: 18 0.0 1.101 PL 3.00 PF 0.0 18 30.0 0.0 9.6 0.0 0.0 150 FTG E PE -1.3 19 33.0 0.0 8.3 0.0 0.000 TL 10.00 PV Pipe: 19 0.8 1.101 PL 1.50 PF 0.0 15 30.0 0.0 9.6 0.0 0.3 150 FTG ---- PE 0.0 20 30.0 0.0 9.6 0.0 0.000 TL 1.50 PV Pipe: 20 18.9 1.101 PL 2.25 PF 0.4 20 30.0 0.0 9.6 0.0 6.4 150 FTG T PE 0.0 21 30.0 0.0 9.2 0.0 0.061 TL 7.25 PV Pipe: 21 -18.0 1.101 PL 3.00 PF 0.2 20 30.0 0.0 9.6 0.0 6.1 150 FTG ---- PE 0.0 22 30.0 0.0 9.8 0.0 0.056 TL 3.00 PV Pipe: 22 0.0 1.101 PL 1.50 PF 0.0 22 30.0 0.0 9.8 0.0 0.0 150 FTG T PE 0.0 23 30.0 0.0 9.8 0.0 0.000 TL 6.50 PV Pipe: 23 -18.0 1.101 PL 4.00 PF 0.3 22 30.0 0.0 9.8 0.0 6.1 150 FTG 2F PE 0.0 24 30.0 0.0 10.1 0.0 0.056 TL 6.00 PV Pipe: 24 -18.0 1.101 PL 28.50 PF 2.5 24 30.0 0.0 10.1 0.0 6.1 150 FTG 2F2E PE 0.0 25 30.0 0.0 12.6 0.0 0.056 TL 44.50 PV Pipe: 25 -18.0 1.101 PL 26.00 PF 2.4 25 30.0 0.0 12.6 0.0 6.1 150 FTG 2F2E PE 0.0 26 30.0 0.0 15.0 0.0 0.056 TL 42.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. (FT) (K) (PSI) (GPM) FL/FT - (PST) Pipe: 26 -18.0 1.101 PL 26.00 PF 2.4 26 30.0 0.0 15.0 0.0 6.1 150 FTG 2F2E PE 0.0 27 30.0 0.0 17.3 0.0 0.056 TL 42.00 PV Pipe: 27 -18.0 1.101 PL 26.00 PF 2.4 27 30.0 0.0 17.3 0.0 6.1 150 FTG 2F2E PE 0.0 28 30.0 0.0 19.7 0.0 0.056 TL 42.00 PV Pipe: 28 -18.0 1.101 PL 22.50 PF 2.2 28 30.0 0.0 19.7 0.0 6.1 150 FTG 2F2E PE 0.0 29 30.0 0.0 21.9 0.0 0.056 TL 38.50 PV Pipe: 29 -9.1 1.101 PL 36.25 PF 1.0 29 30.0 0.0 21.9 0.0 3.1 150 FTG 2E2T PE 0.0 30 30.0 0.0 22.8 0.0 0.016 TL 60.25 PV Pipe: 30 -8.9 1.101 PL 7.75 PF 0.1 29 30.0 0.0 21.9 0.0 3.0 150 FTG 2F PE 0.0 31 30.0 0.0 22.0 0.0 0.015 TL 9.75 PV Pipe: 31 -8.9 1.101 PL 3.50 PP 0.1 31 30.0 0.0 22.0 0.0 3.0 150 FTG T PE 0.0 32 30.0 0.0 22.1 0.0 0.015 TL 8.50 PV Pipe: 32 -8.9 1.101 PL 10.00 PP 0.3 32 30.0 0.0 22.1 0.0 3.0 150 FTG E PE 4.3 33 20.0 0.0 26.7 0.0 0.015 TL 17.00 PV Pipe: 33 -8.9 1.101 PL 21.25 PP 0.4 33 20.0 0.0 26.7 0.0 3.0 150 FTG 4F PE 0.0 34 20.0 0.0 27.1 0.0 0.015 TL 25.25 PV Pipe: 34 -8.9 1.101 PL 21.25 PF 0.4 34 20.0 0.0 27.1 0.0 3.0 150 FTG 4F PE 0.0 35 20.0 0.0 27.5 0.0 - 0.015 TL 25.25 - PV Pipe: 35 -8.9 1.101 PL 10.00 PP 0.3 35 20.0 0.0 27.5 0.0 3.0 150 FTG E PE -4.3 36 30.0 0.0 23.4 0.0 0.015 TL 17.00 PV Pipe: 36 -8.9 1.101 PL 6.50 PF 0.2 36 30.0 0.0 23.4 0.0 3.0 150 FTG E PE 0.0 37 .....30.0 0.0 23.6 0.0 0.015 TL 13.50 PV - . . . Pipe: 37 -8.9 1.101 FL 38.75 PF 0.9 37 30.0 0.0 23.6 0.0 3.0 150 FTG E3T PE 0.0 38 30.0 0.0 24.6 0.0 0.015 TL 60.75 PV Pipe: 38 -8.9 1.101 PL 10.00 PP 0.3 38 30.0 0.0 24.6 0.0 3.0 150 FTG E FE 4.3 39 20.0 0.0 29.1 0.0 0.015 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 -8.9 1.101 PL 5.25 PF 0.2 39 20.0 0.0 29.1 0.0 3.0 150 FTG E PE 0.0 40 20.0 0.0 29.3 0.0 0.015 TL 12.25 PV Pipe: 40 -9.1 1.101 PL 10.00 PF 0.3 30 30.0 0.0 22.8 0.0 3.1 150 FTG E PE 4.3 41 20.0 0.0 27.4 0.0 0.016 TL 17.00 PV Pipe: 41 0.0 1.101 PL 10.00 PF 0.0 10 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 4.3 42 20.0 0.0 13.9 0.0 0.000 TL 17.00 PV Pipe: 42 0.0 1.101 PL 5.00 PF 0.0 42 20.0 0.0 13.9 0.0 0.0 150 FTG 2E PE 0.0 43 20.0 0.0 13.9 0.0 0.000 TL 19.00 PV Pipe: 43 0.0 1.101 PL 10.00 PF 0.0 14 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 4.3 44 20.0 0.0 13.9 0.0 0.000 TL 17.00 PV Pipe: 44 0.0 1.101 PL 8.00 PF 0.0 44 20.0 0.0 13.9 0.0 0.0 150 FTG 2E PE 0.0 45 20.0 0.0 13.9 0.0 0.000 TL 22.00 PV Pipe: 45 0.0 1.101 PL 10.00 PF 0.0 17 30.0 0.0 9.6 0.0 0.0 150 FTG E PE 4.3 46 20.0 0.0 13.9 0.0 0.000 TL 17.00 PV Pipe: 46 0.0 1.101 PL 3.50 PP 0.0 46 20.0 0.0 13.9 0.0 0.0 150 FTG 2E PE 0.0 47 20.0 0.0 13.9 0.0 0.000 TL 17.50 PV Pipe: 47 18.9 1.101 PL 10.00 PF 1.0 21 30.0 0.0 9.2 0.0 6.4 150 FTG E PE 4.3 48 20.0 0.0 12.5 0_0 0.061 TL 17.00 PV Pipe: 48 18.9 1.101 PL 1.25 PF 0.5 48 20.0 0.0 12.5 0.0 6.4 150 FTG E PE 0.0 49 20.0 0.0 12.0 0.0 0.061 TL 8.25 PV Pipe: 49 0.0 1.101 PL 4.00 PF 0.0 49 20.0 0.0 12.0 0.0 0.0 150 FTG FT PE 0.0 50 20.0 0.0 12.0 0.0 0.000 TL 16.00 PV Pipe: 50 18.9 1.101 PL 9.25 PF 0.6 49 20.0 0.0 12.0 0.0 6.4 150 FTG ---- PE 0.0 51 20.0 0.0 11.4 0.0 0.061 TL 9.25 PV Pipe: 51 13.0 1.101 PL 2.50 PP 0.4 51 20.0 0.0 11.4 0.0 4.4 150 FTG ET PE 0.0 52 20.0 0.0 11.0 0.0 0.031 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 13.0 1.101 PL 2.50 PF 0.3 52 20.0 0.0 11.0 0.0 4.4 150 FTG E PE -1.1 53 22.5 4.2 9.6 13.0 0.031 TL 9.50 PV Pipe: 53 5.9 1.101 PL 5.75 PP 0.1 51 20.0 0.0 11.4 0.0 2.0 150 FTG E PE 0.0 54 20.0 0.0 11.3 0.0 0.007 TL 12.75 PV Pipe: 54 13.1 1.101 PL 2.25 PF 0.2 54 20.0 0.0 11.3 0.0 4.4 150 FTG T PE 0.0 55 20.0 0.0 11.1 0.0 0.031 TL 7.25 PV Pipe: 55 13.1 1.101 PL 2.50 PP 0.3 55 20.0 0.0 11.1 0.0 4.4 150 FTG E PE -1.1 56 22.5 4.2 9.7 13.1 0.031 TL 9.50 PV Pipe: 56 -7.2 1.101 PL 5.00 PP 0.1 54 20.0 0.0 11.3 0.0 2.4 150 FTG ---- PE 0.0 57 20.0 0.0 11.4 0.0 0.010 TL 5.00 PV Pipe: 57 13.1 1.101 PL 2.25 PF 0.2 57 20.0 0.0 11.4 0.0 4.4 150 FTG T PE 0.0 58 20.0 0.0 11.1 0.0 0.031 TL 7.25 PV Pipe: 58 13.1 1.101 PL 2.50 PP 0.3 58 20.0 0.0 11.1 0.0 4.4 150 FTG E PE -1.1 59 22.5 4.2 9.8 13.1 0.031 TL 9.50 PV Pipe: 59 -20.4 1.101 PL 7.75 PP 1.0 57 20.0 0.0 11.4 0.0 6.9 150 FTG E PE 0.0 60 20.0 0.0 12.4 0.0 0.070 TL 14.75 PV Pipe: 60 13.8 1.101 PL 0.50 PF 0.2 60 20.0 0.0 12.4 0.0 4.7 150 FTG T PE 0.0 61 20.0 0.0 12.2 0.0 0.034 TL 5.50 PV Pipe: 61 13.8 1.101 PL 2.50 PF 0.3 61 20.0 0.0 12.2 0.0 4.7 150 FTG E PE -1.1 62 22.5 4.2 10.8 13.8 0.034 TL 9.50 PV Pipe: 62 -34.2 1.101 PL 8.50 PF 1.6 60 20.0 0.0 12.4 0.0 11.5 150 FTG ---- PE 0.0 63 20.0 0.0 14.0 0.0 0.183 TL 8.50 PV Pipe: 63 0.8 1.101 PL 2.50 PF 0.0 63 20.0 0.0 14.0 0.0 0.3 150 FTG ---- PE 0.0 64 20.0 0.0 14.0 0.0 0.000 TL 2.50 PV Pipe: 64 -0.8 1.101 PL 10.00 PP 0.0 3 30.0 0.0 9.6 0.0 0.3 150 FTG 2E PE 4.3 64 20.0 0.0 14.0 0.0 0.000 TL 24.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 -35.0 1.101 PL 2.75 PF 1.5 63 20.0 0.0 14.0 0.0 11.8 150 FTG T PE 0.0 65 20.0 0.0 15.4 0.0 0.191 TL 7.75 PV Pipe: 66 -35.0 1.101 FL 10.50 PF 6..0 65 20.0 0.0 15.4 0.0 11.8 150 FTG 3E PE 4.5 66 9.5 0.0 26.0 0.0 0.191 TL 31.50 PV Pipe: 67 -35.0 1.654 PL 7.00 PF 0.6 66 9.5 0.0 26.0 0.0 5.2 120 FTG T PE 0.0 67 9.5 0.0 26.7 0.0 0.040 TL 16.12 PV Pipe: 68 0.0 1.083 PL 0.50 PF 0.0 67 9.5 0.0 26.7 0.0 0.0 120 FTG E PE -0.2 68 10.0 0.0 26.4 0.0 0.000 TL 2.84 PV Pipe: 69 0.0 1.083 PL 1.50 PF 0.0 68 10.0 0.0 26.4 0.0 0.0 120 FTG ---- PE 0.0 69 10.0 0.0 26.4 0.0 0.000 TL 1.50 PV Pipe: 70 0.0 1.083 FL 10.00 PF 0.0 69 10.0 0.0 26.4 0.0 0.0 120 FTG ---- PE 0.0 70 10.0 0.0 26.4 0.0 0.000 TL 10.00 PV Pipe: 71 -35.0 1.654 FL 13.25 PF 0.5 67 9.5 0.0 26.7 0.0 5.2 120 FTG ---- PE 0.0 71 9.5 0.0 27.2 0.0 0.040 TL 13.25 PV Pipe: 72 0.0 1.083 FL 0.50 PF 0.0 71 9.5 0.0 27.2 0.0 0.0 120 FTG T PE -0.2 72 10.0 0.0 27.0 0.0 0.000 TL 6.34 PV Pipe: 73 0.0 1.083 FL 1.50 PF 0.0 72 10.0 0.0 27.0 0.0 0.0 120 FTG T PE 0.0 7.3 10.0 0.0. 27,0 0.0 0.000 TL 7.3.4 RV Pipe: 74 0.0 1.083 PL 3.00 PF 0.0 73 10.0 0.0 27.0 0.0 0.0 120 FTG T FE 0.0 74 10.0 0.0 27.0 0.0 0.000 TL 8.84 PV Pipe: 75 0.0 1.083 PL 13.00 PF 0.0 73 10.0 0.0 27.0 0.0 0.0 120 FTG E PE 0.0 75 10.0 0.0 27.0 0.0 0.000 TL 15.34 PV Pipe: 76 -35.0 1.654 PL 30.00 PF 1.6 71 9.5 0.0 27.2 0.0 5.2 120 FTG 2E PE 0.0 76 9.5 0.0 28.7 0.0 0.040 TL 39.12 PV Pipe: 77 -35.0 1.654 FL 26.00 PF 1.4 76 9.5 0.0 28.7 0.0 5.2 120 FTG 2E PE 0.0 77 9.5 0.0 30.1 0.0 0.040 TL 35.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOE TITLE: 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 -35.0 1.654 PL 26.00 PF 1.4 77 9.5 0.0 30.1 0.0 5.2 120 FTG 2E PE 0.0 78 9.5 0.0 31.5 0.0 0.040 TL 35.12 PV Pipe: 79 -35.0 1.654 PL 26.00 PF 1.4 78 9.5 0.0 31.5 0.0 5.2 120 FTG 2E PE 0.0 79 9.5 0.0 32.9 0.0 0.040 TL 35.12 PV Pipe: 80 -35.0 1.654 PL 29.75 PF 1.9 79 9.5 0.0 32.9 0.0 5.2 120 FTG 4E PE 0.0 80 9.5 0.0 34.9 0.0 0.040 TL 47.99 PV Pipe: 81 18.0 1.654 PL 4.25 PF 0.2 80 9.5 0.0 34.9 0.0 2.7 120 FTG T PE 0.0 81 9.5 0.0 34.7 0.0 0.012 TL 13.37 PV Pipe: 82 9.1 1.083 PL 0.50 PF 0.2 81 9.5 0.0 34.7 0.0 3.2 120 FTG T PE -0.2 82 10.0 0.0 34.3 0.0 0.026 TL 6.34 PV Pipe: 83 9.1 1.083 PL 6.75 PF 0.4 82 10.0 0.0 34.3 0.0 3.2 120 FTG ET PE 0.0 83 10.0 0.0 33.9 0.0 0.026 TL 14.93 PV Pipe: 84 9.1 1.101 PL 57.25 PF 1.8 83 10.0 0.0 33.9 0.0 3.1 120 FTG 2E3T PE 0.0 84 10.0 0.0 32.1 0.0 0.024 TL 76.44 PV Pipe: 85 -9.1 1.101 PL 10.00 PF 0.4 41 20.0 0.0 27.4 0.0 3.1 120 FTG E PE 4.3 84 10.0 0.0 32.1 0.0 0.024 TL 14.63 PV Pipe: 86 8.9 1.654 FL 37.00 PF 0.2 81 9.5 0.0 34.7 0.0 1.3 120 FTG 4E PE 0.0 85 9.5 0.0 34.5 0.0 0.003 TL 55.24 PV Pipe: 87 8.9 1.654 PL 31.50 PF 0.1 85 9.5 0.0 34.5 0.0 1.3 120 FTG E PE 0.0 86 9.5 0.0 34.4 0.0 0.003 TL 36.06 PV Pipe: 88 8.9 1.654 PL 16.75 PF 0.1 86 9.5 0.0 34.4 0.0 1.3 120 FTG E FE 0.0 87 9.5 0.0 34.3 0.0 0.003 TL 21.31 PV Pipe: 89 -8.9 1.101 FL 10.50 PF 0.5 40 20.0 0.0 29.3 0.0 3.0 120 FTG 2E PE 4.5 87 9.5 0.0 34.3 0.0 0.023 TL 19.76 PV Pipe: 90 -53.0 2.705 FL 17.75 PF 0.4 80 9.5 0.0 34.9 0.0 3.0 120 FTG 2ET PE 0.0 TOP 9.5 0.0 35.3 0.0 0.008 TL 55.19 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 -53.0 2.705 PL 5.50 PP 0.2 TOP 9.5 0.0 35.3 0.0 3.0 120 FTG C PE 2.4 MID 4.0 0.0 37.9 0.0 0.008 TL 27.34 PV Pipe: 92 -53.0 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 37.9 0.0 3.0 120 FTG ---- PE 1.3 BTM 1.0 0.0 39.2 0.0 0.008 TL 3.00 PV Pipe: 93 -53.0 4.026 PL 10.00 PF 0.0 BTM 1.0 0.0 39.2 0.0 1.3 120 FTG E PE 2.2 Ui -4.0 0.0 41.4 0.0 0.001 TL 20.00 PV Pipe: 94 -53.0 4.240 PL 43.80 PF 0.1 Ui -4.0 0.0 41.4 0.0 1.2 150 FTG 3E PE 0.0 U2 -4.0 0.0 41.5 0.0 0.001 TL 103.80 PV Pipe: 95 -53.0 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 41.5 0.0 1.2 150 FTG ---- PE 0.0 U3 -4.0 0.0 41.5 0.0 0.001 TL 3.50 PV Pipe: 96 -53.0 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 41.5 0.0 1.2 140 FTG 2E PE -3.0 U4 3.0 0.0 38.5 0.0 0.001 TL 41.00 PV Pipe: 97 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 46.5 0.0 8.0 psi, 53.0 gpm U4 3.0 0.0 38.5 0.0 Pipe: 98 -53.0 4.220 PL 7.00 PF 0.0 U5 3.0 0.0 46.5 0.0 1.2 140 FTG E PE 3.0 U6 -4.0 0.0 49.5 0.0 0.001 TL 24.00 PV Pipe: 99 -53.0 4.240 PL 22.50 PP 0.0 U6 -4.0 0.0 49.5 0.0 1.2 150 FTG E PE 0.0 SRC - -4.0 SRCE 49.5 (N/A) 0.001 TL 42.50 PV NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 11.8 ft/sec at pipe 65. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: 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 84.21 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP 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 DPViv NPTee 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AimChk NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOE TITLE: PAGE: X MATERIAL: EdFlw HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyViv GatViv AimChk DPViv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 0 0 (N I I I I I I I I I 0 I I 1 I .1 I I / I I / I 0 / 0 40, II / I / / SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: E i) 000 U)Q (0 k •,0 (0 (0 Q (O LO (OLOQf0(0 Q )- Cfl-1QE If) 0) 0(0(0 (0)(0 0,-4 .0 (0-1 H(0c0 —1U) (OUW-1 .00 o --l(00> HLfl 0U)C/)C0 44 LD0 . (0 CD 04 Ln Ln co 04 4J 0 0 10 0 0 0 0 0 0 0 0 o 0 0 0 0 OD '.0 (0' (N < ZD LJ J)U)M —0-(J--1---- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR ATTIC.SDF JOB TITLE: MATER SUPPLY CURVE 96+ 88+ *\ I \ 80+ \ I \ I \ I \\ 72+ \ I \ I \ P 64+ \ R \ E I \\ S \ 5 56+ \ U \ R E PC \ 48+ \\ P I \ S I \ I 40+ \ I \\ 32+ \ \ 24+ * <-20.0 psi @ 1500 gpm I Flow Test Point 16+ LEGEND I X = Required Mater Supply I 49.53 psi 8 153.0 gpm 8+ I 0 = Available Mater Supply I 84.54 psi 8 153.0 gpm U +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 1 - 2ND FLOOR RESIDENTIAL FILE NUMBER: 9301 DATE: FEB 19, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 4 HEADS 8 18'X18' COVERAGE PER SPRINKLER: 18TX18T NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 70.3 gpm TOTAL WATER REQUIRED (including hose) : 170.3 gpm FLOW AND PRESSURE (8 BOR) : 70.3 gpm @ 55.2 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC. DESIGN/LAYOUT BY: RAFAEL E. AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C-16 #786965 CALCULATIONS BYHASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 85.5 20.0 1500.0 84.3 170.3 65.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 170.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 70.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 12.5 - - - 2 30.0 - - - - 12.5 - - - 3 30.0 - - - - 12.7 - - - 4 30.0 - - - - 11.1 - - - 5 30.0 - - - - 10.4 - - - 6 30.0 - - - - 10.4 - - - 7 33.0 - - - - 9.1 - - - 8 30.0 - - - - 9.9 - - - 9 30.0 - - - - 9.9 - - - 10 30.0 - - - - 9.5 - - - 11 30.0 - - - - 11.1 - - - 12 30.0 - - - - 10.0 - - - 13 30.0 - - - - 10.0 - - - 14 30.0 - - - - 9.7 - - - 15 30.0 - - - - 11.1 - - - 16 30.0 - - - - 10.6 - - - 17 30.0 - - - 10.2 - - - 18 30.0 - - - - 10.6 - - - 19 33.0 - - - - 9.3 - - - 20 30.0 - - - - 11.3 - - - 21 30.0 - - - - 11.3 - - - 22 30.0 - - - - 11.6 - - - 23 30.0 - - - - 11.6 - - - 24 30.0 - - - - 12.2 - - - 25 30.0 - - - - 16.8 - - - 26 30.0 - - - - 21.2 - - - 27 30.0 - - - - 25.5 - - - 28 30.0 - - - - 29.9 - - - 29 30.0 - - - - 33.9 - - - 30 30.0 - - - - 35.6 - - - 31 30.0 - - - - 34.1 - - - 32 30.0 - - - - 34.4 - - - 33 20.0 - - - - 39.2 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 20.0 - - - - 39.9 - - - 35 20.0 - - - - 40.6 - - 36 30.0 - - - - 36.8 - - - 37 30.0 - - - - 37.1 - - - 38 30.0 - - - - 38.9 - - - 39 20.0 - - - - 43.7 - - - 40 20.0 - - - - 44.0 - - - 41 20.0 - - - - 40.5 - - - 42 20.0 - - - - 13.0 - - - 43 20.0 K= 4.90 12.1 17.0 44 20.0 - - - - 13.1 - - - 45 20.0 K= 4.90 12.0 17.0 46 20.0 - - - - 13.7 - - - 47 20.0 K= 4.90 12.7 17.5 48 20.0 - - - - 15.7 - - - 49 20.0 - - - - 15.7 - - - 50 20.0 K= 4.90 14.7 18.8 51 20.0 - - - - 16.4 - - - 52 20.0 - - - - 16.4 - - - 53 22.5 - - - - 15.3 - - - 54 20.0 - - - - 17.4 - - - 55 20.0 - - - - 17.4 - - - 56 22.5 - - - - 16.3 - - - 57 20.0 - - - - 17.8 - - - 58 20.0 - - - - 17.8 - - - 59 22.5 - - - - 16.7 - - - 60 20.0 - - - - 18.9 - - - 61 20.0 - - - - 18.9 - - - 62 22.5 - - - - 17.8 - - - 63 20.0 - - - - 19.6 - - - 64 20.0 - - - 19.3 - - - 65 20.0 - - - - 21.9 - - - 66 9.5 - - - - 36.2 - - - 67 9.5 - - - - 37.2 - - - 68 10.0 - - - - 37.0 - - - 69 10.0 - - - - 37.0 - - - 70 10.0 - - - - 37.0 - - - 71 9.5 - - - - 38.0 - - - 72 10.0 - - - - 37.8 - - - 73 10.0 - - - - 37.8 - - - 74 10.0 - - - - 37.8 - - - 75 10.0 - - - - 37.8 - - - 76 9.5 - - - 40.5 -- - - 77 9.5 - - - - 42.8 - - - 78 9.5 - - - - 45.0 - - - 79 9.5 - - - - 47.3 - - - 80 9.5 - - - - 50.4 - - - 81 9.5 - - - - 50.1 - - - 82 10.0 - - - - 49.5 - - - 83 10.0 - - - - 48.8 - - - 84 10.0 - - - - 45.4 - - - 85 9.5 - - - - 49.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/19/2016KLER5\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 86 9.5 - - - - 49.5 - - - 87 9.5 - - - - 49.4 - - - TOP 9.5 - - - - 51.1 - - - MID 4.0 - - - - 53.8 - - - BTM 1.0 - - - - 55.2 - - - Ui -4.0 - - - - 57.4 - - - U2 -4.0 - - - - 57.5 - - - U3 -4.0 - - - - 57.5 - - - U4 3.0 - - - - 54.5 - - - U5 3.0 - - - - 62.5 - - - U6 -4.0 - - - - 65.6 - - - SRC -4.0 SOURCE 65.6 70.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HN(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 2.25 PF 0.0 1 30.0 0.0 12.5 0.0 0.0 150 FTG E PE 0.0 2 30.0 0.0 12.5 0.0 0.000 TL 9.25 PV Pipe: 2 -23.8 1.101 PL 2.25 PF 0.2 2 30.0 0.0 12.5 0.0 8.0 150 FTG ----- PE 0.0 3 30.0 0.0 12.7 0.0 0.094 TL 2.25 PV Pipe: 3 23.8 1.101 PL 8.00 PF 1.4 2 30.0 0.0 12.5 0.0 8.0 150 FTG 2FT PE 0.0 4 30.0 0.0 11.1 0.0 0.094 TL 15.00 PV Pipe: 4 17.0 1.101 PL 10.00 PF 0.8 4 30.0 0.0 11.1 0.0 5.7 150 FTG T PE 0.0 5 30.0 0.0 10.4 0.0 0.050 TL 15.00 PV Pipe: 5 0.0 1.101 PL 0.75 PF 0.0 5 30.0 0.0 10.4 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 10.4 0.0 0.000 TL 5.75 PV Pipe: 6 0.0 1.101 PL 3.00 PF 0.0 6 30.0 0.0 10.4 0.0 0.0 150 FTG E PE -1.3 7 33.0 0.0 9.1 0.0 0.000 TL 10.00 PV Pipe: 7 17.0 1.101 PL 8.50 PF 0.4 5 30.0 0.0 10.4 0.0 5.7 150 FTG ---- PE 0.0 8 30.0 0.0 9.9 0.0 0.050 TL 8.50 PV Pipe: 8 0.0 1.101 PL 8.75 PF 0.0 8 30.0 0.0 9.9 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 9.9 0.0 0.000 TL 13.75 PV Pipe: 9 17.0 1.101 PL - 7.75 PF 0.4 -8 30:0 0.0 9'.9 0.0 5.7 150 FTG ---- PE 0.0 10 30.0 0.0 9.5 0.0 0.050 TL 7.75 PV Pipe: 10 6.7 1.101 PL 3.75 PF 0.0 4 30.0 0.0 11.1 0.0 2.3 150 FTG ---- PE 0.0 11 30.0 0.0 11.1 0.0 0.009 TL 3.75 PV Pipe: 11- 17.0 1.101 PL 16.25 PF 1.1 11 30.0 0.0 11.1 0.0 5.7 150 FTG T FE 0.0 12 30.0 0.0 10.0 0.0 0.050 TL 21.25 PV Pipe: 12 0.0 1.101 PL 7.25 PF 0.0 12 30.0 0.0 10.0 0.0 0.0 150 FTG E PE 0.0 13 30.0 0.0 10.0 0.0 0.000 TL 14.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 17.0 1.101 PL 2.00 PF 0.4 12 30.0 0.0 10.0 0.0 5.7 150 FTG T PE 0.0 14 30.0 0.0 9.7 0.0 0.050 TL 7.00 PV Pipe: 14 -10.3 1.101 PL 0.50 PF 0.0 11 30.0 0.0 11.1 0.0 3.5 150 FTG ---- PE 0.0 15 30.0 0.0 11.1 0.0 0.020 TL 0.50 PV Pipe: 15 17.5 1.101 PL 4.00 PF 0.5 15 30.0 0.0 11.1 0.0 5.9 150 FTG T PE 0.0 16 30.0 0.0 10.6 0.0 0.053 TL 9.00 PV Pipe: 16 17.5 1.101 PL 2.25 PP 0.4 16 30.0 0.0 10.6 0.0 5.9 150 FTG T PE 0.0 17 30.0 0.0 10.2 0.0 0.053 TL 7.25 PV Pipe: 17 0.0 1.101 PL 6.50 PF 0.0 16 30.0 0.0 10.6 0.0 0.0 150 FTG E PE 0.0 18 30.0 0.0 10.6 0.0 0.000 TL 13.50 PV Pipe: 18 0.0 1.101 PL 3.00 PF 0.0 18 30.0 0.0 10.6 0.0 0.0 150 FTG E PE -1.3 19 33.0 0.0 9.3 0.0 0.000 TL 10.00 PV Pipe: 19 -27.7 1.101 PL 1.50 PF 0.2 15 30.0 0.0 11.1 0.0 9.3 150 FTG ---- PE 0.0 20 30.0 0.0 11.3 0.0 0.125 TL 1.50 PV Pipe: 20 -2.6 1.101 PL 2.25 PP 0.0 20 30.0 0.0 11.3 0.0 0.9 150 FTG T PE 0.0 21 30.0 0.0 11.3 0.0 0.002 TL 7.25 PV Pipe: 21 -25.1 1.101 PL 3.00 PF 0.3 20 30.0 0.0 11.3 0.0 8.5 150 FTG ---- PE 0.0 22 30.0 0.0 11.6 0.0 0.104 TL 3.00 PV Pipe: 22 0.0 1.101 PL 1.50 PF 0.0 22 30.0 0.0 11.6 0.0 0.0 150 FTG T PE 0.0 23 30.0 0.0 11.6 0.0 0.000 TL 6.50 PV Pipe: 23 -25.1 1.101 PL 4.00 PF 0.6 22 30.0 0.0 11.6 0.0 8.5 150 FTG 2F PE 0.0 24 30.0 0.0 12.2 0.0 0.104 TL 6.00 PV Pipe: 24 -25.1 1.101 PL 28.50 PP 4.6 24 30.0 0.0 12.2 0.0 8.5 150 FTG 2F2E PE 0.0 25 30.0 0.0 16.8 0.0 0.104 TL 44.50 PV Pipe: 25 -25.1 1.101 PL 26.00 PP 4.4 25 30.0 0.0 16.8 0.0 8.5 150 FTG 2P2E PE 0.0 26 30.0 0.0 21.2 0.0 0.104 TL 42.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 -25.1 1.101 PL 26.00 PP 4.4 26 30.0 0.0 21.2 0.0 8.5 150 FTG 2F2E PE 0.0 27 30.0 0.0 25.5 0.0 0.104 TL 42.00 PV Pipe: 27 -25.1 1.101 PL 26.00 PF 4.4 27 30.0 0.0 25.5 0.0 8.5 150 FTG 2F2E PE 0.0 28 30.0 0.0 29.9 0.0 0.104 TL 42.00 PV Pipe: 28 -25.1 1.101 PL 22.50 PF 4.0 28 30.0 0.0 29.9 0.0 8.5 150 FTG 2F2E PE 0.0 29 30.0 0.0 33.9 0.0 0.104 TL 38.50 PV Pipe: 29 -12.7 1.101 PL 36.25 PF 1.8 29 30.0 0.0 33.9 0.0 4.3 150 FTG 2E2T PE 0.0 30 30.0 0.0 35.6 0.0 0.029 TL 60.25 PV Pipe: 30 -12.4 1.101 PL 7.75 PF 0.3 29 30.0 0.0 33.9 0.0 4.2 150 FTG 2F PE 0.0 31 30.0 0.0 34.1 0.0 0.028 TL 9.75 PV Pipe: 31 -12.4 1.101 PL 3.50 PF 0.2 31 30.0 0.0 34.1 0.0 4.2 150 FTG T PE 0.0 32 30.0 0.0 34.4 0.0 0.028 TL 8.50 PV Pipe: 32 -12.4 1.101 PL 10.00 PF 0.5 32 30.0 0.0 34.4 0.0 4.2 150 FTG E PE 4.3 33 20.0 0.0 39.2 0.0 0.028 TL 17.00 PV Pipe: 33 -12.4 1.101 PL 21.25 PF 0.7 33 20.0 0.0 39.2 0.0 4.2 150 FTG 4F PE 0.0 34 20.0 0.0 39.9 0.0 0.028 TL 25.25 PV Pipe: 34 -12.4 1.101 PL 21.25 PP 0.7 34 20.0 0.0 39.9 0.0 4.2 150 FTG 4F PE 0.0 35 20.0 0.0 40.6 0.0 0.028 TL 25.25 PV Pipe: 35 -12.4 1.101 PL 10.00 PF 0.5 35 20.0 0.0 40.6 0.0 4.2 150 FTG E PE -4.3 36 30.0 0.0 36.8 0.0 0.028 TL 17.00 PV Pipe: 36 -12.4 1.101 PL 6.50 PP 0.4 36 30.0 0.0 36.8 0.0 4.2 150 FTG E PE 0.0 37 30.0 0.0 37.1 0.0 0.028 TL 13.50 PV Pipe: 37 -12.4 1.101 PL 38.75 PF 1.7 37 30.0 0.0 37.1 0.0 4.2 150 FTG E3T PE 0.0 38 30.0 0.0 38.9 0.0 0.028 TL 60.75 PV Pipe: 38 -12.4 1.101 PL 10.00 PF 0.5 38 30.0 0.0 38.9 0.0 4.2 150 FTG E PE 4.3 39 20.0 0.0 43.7 0.0 0.028 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 -12.4 1.101 PL 5.25 PF 0.3 39 20.0 0.0 43.7 0.0 4.2 150 FTG E PE 0.0 40 20.0 0.0 44.0 0.0 0.028 TL 12.25 PV Pipe: 40 -12.7 1.101 PL 10.00 PF 0.5 30 30.0 0.0 35.6 0.0 4.3 150 FTG E PE 4.3 41 20.0 0.0 40.5 0.0 0.029 TL 17.00 PV Pipe: 41 17.0 1.101 PL 10.00 PF 0.9 10 30.0 0.0 9.5 0.0 5.7 150 FTG E PE 4.3 42 20.0 0.0 13.0 0.0 0.050 TL 17.00 PV Pipe: 42 17.0 1.101 PL 5.00 PF 1.0 42 20.0 0.0 13.0 0.0 5.7 150 FTG 2E FE 0.0 43 20.0 4.9 12.1 17.0 0.050 TL 19.00 PV Pipe: 43 17.0 1.101 FL 10.00 PF 0.9 14 30.0 0.0 9.7 0.0 5.7 150 FTG E FE 4.3 44 20.0 0.0 13.1 0.0 0.050 TL 17.00 PV Pipe: 44 17.0 1.101 FL 8.00 PF 1.1 44 20.0 0.0 13.1 0.0 5.7 150 FTG 2E FE 0.0 45 20.0 4.9 12.0 17.0 0.050 TL 22.00 PV Pipe: 45 17.5 1.101 FL 10.00 PF 0.9 17 30.0 0.0 10.2 0.0 5.9 150 FTG E PE 4.3 46 20.0 0.0 13.7 0.0 0.053 TL 17.00 PV Pipe: 46 17.5 1.101 FL 3.50 PF 0.9 46 20.0 0.0 13.7 0.0 5.9 150 FTG 2E FE 0.0 47 20.0 4.9 12.7 17.5 0.053 TL 17.50 PV Pipe: 47 -2.6 1.101 FL 10.00 PF 0.0 21 30.0 0.0 11.3 0.0 0.9 150 FTG E FE 4.3 48 20.0 0.0 15.7 0.0 0.002 TL 17.00 PV Pipe: 48 -2.6 1.101 PL 1.25 PF 0.0 48 20.0 0.0 15.7 0.0 0.9 150 FTG E FE 0.0 49 20.0 0.0 15.7 0.0 0.002 TL 8.25 PV Pipe: 49 18.8 1.101 PL 4.00 PF 1.0 49 20.0 0.0 15.7 0.0 6.3 150 FTG ET FE 0.0 50 20.0 4.9 14.7 18:8 - 0.061 TL 16.00 PV Pipe: 50 -21.4 1.101 FL 9.25 PF 0.7 49 20.0 0.0 15.7 0.0 7.2 150 FTG ---- FE 0.0 51 20.0 0.0 16.4 0.0 0.077 TL 9.25 PV Pipe: 51 0.0 1.101 FL 2.50 PF 0.0 51 20.0 0.0 16.4 0.0 0.0 150 FTG ET FE 0.0 52 20.0 0.0 16.4 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 0.0 1.101 FL 2.50 PF 0.0 52 20.0 0.0 16.4 0.0 0.0 150 FTG E PE -1.1 53 22.5 0.0 15.3 0.0 0.000 TL 9.50 PV Pipe: 53 -21.4 1.101 PL 5.75 PF 1.0 51 20.0 0.0 16.4 0.0 7.2 150 FTG E PE 0.0 54 20.0 0.0 17.4 0.0 0.077 TL 12.75 PV Pipe: 54 0.0 1.101 FL 2.25 PF 0.0 54 20.0 0.0 17.4 0.0 0.0 150 FTG T PE 0.0 55 20.0 0.0 17.4 0.0 0.000 TL 7.25 PV Pipe: 55 0.0 1.101 FL 2.50 PF 0.0 55 20.0 0.0 17.4 0.0 0.0 150 FTG E FE -1.1 56 22.5 0.0 16.3 0.0 0.000 TL 9.50 PV Pipe: 56 -21.4 1.101 PL 5.00 PF 0.4 54 20.0 0.0 17.4 0.0 7.2 150 FTG ---- FE 0.0 57 20.0 0.0 17.8 0.0 0.077 TL 5.00 PV Pipe: 57 0.0 1.101 FL 2.25 PF 0.0 57 20.0 0.0 17.8 0.0 0.0 150 FTG T FE 0.0 58 20.0 0.0 17.8 0.0 0.000 TL 7.25 PV Pipe: 58 0.0 1.101 FL 2.50 PF 0.0 58 20.0 0.0 17.8 0.0 0.0 150 FTG E FE -1.1 59 22.5 0.0 16.7 0.0 0.000 TL 9.50 PV Pipe: 59 -21.4 1.101 FL 7.75 PF 1.1 57 20.0 0.0 17.8 0.0 7.2 150 FTG E FE 0.0 60 20.0 0.0 18.9 0.0 0.077 TL 14.75 PV Pipe: 60 0.0 1.101 FL 0.50 PF 0.0 60 20.0 0.0 18.9 0.0 0.0 150 FTG T FE 0.0 61 20.0 0.0 18.9 0.0 0.000 TL 5.50 PV Pipe: 61 0.0 1.101 FL 2.50 PF 0.0 61 20.0 0.0 18.9 0.0 0.0 150 FTG E PE -1.1 62 22.5 0.0 17.8 0.0 0.000 TL 9.50 PV • Pipe: 62 -21.4 1.101 FL 8.50 PF 0.7 60 20.0 0.0 18.9 0.0 7.2 150 FTG ---- FE 0.0 63 20.0 0.0 19.6 0.0 0.077 TL 8.50 FV Pipe: 63 23.8 1.101 FL 2.50 PF 0.2 63 20.0 0.0 19.6 0.0 8.0 150 FTG ---- PE 0.0 64 20.0 0.0 19.3 0.0 0.094 TL 2.50 PV Pipe: 64 -23.8 1.101 FL 10.00 PF 2.2 3 30.0 0.0 12.7 0.0 8.0 150 FTG 2E FE 4.3 64 20.0 0.0 19.3 0.0 0.094 TL 24.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 -45.2 1.101 PL 2.75 PF 2.4 63 20.0 0.0 19.6 0.0 15.2 150 FTG T PE 0.0 65 20.0 0.0 21.9 0.0 0.307 TL 7.75 PV Pipe: 66 -45.2 1.101 PL 10.50 PF 9.7 65 20.0 0.0 21.9 0.0 15.2 150 FTG 3E PE 4.5 66 9.5 0.0 36.2 0.0 0.307 TL 31.50 PV Pipe: 67 -45.2 1.654 PL 7.00 PF 1.0 66 9.5 0.0 36.2 0.0 6.7 120 FTG T PE 0.0 67 9.5 0.0 37.2 0.0 0.064 TL 16.12 PV Pipe: 68 0.0 1.083 PL 0.50 PF 0.0 67 9.5 0.0 37.2 0.0 0.0 120 FTG E FE -0.2 68 10.0 0.0 37.0 0.0 0.000 TL 2.84 PV Pipe: 69 0.0 1.083 FL 1.50 PF 0.0 68 10.0 0.0 37.0 0.0 0.0 120 FTG ---- FE 0.0 69 10.0 0.0 37.0 0.0 0.000 TL 1.50 FV Pipe: 70 0.0 1.083 PL 10.00 PF 0.0 69 10.0 0.0 37.0 0.0 0.0 120 FTG ---- FE 0.0 70 10.0 0.0 37.0 0.0 0.000 TL 10.00 FV Pipe: 71 -45.2 1.654 PL 13.25 PF 0.8 67 9.5 0.0 37.2 0.0 6.7 120 FTG ---- FE 0.0 71 9.5 0.0 38.0 0.0 0.064 TL 13.25 PV Pipe: 72 0.0 1.083 FL 0.50 PF 0.0 71 9.5 0.0 38.0 0.0 0.0 120 FTG T FE -0.2 72 10.0 0.0 37.8 0.0 0.000 TL 6.34 PV Pipe: 73 0.0 1.083 FL 1.50 PF 0.0 72 10.0 0.0 37.8 0.0 0.0 120 FTG T FE 0.0 73 10.0 0..0 37.5 0..0 0.000 TL7.3.4 PV Pipe: 74 0.0 1.083 FL 3.00 PF 0.0 73 10.0 0.0 37.8 0.0 0.0 120 FTG T FE 0.0 74 10.0 0.0 37.8 0.0 0.000 TL 8.84 PV Pipe: 75 0.0 1.083 FL 13.00 PF 0.0 73 10.0 0.0 37.8 0.0 0.0 120 FTG E FE 0.0 75 10.0 0.0 37.8 0.0 0.000 TL 15.34 PV Pipe: 76 -45.2 1.654 FL 30.00 PF 2.5 71 9.5 0.0 38.0 0.0 6.7 120 FTG 2E FE 0.0 76 9.5 0.0 40.5 0.0 0.064 TL 39.12 PV Pipe: 77 -45.2 1.654 FL 26.00 PF 2.2 76 9.5 0.0 40.5 0.0 6.7 120 FTG 2E FE 0.0 77 9.5 0.0 42.8 0.0 0.064 TL 35.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 78 -45.2 1.654 PL 26.00 PF 2.2 77 9.5 0.0 42.8 0.0 6.7 120 FTG 2E PE 0.0 78 9.5 0.0 45.0 0.0 0.064 TL 35.12 PV Pipe: 79 -45.2 1.654 PL 26.00 PF 2.2 78 9.5 0.0 45.0 0.0 6.7 120 FTG 2E PE 0.0 79 9.5 0.0 47.3 0.0 0.064 TL 35.12 PV Pipe: 80 -45.2 1.654 PL 29.75 PF 3.1 79 9.5 0.0 47.3 0.0 6.7 120 FTG 4E PE 0.0 80 9.5 0.0 50.4 0.0 0.064 TL 47.99 PV Pipe: 81 25.1 1.654 PL 4.25 PF 0.3 80 9.5 0.0 50.4 0.0 3.7 120 FTG T PE 0.0 81 9.5 0.0 50.1 0.0 0.022 TL 13.37 PV Pipe: 82 12.7 1.083 PL 0.50 PF 0.3 81 9.5 0.0 50.1 0.0 4.4 120 FTG T PE -0.2 82 10.0 0.0 49.5 0.0 0.048 TL 6.34 PV Pipe: 83 12.7 1.083 PL 6.75 PF 0.7 82 10.0 0.0 49.5 0.0 4.4 120 FTG ET PE 0.0 83 10.0 0.0 48.8 0.0 0.048 TL 14.93 PV Pipe: 84 12.7 1.101 PL 57.25 PF 3.4 83 10.0 0.0 48.8 0.0 4.3 120 FTG 2E3T PE 0.0 84 10.0 0.0 45.4 0.0 0.044 TL 76.44 PV Pipe: 85 -12.7 1.101 PL 10.00 PF 0.6 41 20.0 0.0 40.5 0.0 4.3 120 FTG E PE 4.3 84 10.0 0.0 45.4 0.0 0.044 TL 14.63 PV Pipe: 86 12.4 1.654 PL 37.00 PF 0.3 81 9.5 0.0 50.1 0.0 1.9 120 FTG 4E PE 0.0 85 9.5 0.0 49.7 0.0 0.006 TL 55.24 PV Pipe: 87 12.4 1.654 PL 31.50 PF 0.2 85 9.5 0.0 49.7 0.0 1.9 120 FTG E PE 0.0 86 9.5 0.0 49.5 0.0 0.006 TL 36.06 PV Pipe: 88 12.4 1.654 PL 16.75 PF 0.1 86 9.5 0.0 49.5 0.0 1.9 120 FTG E PE 0.0 87 9.5 0.0 49.4 0.0 0.006 TL 21.31 PV Pipe: 89 -12.4 1.101 PL 10.50 PF 0.8 40 20.0 0.0 44.0 0.0 4.2 120 FTG 2E PR 4.5 87 9.5 0.0 49.4 0.0 0.043 TL 19.76 PV Pipe: 90 -70.3 2.705 PL 17.75 PF 0.7 80 9.5 0.0 50.4 0.0 3.9 120 FTG 2ET PE 0.0 TOP 9.5 0.0 51.1 0.0 0.013 TL 55.19 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 2/19/2016KLER5\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 -70.3 2.705 PL 5.50 PF 0.4 TOP 9.5 0.0 51.1 0.0 3.9 120 FTG C PE 2.4 MID 4.0 0.0 53.8 0.0 0.013 TL 27.34 PV Pipe: 92 -70.3 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 53.8 0.0 3.9 120 FTG ---- PE 1.3 BTM 1.0 0.0 55.2 0.0 0.013 TL 3.00 PV Pipe: 93 -70.3 4.026 PL 10.00 PF 0.0 BTM 1.0 0.0 55.2 0.0 1.8 120 FTG E PE 2.2 Ui -4.0 0.0 57.4 0.0 0.002 TL 20.00 PV Pipe: 94 -70.3 4.240 PL 43.80 PF 0.1 Ui -4.0 0.0 57.4 0.0 1.6 150 FTG 3E PE 0.0 U2 -4.0 0.0 57.5 0.0 0.001 TL 103.80 PV Pipe: 95 -70.3 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 57.5 0.0 1.6 150 FTG ---- PE 0.0 U3 -4.0 0.0 57.5 0.0 0.001 TL 3.50 PV Pipe: 96 -70.3 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 57.5 0.0 1.6 140 FTG 2E PE -3.0 U4 3.0 0.0 54.5 0.0 0.001 TL 41.00 PV Pipe: 97 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 62.5 0.0 8.0 psi, 70.3 gpm U4 3.0 0.0 54.5 0.0 Pipe: 98 -70.3 4.220 PL 7.00 PF 0.0 U5 3.0 0.0 62.5 0.0 1.6 140 FTG E PE 3.0 U6 -4.0 0.0 65.6 0.0 0.001 TL 24.00 PV Pipe: 99 -70.3 4.240 PL 22.50 PP 0.0 U6 -4.0 0.0 65.6 0.0 1.6 150 FTG E PE 0.0 SRC -4.0 SRCE 65.6 (N/A) 0.001 TL 42.50 PV NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.198 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 15.2 ft/sec at pipe 66. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 84.15 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEil ChkVlv BfyVlv GatVlv NPTee 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Eli Tee LngEli ChkVlv BfyVlv GatVlv NPTee 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEil ChkVlv BfyVlv GatVlv AimChk NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: PAGE: X MATERIAL: EdF1w HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEli ChkViv BfyVlv GatViv AimChk DPViv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: S C 04 0L DC CC d) 000 cC CC W(1 co C • OCQ Q u) r- Lo r— Q(0Cd WV-C (d-10C LI) e p Ci)OH CC .0 Cd--C --1 Cd C Cd P-CO dOCUd) -C .0CC Cd 4)CCO44J-H CCCd o icn -H00> -Hr-C CDCC)CC) 44 WOO WD CD CD N Ln co >H U 04 4J U) Cl) U) I I I I I II I I I I I / I I / I, / I / I C C LU C C 1-11 C Wo C C C C C C • cC C C C cC (N CL, U)CflU)U) - CO•H - - 1- C C SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: MATER SUPPLY CURVE 96+ 88+ *\ 1 0\ I \ 80+ \ I \ 72+ I \ IX P 64+ \ R I E I \\ S I S 56+ \ U I \ R I \ E I \ 48+ \\ I \ P I S I I 40+ \\ 32+ 24+ I * <-20.0 psi 8 1500 gpm Flow Test Point 16+ LEGEND I X = Required Mater Supply I 65.60 psi 8 170.3 gpm 8+ I 0 = Available Water Supply I 84.33 psi 8 170.3 gpm +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 1 - 3RD FLOOR ATTIC FILE NUMBER: 9301 DATE: FEB 19, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 240 sq. ft. COVERAGE PER SPRINKLER: 120 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 26.0 gpm TOTAL WATER REQUIRED (including hose) : 126.1 gpm FLOW AND PRESSURE (8 BOR) : 26.0 gpm 8 29.6 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC. DESIGN/LAYOUT BY: RAFAEL E. AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C-16 #786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 ) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 85.5 20.0 1500.0 84.8 126.1 39.8 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 126.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 12.1 - - - 2 30.0 - - - - 12.1 - - 3 30.0 - - - - 12.2 - - - 4 30.0 - - - - 11.9 - - - 5 30.0 - - - - 11.4 - - - 6 30.0 - - - - 11.2 - - - 7 33.0 K= 4.20 9.6 13.0 8 30.0 - - - - 11.4 - - - 9 30.0 - - - - 11.4 - - - 10 30.0 - - - - 11.4 - - - 11 30.0 - - - - 11.9 - - - 12 30.0 - - - - 11.9 - - - 13 30.0 - - - - 11.9 - - - 14 30.0 - - - - 11.9 - - - 15 30.0 - - - - 11.9 - - - 16 30.0 - - - - 11.6 - - - 17 30.0 - - - - 11.6 - - - 18 30.0 - - - - 11.2 - - - 19 33.0 K= 4.20 9.6 13.0 20 30.0 - - - - 11.9 - - - 21 30.0 - - - - 12.0 - - - 22 30.0 - - - - 12.0 - - - 23 30.0 - - - 12.0 - - - 24 30.0 - - - - 12.1 - - - 25 30.0 - - - - 12.8 - - - 26 30.0 - - - - 13.5 - - - 27 30.0 - - - - 14.2 - - - 28 30.0 - - - - 15.0 - - - 29 30.0 - - - - 15.6 - - - 30 30.0 - - - - 15.9 - - - 31 30.0 - - - - 15.6 - - - 32 30.0 - - - - 15.7 - - - 33 20.0 - - - - 20.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 20.0 - - - - 20.2 - - - 35 20.0 - - - - 20.3 - - - 36 30.0 - - - - 16.1 - - - 37 30.0 - - - - 16.1 - - - 38 30.0 - - - - 16.4 - - - 39 20.0 - - - - 20.8 - - - 40 20.0 - - - - 20.9 - - - 41 20.0 - - - - 20.3 - - - 42 20.0 - - - - 15.7 - - - 43 20.0 - - - - 15.7 - - - 44 20.0 - - - - 16.2 - - - 45 20.0 - - - - 16.2 - - - 46 20.0 - - - - 15.9 - - - 47 20.0 - - - - 15.9 - - - 48 20.0 - - - - 16.5 - - - 49 20.0 - - - - 16.6 - - - 50 20.0 - - - - 16.6 - - - 51 20.0 - - - - 16.7 - - - 52 20.0 - - - - 16.7 - - - 53 22.5 - - - - 15.6 - - - 54 20.0 - - - - 16.8 - - - 55 20.0 - - - - 16.8 - - - 56 22.5 - - - - 15.7 - - - 57 20.0 - - - - 16.8 - - - 58 20.0 - - - - 16.8 - - - 59 22.5 - - - - 15.7 - - - 60 20.0 - - - - 16.9 - - - 61 20.0 - - - - 16.9 - - - 62 22.5 - - - - 15.9 - - - 63 20.0 - - - - 17.0 - - - 64 20.0 - - - - 17.0 - - - 65 20.0 - - - - 17.4 - - - 66 9.5 - - - - 23.5 - - - 67 9.5 - - - - 23.6 - - - 68 10.0 - - - - - - 23.4 -- 69 10.0 -- - - 23.4 - - - 70 10.0 - - - - 23.4 - - - 71 9.5 - - - - 23.8 - - - 72 10.0 - - - - 23.6 - - - 73 10.0 - - - - 23.6 - - - 74 10.0 - - - - 23.6 - - - 75 10.0 - - - - 23.6 - - - 76 9.5 - - - - 24.2 - 77 9.5 - - - - 24.5 - - - 78 9.5 - - - - 24.9 - - - 79 9.5 - - - - 25.2 - - - 80 9.5 - - - - 25.7 - - - 81 9.5 - - - - 25.7 - - - 82 10.0 - - - - 25.4 - - - 83 10.0 - - - - 25.3 - - - 84 10.0 - - - - 24.7 - - - 85 9.5 - - - - 25.6 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 86 9.5 - - - - 25.6 - - - 87 9.5 - - - - 25.6 - - - TOP 9.5 - - - - 25.8 - - - MID 4.0 - - - - 28.3 - - - BTM 1.0 - - - - 29.6 - - - Ui -4.0 - - - - 31.7 - - - U2 -4.0 - - - - 31.8 - - - U3 -4.0 - - - - 31.8 - - - U4 3.0 - - - - 28.7 - - - U5 3.0 - - - - 36.7 - - - U6 -4.0 - - - - 39.8 - - - SRC -4.0 SOURCE 39.8 26.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOE TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 2.25 PF 0.0 1 30.0 0.0 12.1 0.0 0.0 150 FTG E PE 0.0 2 30.0 0.0 12.1 0.0 0.000 TL 9.25 PV Pipe: 2 -10.0 1.101 PL 2.25 PF 0.0 2 30.0 0.0 12.1 0.0 3.4 150 FTG ---- PE 0.0 3 30.0 0.0 12.2 0.0 0.019 TL 2.25 PV Pipe: 3 10.0 1.101 PL 8.00 PF 0.3 2 30.0 0.0 12.1 0.0 3.4 150 FTG 2FT PE 0.0 4 30.0 0.0 11.9 0.0 0.019 TL 15.00 PV Pipe: 4 13.0 1.101 PL 10.00 PF 0.5 4 30.0 0.0 11.9 0.0 4.4 150 FTG T PE 0.0 5 30.0 0.0 11.4 0.0 0.031 TL 15.00 PV Pipe: 5 13.0 1.101 PL 0.75 PF 0.2 5 30.0 0.0 11.4 0.0 4.4 150 FTG T PE 0.0 6 30.0 0.0 11.2 0.0 0.031 TL 5.75 PV Pipe: 6 13.0 1.101 PL 3.00 PP 0.3 6 30.0 0.0 11.2 0.0 4.4 150 FTG E PE -1.3 7 33.0 4.2 9.6 13.0 0.031 TL 10.00 PV Pipe: 7 0.0 1.101 PL 8.50 PF 0.0 5 30.0 0.0 11.4 0.0 0.0 150 FTG ---- PE 0.0 8 30.0 0.0 11.4 0.0 0.000 TL 8.50 PV Pipe: 8 0.0 1.101 PL 8.75 PP 0.0 8 30.0 0.0 11.4 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 11.4 0.0 0.000 TL 13.75 PV Pipe: 9 - 0.0 1.101 PL 7.75 PP 0.0 8 30.0 0.0 11.4 0.0 0.0 150 FTG ---- PE 0.0 10 30.0 0.0 11.4 0.0 0.000 TL 7.75 PV Pipe: 10 -3.1 1.101 PL 3.75 PF 0.0 4 30.0 0.0 11.9 0.0 1.0 150 FTG ---- PE 0.0 11 30.0 0.0 11.9 0.0 0.002 TL 3.75 PV Pipe: 11 0.0 1.101 PL 16.25 PF 0.0 11 30.0 0.0 11.9 0.0 0.0 150 FTG T FE 0.0 12 30.0 0.0 11.9 0.0 0.000 TL 21.25 PV Pipe: 12 0.0 1.101 PL 7.25 PF 0.0 12 30.0 0.0 11.9 0.0 0.0 150 FTG E PE 0.0 13 30.0 0.0 11.9 0.0 0.000 TL 14.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 0.0 1.101 PL 2.00 PF 0.0 12 30.0 0.0 11.9 0.0 0.0 150 FTG T PE 0.0 14 30.0 0.0 11.9 0.0 0.000 TL 7.00 PV Pipe: 14 -3.1 1.101 PL 0.50 PF 0.0 11 30.0 0.0 11.9 0.0 1.0 150 FTG ---- PE 0.0 15 30.0 0.0 11.9 0.0 0.002 TL 0.50 PV Pipe: 15 13.0 1.101 PL 4.00 PF 0.3 15 30.0 0.0 11.9 0.0 4.4 150 FTG T PE 0.0 16 30.0 0.0 11.6 0.0 0.031 TL 9.00 PV Pipe: 16 0.0 1.101 PL 2.25 PF 0.0 16 30.0 0.0 11.6 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 11.6 0.0 0.000 TL 7.25 PV Pipe: 17 13.0 1.101 PL 6.50 PF 0.4 16 30.0 0.0 11.6 0.0 4.4 150 FTG E PE 0.0 18 30.0 0.0 11.2 0.0 0.031 TL 13.50 PV Pipe: 18 13.0 1.101 PL 3.00 PF 0.3 18 30.0 0.0 11.2 0.0 4.4 150 FTG E PE -1.3 19 33.0 4.2 9.6 13.0 0.031 TL 10.00 PV Pipe: 19 -16.1 1.101 PL 1.50 PF 0.1 15 30.0 0.0 11.9 0.0 5.4 150 FTG ---- PE 0.0 20 30.0 0.0 11.9 0.0 0.045 TL 1.50 PV Pipe: 20 -6.7 1.101 PL 2.25 PF 0.1 20 30.0 0.0 11.9 0.0 2.3 150 FTG T PE 0.0 21 30.0 0.0 12.0 0.0 0.009 TL 7.25 PV Pipe: 21 -9.4 1.101 PL 3.00 PF 0.1 20 30.0 0.0 11.9 0.0 3.2 150 FTG ---- PE 0.0 22 30.0 0.0 12.0 0.0 0.017 TL 3.00 PV - Pipe: 22 0.0 1.101 PL 1.50 PF 0.0 22 30.0 0.0 12.0 0.0 0.0 150 FTG T PE 0.0 23 30.0 0.0 12.0 0.0 0.000 TL 6.50 PV Pipe: 23 -9.4 1.101 PL 4.00 PF 0.1 22 30.0 0.0 12.0 0.0 3.2 150 FTG 2F PE 0.0 24 30.0 0.0 12.1 0.0 0.017 TL 6.00 PV Pipe: 24 -9.4 1.101 PL 28.50 PF 0.7 24 30.0 0.0 12.1 0.0 3.2 150 FTG 2F2E PE 0.0 25 30.0 0.0 12.8 0.0 0.017 TL 44.50 PV Pipe: 25 -9.4 1.101 PL 26.00 PF 0.7 25 30.0 0.0 12.8 0.0 3.2 150 FTG 2F2E PE 0.0 26 30.0 0.0 13.5 0.0 0.017 TL 42.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 -9.4 1.101 PL 26.00 PF 0.7 26 30.0 0.0 13.5 0.0 3.2 150 FTG 2F2E PE 0.0 27 30.0 0.0 14.2 0.0 0.017 TL 42.00 PV Pipe: 27 -9.4 1.101 PL 26.00 PF 0.7 27 30.0 0.0 14.2 0.0 3.2 150 FTG 2F2E PE 0.0 28 30.0 0.0 15.0 0.0 0.017 TL 42.00 PV Pipe: 28 -9.4 1.101 PL 22.50 PF 0.6 28 30.0 0.0 15.0 0.0 3.2 150 FTG 2F2E PE 0.0 29 30.0 0.0 15.6 0.0 0.017 TL 38.50 PV Pipe: 29 -4.7 1.101 PL 36.25 PF 0.3 29 30.0 0.0 15.6 0.0 1.6 150 FTG 2E2T PE 0.0 30 30.0 0.0 15.9 0.0 0.005 TL 60.25 PV Pipe: 30 -4.6 1.101 PL 7.75 PF 0.0 29 30.0 0.0 15.6 0.0 1.6 150 FTG 2F PE 0.0 31 30.0 0.0 15.6 0.0 0.005 TL 9.75 PV Pipe: 31 -4.6 1.101 PL 3.50 PF 0.0 31 30.0 0.0 15.6 0.0 1.6 150 FTC T PE 0.0 32 30.0 0.0 15.7 0.0 0.005 TL 8.50 PV Pipe: 32 -4.6 1.101 PL 10.00 PF 0.1 32 30.0 0.0 15.7 0.0 1.6 150 FTG E PE 4.3 33 20.0 0.0 20.1 0.0 0.005 TL 17.00 PV Pipe: 33 -4.6 1.101 PL 21.25 PF 0.1 33 20.0 0.0 20.1 0.0 1.6 150 FTG 4F PE 0.0 34 20.0 0.0 20.2 0.0 0.005 TL 25.25 PV Pipe: 34 -4.6 1.101 PL 21.25 PF 0.1 34 20.0 0.0 20.2 0.0 1.6 150 FTG 4F PE 0.0 35 20.0 0.0 20.3 0.0 0.005 TL 25.25 PV Pipe: 35 -4.6 1.101 PL 10.00 PF 0.1 35 20.0 0.0 20.3 0.0 1.6 150 FTG E PE -4.3 36 30.0 0.0 16.1 0.0 0.005 TL 17.00 PV Pipe: 36 -4.6 1.101 PL 6.50 PF 0.1 36 30.0 0.0 16.1 0.0 1.6 150 FTG E PE 0.0 37 30.0 0.0 16.1 0.0 0.005 TL 13.50 PV Pipe: 37 -4.6 1.101 PL 38.75 PF 0.3 37 30.0 0.0 16.1 0.0 1.6 150 FTG E3T PE 0.0 38 30.0 0.0 16.4 0.0 0.005 TL 60.75 PV Pipe: 38 -4.6 1.101 PL 10.00 PF 0.1 38 30.0 0.0 16.4 0.0 1.6 150 FTG E PE 4.3 39 20.0 0.0 20.8 0.0 0.005 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 -4.6 1.101 PL 5.25 PF 0.1 39 20.0 0.0 20.8 0.0 1.6 150 FTG E PE 0.0 40 20.0 0.0 20.9 0.0 0.005 TL 12.25 PV Pipe: 40 -4.7 1.101 FL 10.00 PF 0.1 30 30.0 0.0 15.9 0.0 1.6 150 FTG E PE 4.3 41 20.0 0.0 20.3 0.0 0.005 TL 17.00 PV Pipe: 41 0.0 1.101 PL 10.00 PF 0.0 10 30.0 0.0 11.4 0.0 0.0 150 FTG E PE 4.3 42 20.0 0.0 15.7 0.0 0.000 TL 17.00 PV Pipe: 42 0.0 1.101 PL 5.00 PF 0.0 42 20.0 0.0 15.7 0.0 0.0 150 FTG 2E PE 0.0 43 20.0 0.0 15.7 0.0 0.000 TL 19.00 PV Pipe: 43 0.0 1.101 PL 10.00 PF 0.0 14 30.0 0.0 11.9 0.0 0.0 150 FTG E PE 4.3 44 20.0 0.0 16.2 0.0 0.000 TL 17.00 PV Pipe: 44 0.0 1.101 PL 8.00 PF 0.0 44 20.0 0.0 16.2 0.0 0.0 150 FTG 2E PE 0.0 45 20.0 0.0 16.2 0.0 0.000 TL 22.00 PV Pipe: 45 0.0 1.101 PL 10.00 PF 0.0 17 30.0 0.0 11.6 0.0 0.0 150 FTG E PE 4.3 46 20.0 0.0 15.9 0.0 0.000 TL 17.00 PV Pipe: 46 0.0 1.101 PL 3.50 PF 0.0 46 20.0 0.0 15.9 0.0 0.0 150 FTG 2E PE 0.0 47 20.0 0.0 15.9 0.0 0.000 TL 17.50 PV Pipe: 47 -6.7 1.101 PL 10.00 PF 0.2 21 30.0 0.0 12.0 0.0 2.3 150 FTG E PE 4.3 48 20.0 0.0 16.5 0.0 0.009 TL 17.00 PV Pipe: 48 -6.7 1.101 PL 1.25 PF 0.1 48 20.0 0.0 16.5 0.0 2.3 150 FTG E FE 0.0 49 20.0 0.0 16.6 0.0 0.009 TL 8.25 PV Pipe: 49 0.0 1.101 PL 4.00 PF 0.0 49 20.0 0.0 16.6 0.0 0.0 150 FTG ET PE 0.0 50 20.0 0.0 16.6 0.0 0.000 TL 16.00 PV Pipe: 50 -6.7 1.101 PL 9.25 PF 0.1 49 20.0 0.0 16.6 0.0 2.3 150 FTG ---- PE 0.0 51 20.0 0.0 16.7 0.0 0.009 TL 9.25 PV Pipe: 51 0.0 1.101 FL 2.50 PF 0.0 51 20.0 0.0 16.7 0.0 0.0 150 FTG ET PE 0.0 52 20.0 0.0 16.7 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HN(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 0.0 1.101 PL 2.50 PF 0.0 52 20.0 0.0 16.7 0.0 0.0 150 FTG E PE -1.1 53 22.5 0.0 15.6 0.0 0.000 TL 9.50 PV Pipe: 53 -6.7 1.101 PL 5.75 PF 0.1 51 20.0 0.0 16.7 0.0 2.3 150 FTG F PE 0.0 54 20.0 0.0 16.8 0.0 0.009 TL 12.75 PV Pipe: 54 0.0 1.101 PL 2.25 PF 0.0 54 20.0 0.0 16.8 0.0 0.0 150 FTG T PE 0.0 55 20.0 0.0 16.8 0.0 0.000 TL 7.25 PV Pipe: 55 0.0 1.101 PL 2.50 PF 0.0 55 20.0 0.0 16.8 0.0 0.0 150 FTG E PE -1.1 56 22.5 0.0 15.7 0.0 0.000 TL 9.50 PV Pipe: 56 -6.7 1.101 PL 5.00 PF 0.0 54 20.0 0.0 16.8 0.0 2.3 150 FTG ---- PE 0.0 57 20.0 0.0 16.8 0.0 0.009 TL 5.00 PV Pipe: 57 0.0 1.101 PL 2.25 PF 0.0 57 20.0 0.0 16.8 0.0 0.0 150 FTG T PE 0.0 58 20.0 0.0 16.8 0.0 0.000 TL 7.25 PV Pipe: 58 0.0 1.101 PL 2.50 PF 0.0 58 20.0 0.0 16.8 0.0 0.0 150 FTG E PE -1.1 59 22.5 0.0 15.7 0.0 0.000 TL 9.50 PV Pipe: 59 -6.7 1.101 PL 7.75 PF 0.1 57 20.0 0.0 16.8 0.0 2.3 150 FTG E PE 0.0 60 20.0 0.0 16.9 0.0 0.009 TL 14.75 PV Pipe: 60 0.0 1.101 PL 0.50 PF 0.0 60 20.0 0.0 16.9 0.0 0.0 150 FTG T PE 0.0 61 20.0 0.0 16.9 0.0 0.000 TL 5.50 PV Pipe: 61 0.0 1.101 PL 2.50 PF 0.0 61 20.0 0.0 16.9 0.0 0.0 150 FTG E PE -1.1 62 22.5 0.0 15.9 0.0 0.000 TL 9.50 PV Pipe: 62 -6.7 1.101 PL 8.50 PF 0.1 60 20.0 0.0 16.9 0.0 2.3 150 FTG ---- PE 0.0 63 20.0 0.0 17.0 0.0 0.009 TL 8.50 PIT Pipe: 63 10.0 1.101 PL 2.50 PF 0.0 63 20.0 0.0 17.0 0.0 3.4 150 FTG ---- PE 0.0 64 20.0 0.0 17.0 0.0 0.019 TL 2.50 PV Pipe: 64 -10.0 1.101 PL 10.00 PF 0.4 3 30.0 0.0 12.2 0.0 3.4 150 FTG 2E PE 4.3 64 20.0 0.0 17.0 0.0 0.019 TL 24.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 -16.7 1.101 PL 2.75 PF 0.4 63 20.0 0.0 17.0 0.0 5.6 150 FTG T PE 0.0 65 20.0 0.0 17.4 0.0 0.048 TL 7.75 PV Pipe: 66 -16.7 1.101 PL 10.50 PF 1.5 65 20.0 0.0 17.4 0.0 5.6 150 FTG 3E PE 4.5 66 9.5 0.0 23.5 0.0 0.048 TL 31.50 PV Pipe: 67 -16.7 1.654 PL 7.00 PF 0.2 66 9.5 0.0 23.5 0.0 2.5 120 FTG T PE 0.0 67 9.5 0.0 23.6 0.0 0.010 TL 16.12 PV Pipe: 68 0.0 1.083 PL 0.50 PF 0.0 67 9.5 0.0 23.6 0.0 0.0 120 FTG E PE -0.2 68 10.0 0.0 23.4 0.0 0.000 TL 2.84 PV Pipe: 69 0.0 1.083 PL 1.50 PF 0.0 68 10.0 0.0 23.4 0.0 0.0 120 FTG ---- PE 0.0 69 10.0 0.0 23.4 0.0 0.000 TL 1.50 PV Pipe: 70 0.0 1.083 FL 10.00 PF 0.0 69 10.0 0.0 23.4 0.0 0.0 120 FTG ---- FE 0.0 70 10.0 0.0 23.4 0.0 0.000 TL 10.00 PV Pipe: 71 -16.7 1.654 FL 13.25 PF 0.1 67 9.5 0.0 23.6 0.0 2.5 120 FTG ---- FE 0.0 71 9.5 0.0 23.8 0.0 0.010 TL 13.25 PV Pipe: 72 0.0 1.083 FL 0.50 PF 0.0 71 9.5 0.0 23.8 0.0 0.0 120 FTG T FE -0.2 72 10.0 0.0 23.6 0.0 0.000 TL 6.34 PV Pipe: 73 0.0 1.083 FL 1.50 PF 0.0 72 10.0 0.0 23.6 0.0 0.0 120 FTG T FE 0.0 73 .. 10.0 .0..0 .23.6 0.0 0.000 TL 7.34 2V. Pipe: 74 0.0 1.083 FL 3.00 PF 0.0 73 10.0 0.0 23.6 0.0 0.0 120 FTG T PE 0.0 74 10.0 0.0 23.6 0.0 0.000 TL 8.84 PV Pipe: 75 0.0 1.083 FL 13.00 PF 0.0 73 10.0 0.0 23.6 0.0 0.0 120 FTG E FE 0.0 75 10.0 0.0 23.6 0.0 0.000 TL 15.34 PV Pipe: 76 -16.7 1.654 FL 30.00 PF 0.4 71 9.5 0.0 23.8 0.0 2.5 120 FTG 2E FE 0.0 76 9.5 0.0 24.2 0.0 0.010 TL 39.12 PV Pipe: 77 -16.7 1.654 FL 26.00 PF 0.4 76 9.5 0.0 24.2 0.0 2.5 120 FTG 2E FE 0.0 77 9.5 0.0 24.5 0.0 0.010 TL 35.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 -16.7 1.654 FL 26.00 PF 0.4 77 9.5 0.0 24.5 0.0 2.5 . 120 FTG 2E PE 0.0 78 9.5 0.0 24.9 0.0 0.010 TL 35.12 PV Pipe: 79 -16.7 1.654 FL 26.00 PF 0.4 78 9.5 0.0 24.9 0.0 2.5 120 FTG 2E PE 0.0 79 9.5 0.0 25.2 0.0 0.010 TL 35.12 PV Pipe: 80 -16.7 1.654 PL 29.75 PF 0.5 79 9.5 0.0 25.2 0.0 2.5 120 FTG 4E PE 0.0 80 9.5 0.0 25.7 0.0 0.010 TL 47.99 PV Pipe: 81 9.4 1.654 FL 4.25 PF 0.0 80 9.5 0.0 25.7 0.0 1.4 120 FTG T PE 0.0 81 9.5 0.0 25.7 0.0 0.003 TL 13.37 PV Pipe: 82 4.7 1.083 PL 0.50 PF 0.0 81 9.5 0.0 25.7 0.0 1.7 120 FTG T PE -0.2 82 10.0 0.0 25.4 0.0 0.008 TL 6.34 PV Pipe: 83 4.7 1.083 PL 6.75 PF 0.1 82 10.0 0.0 25.4 0.0 1.7 120 FTG ET PE 0.0 83 10.0 0.0 25.3 0.0 0.008 TL 14.93 PV Pipe: 84 4.7 1.101 PL 57.25 PF 0.5 83 10.0 0.0 25.3 0.0 1.6 120 FTG 2E3T PE 0.0 84 10.0 0.0 24.7 0.0 0.007 TL 76.44 PV Pipe: 85 -4.7 1.101 PL 10.00 PF 0.1 41 20.0 0.0 20.3 0.0 1.6 120 FTG E PE 4.3 84 10.0 0.0 24.7 0.0 0.007 TL 14.63 PV Pipe: 86 4.6 1.654 PL 37.00 PF 0.1 81 9.5 0.0 25.7 0.0 0.7 120 FTG 4E PE 0.0 85 9.5 0.0 25.6 0.0 0.001 TL 55.24 PV Pipe: 87 4.6 1.654 PL 31.50 PF 0.0 85 9.5 0.0 25.6 0.0 0.7 120 FTG E PE 0.0 86 9.5 0.0 25.6 0.0 0.001 TL 36.06 PV Pipe: 88 4.6 1.654 FL 16.75 PF 0.0 86 9.5 0.0 25.6 0.0 0.7 .120 FTG E PE 0.0 87 9.5 0.0 25.6 0.0 0.001 TL 21 .,31 p Pipe: 89 -4.6 1.101 PL 10.50 PF 0.1 40 20.0 0.0 20.9 0.0 1.6 120 FTG 2E PE 4.5 87 9.5 0.0 25.6 0.0 0.007 TL 19.76 PV Pipe: 90 -26.0 2.705 PL 17.75 PF 0.1 80 9.5 0.0 25.7 0.0 1.5 120 FTG 2ET PE 0.0 TOP 9.5 0.0 25.8 0.0 0.002 TL 55.19 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 -26.0 2.705 PL 5.50 PF 0.1 TOP 9.5 0.0 25.8 0.0 1.5 120 FTG C PE 2.4 MID 4.0 0.0 28.3 0.0 0.002 TL 27.34 PV Pipe: 92 -26.0 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 28.3 0.0 1.5 120 FTG ---- PE 1.3 BTM 1.0 0.0 29.6 0.0 0.002 TL 3.00 PV Pipe: 93 -26.0 4.026 PL 10.00 PF 0.0 BTM 1.0 0.0 29.6 0.0 0.7 120 FTG E FE 2.2 Ui -4.0 0.0 31.7 0.0 0.000 TL 20.00 PV Pipe: 94 -26.0 4.240 PL 43.80 PF 0.0 Ui -4.0 0.0 31.7 0.0 0.6 150 FTG 3E PE 0.0 U2 -4.0 0.0 31.8 0.0 0.000 TL 103.80 PV Pipe: 95 -26.0 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 31.8 0.0 0.6 150 FTG ---- FE 0.0 U3 -4.0 0.0 31.8 0.0 0.000 TL 3.50 PV Pipe: 96 -26.0 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 31.8 0.0 0.6 140 FTG 2E FE -3.0 U4 3.0 0.0 28.7 0.0 0.000 TL 41.00 PV Pipe: 97 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 36.7 0.0 8.0 psi, 26.0 gpm U4 3.0 0.0 28.7 0.0 Pipe: 98 -26.0 4.220 FL 7.00 PF 0.0 U5 3.0 0.0 36.7 0.0 0.6 140 FTG K FE 3.0 U6 -4.0 0.0 39.8 0.0 0.000 TL 24.00 PV Pipe: 99 -26.1 4.240 FL 22.50 PF 0.0 U6 -4.0 0.0 39.8 0.0 0.6 150 FTG E PE 0.0 SRC -4.0 SRCE 39.8 (N/A) p.000 TL 42.50 PV. NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.095 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 5.6 ft/sec at pipe 66. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: 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 84.55 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A P N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B 0 N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 PAGE: E MATERIAL: PVC150 HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B 0 N Eli Tee LngEll ChkVlv BfyVlv GatVlv NPTee 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C 0 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B 0 A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AimChk NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12- 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: PAGE: X MATERIAL: EdFiw HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv BfyVlv GatViv AlmChk DPViv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 0 0 0 (N I I I I 4. I I I I 0 I I I I I II / I I / I 0 $ 41P / 0 —1 $4. / I / / / SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOE TITLE: E E U)U)U) E 00 (I) )4--1 000 U)-4 (I) 0 - ) o V) Lo 0D-04-) U)c'QU)U) Q U)- U)-0E U) OWU) if) la4 I4 U) 0l- -HU)U) -U) 0Q CUOU)- U)4J.,- (U o ,-1U)( -1D 0 >' 0r-U)&) H U) 04 co cn Ln >o (13 a4 4) (j)&) H 0 Co tN IN N 0 0 0 0 0 0 0 0 0 0 0 00 k.0 IT (N 0 —O.cflH--- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 2/19/2016 SPRINKLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR ATTIC.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ *\ O\ 80+ \ I \ I \ I \\ 72+ \ \ I \ P 64+ \ R I \ E I S \ 5 56+ U I \ R I \ E I \ 48+ \\ I \ P I \ S I \ I 40X \ I \\ 32+ \ 24+ \ * <-20.0 psi 8 1500 gpm I ============================= Flow Test Point 16+ LEGEND I X = Required Water Supply 39.78 psi 8 126.1 gpm 8+ I 0 = Available Water Supply I 84.83 psi 8 126.1 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 1 - 3RD FLOOR RESIDENTIAL FILE NUMBER: 9301 DATE: FEB 19, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (8 BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: LIGHT HAZARD 0.10 gpm/sq. ft. 4 HEADS @ 18TX18' 18'X18 ' 4 sprinklers 70.4 gpm 170.4 gpm 70.4 gpm 0 58.0 psi 7/16 inch RESIDENTIAL FIRE SYSTEMS, INC. RAFAEL E. CARLSBAD FIRE DEPARTMENT C-16 #786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 85.5 20.0 1500.0 84.3 170.4 68.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 170.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 70.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 K= 4.90 13.7 18.1 2 30.0 - - - - 14.2 - - - 3 30.0 - - - 14.5 - - - 4 30.0 - - - - 13.9 - - 5 30.0 - - - - 13.2 - - - 6 30.0 - - - - 13.2 - - - 7 33.0 - - - - 11.9 - - - 8 30.0 - - - - 12.7 - - - 9 30.0 K= 4.90 12.0 17.0 10 30.0 - - - - 12.7 - - - 11 30.0 - - - - 13.9 - - - 12 30.0 - - - - 12.9 - - - 13 30.0 K= 4.90 12.1 17.1 14 30.0 - - - - 12.9 - - - 15 30.0 - - - - 14.0 - - - 16 30.0 - - - - 14.0 - - - 17 30.0 - - - - 14.0 - - - 18 30.0 - - - - 14.0 - - - 19 33.0 - - - - 12.7 - - - 20 30.0 - - - - 14.1 - - - 21 30.0 - - - - 14.5 - - - 22 30.0 - - - - 14.2 - - - 23 30.0 K= 4.90 13.8 18.2 24 30.0 - - - - 14.8 - - - 25 30.0 - - - - 19.4 - - - 26 30.0 - - - - 23.8 - - - 27 30.0 - - - - 28.2 - - - 28 30.0 - - - - 32.6 - - - 29 30.0 - - - - 36.6 - - - 30 30.0 - - - - 38.4 - - - 31 30.0 - - - - 36.9 - - - 32 30.0 - - - - 37.1 - - - 33 20.0 - - - - 42.0 - - - S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 20.0 - - - - 42.7 - - - 35 20.0 - - - - 43.4 - - - 36 30.0 - - - - 39.5 - - - 37 30.0 - - - - 39.9 - - - 38 30.0 - - - - 41.7 - - - 39 20.0 - - - - 46.5 - - - 40 20.0 - - - - 46.8 - - - 41 20.0 - - - - 43.2 - - - 42 20.0 - - - - 17.1 - - - 43 20.0 - - - - 17.1 - - - 44 20.0 - - - - 17.2 - - - 45 20.0 - - - - 17.2 - - - 46 20.0 - - - - 18.3 - - - 47 20.0 - - - - 18.3 - - - 48 20.0 - - - - 19.6 - - 49 20.0 - - - 20.0 - - - 50 20.0 - - - - 20.0 - - - 51 20.0 - - - - 20.4 - - - 52 20.0 - - - - 20.4 - - - 53 22.5 - - - - 19.4 - - - 54 20.0 - - - - 21.0 - - - 55 20.0 - - - - 21.0 - - - 56 22.5 - - - - 20.0 - - - 57 20.0 - - - - 21.3 - - - 58 20.0 - - - 21.3 - - - 59 22.5 - - - - 20.2 - - - 60 20.0 - - - - 22.0 - - - 61 20.0 - - - - 22.0 - - - 62 22.5 - - - - 20.9 - - - 63 20.0 - - - - 22.4 - - - 64 20.0 - - - - 22.0 - - - 65 20.0 - - - - 24.8 - - - 66 9.5 - - - - 39.0 - - - 67 9.5 - - - - 40.0 - - - 68 10.0 - - - - 39.8 - - - 69 10.0 - - - - 39.8 - - -- 70 10.0 - - - - 39.8 - - - 71 9.5 - - - 40.9 - - - 72 10.0 - - - - 40.6 - - - 73 10.0 - - - - 40.6 - - - 74 10.0 - - - - 40.6 - - - 75 10.0 - - - - 40.6 - - - 76 9.5 - - - - 43.4 - - - 77 9.5 - - - - 45.6 - - - 78 9.5 - - - - 47.9 - - - 79 9.5 - - - - 50.1 - - - 80 9.5 - - - - 53.2 - - - 81 9.5 - - - - 52.9 - - - 82 10.0 - - - - 52.4 - - - 83 10.0 - - - - 51.6 - - - 84 10.0 - - - - 48.2 - - - 85 9.5 - - - - 52.6 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/19/2016KLER5\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 86 9.5 - - - - 52.3 - - - 87 9.5 - - - - 52.2 - - - TOP 9.5 - - - - 53.9 - - - MID 4.0 - - - - 56.7 - - - BTM 1.0 - - - - 58.0 - - - Ui -4.0 - - - - 60.2 - - - U2 -4.0 - - - - 60.3 - - - U3 -4.0 - - - - 60.3 - - - U4 3.0 - - - - 57.3 - - - U5 3.0 - - - - 65.3 - - - U6 -4.0 - - - - 68.4 - - - SRC -4.0 SOURCE 68.4 70.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOE TITLE: PIPE DATA 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: 1 -18.1 1.101 FL 2.25 PF 0.5 1 30.0 4.9 13.7 18.1 6.1 150 FTG E PE 0.0 2 30.0 0.0 14.2 0.0 0.057 TL 9.25 PV Pipe: 2 -28.7 1.101 FL 2.25 PF 0.3 2 30.0 0.0 14.2 0.0 9.7 150 FTG ---- PE 0.0 3 30.0 0.0 14.5 0.0 0.133 TL 2.25 PV Pipe: 3 10.6 1.101 PL 8.00 PF 0.3 2 30.0 0.0 14.2 0.0 3.6 150 FTG 2FT PE 0.0 4 30.0 0.0 13.9 0.0 0.021 TL 15.00 PV Pipe: 4 17.0 1.101 PL 10.00 PF 0.8 4 30.0 0.0 13.9 0.0 5.7 150 FTG T PE 0.0 5 30.0 0.0 13.2 0.0 0.050 TL 15.00 FV Pipe: 5 0.0 1.101 PL 0.75 PF 0.0 5 30.0 0.0 13.2 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 13.2 0.0 0.000 TL 5.75 PV Pipe: 6 0.0 1.101 PL 3.00 PF 0.0 6 30.0 0.0 13.2 0.0 0.0 150 FTG E PE -1.3 7 33.0 0.0 11.9 0.0 0.000 TL 10.00 PV Pipe: 7 17.0 1.101 PL 8.50 PF 0.4 5 30.0 0.0 13.2 0.0 5.7 150 FTG ---- FE 0.0 8 30.0 0.0 12.7 0.0 0.050 TL 8.50 PV Pipe: 8 17.0 1.101 FL 8.75 PF 0.7 8 30.0 0.0 12.7 0.0 5.7 150 FTG T FE 0.0 9 30.0 4.9 12.0 17.0 0.050 TL 13.75 PV Pipe: 9 0.0 1.101 PL 7.75 PF 0.0 8 30.0 0.0 12.7 0.0 0.0 150 FTG ---- FE 0.0 10 30.0 0.0 12.7 0.0 0.000 TL 7.75 PV Pipe: 10 -6.4 1.101 FL 3.75 PF 0.0 4 30.0 0.0 13.9 0.0 2.2 150 FTG ---- FE 0.0 11 30.0 0.0 13.9 0.0 0.008 TL 3.75 PV Pipe: 11 17.1 1.101 PL 16.25 PF 1-.l-- 11 30.0 0.0 13.9 0.0 5.8 150 FTG T FE 0.0 12 30.0 0.0 12.9 0.0 0.051 TL 21.25 PV Pipe: 12 17.1 1.101 FL 7.25 PF 0.7 12 30.0 0.0 12.9 0.0 5.8 150 FTG E FE 0.0 13 30.0 4.9 12.1 17.1 0.051 TL 14.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 0.0 1.101 PL 2.00 PF 0.0 12 30.0 0.0 12.9 0.0 0.0 150 FTG T PE 0.0 14 30.0 0.0 12.9 0.0 0.000 TL 7.00 PV Pipe: 14 -23.5 1.101 PL 0.50 PF 0.0 11 30.0 0.0 13.9 0.0 7.9 150 FTG ---- PE 0.0 15 30.0 0.0 14.0 0.0 0.092 TL 0.50 PV Pipe: 15 0.0 1.101 PL 4.00 PF 0.0 15 30.0 0.0 14.0 0.0 0.0 150 FTG T PE 0.0 a 16 30.0 0.0 14.0 0.0 0.000 TL 9.00 PV Pipe: 16 0.0 1.101 PL 2.25 PF 0.0 16 30.0 0.0 14.0 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 14.0 0.0 0.000 TL 7.25 PV Pipe: 17 0.0 1.101 PL 6.50 PF 0.0 16 30.0 0.0 14.0 0.0 0.0 150 FTG E PE 0.0 18 30.0 0.0 14.0 0.0 0.000 TL 13.50 PV Pipe: 18 0.0 1.101 PL 3.00 PF 0.0 18 30.0 0.0 14.0 0.0 0.0 150 FTG E PE -1.3 19 33.0 0.0 12.7 0.0 0.000 TL 10.00 PV Pipe: 19 -23.5 1.101 PL 1.50 PF 0.1 15 30.0 0.0 14.0 0.0 7.9 150 FTG ---- PE 0.0 20 30.0 0.0 14.1 0.0 0.092 TL 1.50 PV Pipe: 20 -16.5 1.101 PL 2.25 PF 0.3 20 30.0 0.0 14.1 0.0 5.5 150 FTG T PE 0.0 21 30.0 0.0 14.5 0.0 0.047 TL 7.25 PV Pipe: 21 -7.0 1.101 PL 3.00 PF 0.0 20 30.0 0.0 14.1 0.0 2.4 150 FTG ---- PE 0.0 22 30.0 0.0. 14.2 0.0 0.010 TL 3.00 PV Pipe: 22 18.2 1.101 PL 1.50 PF 0.4 22 30.0 0.0 14.2 0.0 6.1 150 FTG T PE 0.0 23 30.0 4.9 13.8 18.2 0.057 TL 6.50 PV Pipe: 23 -25.2 1.101 PL 4.00 PF 0.6 22 30.0 0.0 14.2 0.0 8.5 150 FTG 2F PE 0.0 24 30.0 0.0 14.8 0.0 0.105 TL 6.00 PV Pipe: 24 -25.2 1.101 PL 28.50 PF 4.7 24 30.0 0.0 14.8 0.0 8.5 150 FTG 2F2E PE 0.0 25 30.0 0.0 19.4 0.0 0.105 TL 44.50 PV Pipe: 25 -25.2 1.101 PL 26.00 PF 4.4 25 30.0 0.0 19.4 0.0 8.5 150 FTG 2F2E PE 0.0 26 30.0 0.0 23.8 0.0 0.105 TL 42.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES '(FT) (K) (PSI) (GPM) FL/FT (PSI)' Pipe: 26 -25.2 1.101 PL 26.00 PF 4.4 26 30.0 0.0 23.8 0.0 8.5 150 FTG 2F2E PE 0.0 27 30.0 0.0 28.2 0.0 0.105 TL 42.00 PV Pipe: 27 -25.2 1.101 PL 26.00 PF 4.4 27 30.0 0.0 28.2 0.0 8.5 150 FTG 2F2E PE 0.0 28 30.0 0.0 32.6 0.0 0.105 TL 42.00 PV Pipe: 28 -25.2 1.101 PL 22.50 PF 4.0 28 30.0 0.0 32.6 0.0 8.5 150 FTG 2F2E FE 0.0 29 30.0 0.0 36.6 0.0 0.105 TL 38.50 PV Pipe: 29 -12.7 1.101 PL 36.25 PF 1.8 29 30.0 0.0 36.6 0.0 4.3 150 FTG 2E2T PE 0.0 30 30.0 0.0 38.4 0.0 0.030 TL 60.25 pv Pipe: 30 -12.5 1.101 PL 7.75 PF 0.3 29 30.0 0.0 36.6 0.0 4.2 150 FTG 2F PE 0.0 31 30.0 0.0 36.9 0.0 0.028 TL 9.75 PV Pipe: 31 -12.5 1.101 FL 3.50 PF 0.2 31 30.0 0.0 36.9 0.0 4.2 150 FTG T PE 0.0 32 30.0 0.0 37.1 0.0 0.028 TL 8.50 PV Pipe: 32 -12.5 1.101 PL 10.00 PF 0.5 32 30.0 0.0 37.1 0.0 4.2 150 FTG E FE 4.3 33 20.0 0.0 42.0 0.0 0.028 TL 17.00 PV Pipe: 33 -12.5 1.101 FL 21.25 PF 0.7 33 20.0 0.0 42.0 0.0 4.2 150 FTG 4F FE 0.0 34 20.0 0.0 42.7 0.0 0.028 TL 25.25 PV Pipe: 34 -12.5 1.101 PL 21.25 PF 0.7 34 20.0 0.0 42.7 0.0 4.2 150 FTG 4F PE 0.0 35 20.0 0.0 43.4 0.0 0.028 TL 25.25 PV Pipe: 35 -12.5 1.101 PL 10.00 PF 0.5 35 20.0 0.0 43.4 0.0 4.2 150 FTG E FE -4.3 36 30.0 0.0 39.5 0.0 0.028 TL 17.00 PV Pipe: 36 -12.5 1.101 FL 6.50 PF 0.4 36 30.0 0.0 39.5 0.0 4.2 150 FTG E FE 0.0 37 30.0 0.0 39.9 0.0 0.028 TL 13.50 PV . . . Pipe: 37 -12.5 1.101 FL 38.75 PF 1.7 37 30.0 0.0 39.9 0.0 4.2 150 FTG E3T PE 0.0 38 30.0 0.0 41.7 0.0 0.028 TL 60.75 PV Pipe: 38 -12.5 1.101 PL 10.00 PF 0.5 38 30.0 0.0 41.7 0.0 4.2 150 FTG E FE 4.3 39 20.0 0.0 46.5 0.0 0.028 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/19/2016KLERS\CALCS\DELTA 2\EUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOE TITLE: 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 -12.5 1.101 PL 5.25 PF 0.3 39 20.0 0.0 46.5 0.0 4.2 150 FTG E PE 0.0 40 20.0 0.0 46.8 0.0 0.028 TL 12.25 PV Pipe: 40 -12.7 1.101 PL 10.00 PF 0.5 30 30.0 0.0 38.4 0.0 4.3 150 FTG E PE 4.3 41 20.0 0.0 43.2 0.0 0.030 TL 17.00 PV Pipe: 41 0.0 1.101 PL 10.00 PF 0.0 10 30.0 0.0 12.7 0.0 0.0 150 FTG E PE 4.3 S 42 20.0 0.0 17.1 0.0 0.000 TL 17.00 PV Pipe: 42 0.0 1.101 PL 5.00 PF 0.0 42 20.0 0.0 17.1 0.0 0.0 150 FTG 2E PE 0.0 43 20.0 0.0 17.1 0.0 0.000 TL 19.00 PV Pipe: 43 0.0 1.101 PL 10.00 PF 0.0 14 30.0 0.0 12.9 0.0 0.0 150 FTG E PE 4.3 44 20.0 0.0 17.2 0.0 0.000 TL 17.00 PV Pipe: 44 0.0 1.101 PL 8.00 PF 0.0 44 20.0 0.0 17.2 0.0 0.0 150 FTG 2E PE 0.0 45 20.0 0.0 17.2 0.0 0.000 TL 22.00 PV Pipe: 45 0.0 1.101 PL 10.00 PF 0.0 17 30.0 0.0 14.0 0.0 0.0 150 FTG E PE 4.3 46 20.0 0.0 18.3 0.0 0.000 TL 17.00 PV Pipe: 46 0.0 1.101 PL 3.50 PF 0.0 46 20.0 0.0 18.3 0.0 0.0 150 FTG 2E PE 0.0 47 20.0 0.0 18.3 0.0 0.000 TL 17.50 PV Pipe: 47 -16.5 1.101 PL 10.00 PF 0.8 21 30.0 0.0 14.5 0.0 5.5 150 FTG E PE 4.3 48 20.0 0.0 19.6 0.0 0.047 TL 17.00 PV Pipe: 48 -16.5 1.101 PL 1.25 PF 0.4 48 20.0 0.0 19.6 0.0 5.5 150 FTG E PE 0.0 49 20.0 0.0 20.0 0.0 0.047 TL 8.25 PV Pipe: 49 0.0 1.101 PL 4.00 PF 0.0 49 20.0 0.0 20.0 0.0 0.0 150 FTG ET PE 0.0 50 20.0 0.0 20.0 0.0 0.000 TL 16.00 PV Pipe: 50 -16.5 1.101 PL 9.25 PF 0.4 49 20.0 0.0 20.0 0.0 5.5 150 FTG ---- PE 0.0 51 20.0 0.0 20.4 0.0 0.047 TL 9.25 PV Pipe: 51 0.0 1.101 FL 2.50 PF 0.0 51 20.0 0.0 20.4 0.0 0.0 150 FTG ST PE 0.0 52 20.0 0.0 20.4 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) .HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 0.0 1.101 PL 2.50 PF 0.0 52 20.0 0.0 20.4 0.0 0.0 150 FTG E PE -1.1 53 22.5 0.0 19.4 0.0 0.000 TL 9.50 PV Pipe: 53 -16.5 1.101 PL 5.75 PF 0.6 51 20.0 0.0 20.4 0.0 5.5 150 FTG E PE 0.0 54 20.0 0.0 21.0 0.0 0.047 TL 12.75 PV Pipe: 54 0.0 1.101 PL 2.25 PF 0.0 54 20.0 0.0 21.0 0.0 0.0 150 FTG T PE 0.0 55 20.0 0.0 21.0 0.0 0.000 TL 7.25 PV Pipe: 55 0.0 1.101 PL 2.50 PF 0.0 55 20.0 0.0 21.0 0.0 0.0 150 FTG E PE -1.1 56 22.5 0.0 20.0 0.0 0.000 TL 9.50 PV Pipe: 56 -16.5 1.101 PL 5.00 PF 0.2 54 20.0 0.0 21.0 0.0 5.5 150 FTG ---- PE 0.0 57 20.0 0.0 21.3 0.0 0.047 TL 5.00 PV Pipe: 57 0.0 1.101 Pb 2.25 PF 0.0 57 20.0 0.0 21.3 0.0 0.0 150 FTG T PE 0.0 58 20.0 0.0 21.3 0.0 0.000 TL 7.25 PV Pipe: 58 0.0 1.101 Pb 2.50 PF 0.0 58 20.0 0.0 21.3 0.0 0.0 150 FTG E PE -1.1 59 22.5 0.0 20.2 0.0 0.000 TL 9.50 PV Pipe: 59 -16.5 1.101 Pb 7.75 PF 0.7 57 20.0 0.0 21.3 0.0 5.5 150 FTG E PE 0.0 60 20.0 0.0 22.0 0.0 0.047 TL 14.75 PV Pipe: 60 0.0 1.101 Pb 0.50 PF 0.0 60 20.0 0.0 22.0 0.0 0.0 150 FTG T PE 0.0 61 20.0 0.0 22.0 0.0 0.000 TL 5.50 PV Pipe: 61 0.0 1.101 PL 2.50 PF 0.0 61 20.0 0.0 22.0 0.0 0.0 150 FTG E PE -1.1 62 22.5 0.0 20.9 0.0 0.000 TL 9.50 PV Pipe: 62 -16.5 1.101 PL 8.50 PF 0.4 60 20.0 0.0 22.0 0.0 5.5 150 FTG ---- PE 0.0 63 20.0 0.0 22.4 0.0 0.047 TL 8.50 PV Pipe: 63 28.7 1.101 Pb 2.50 PF 0.3 63 20.0 0.0 22.4 0.0 9.7 150 FTG ---- PE 0.0 64 20.0 0.0 22.0 0.0 0.133 TL 2.50 PV Pipe: 64 -28.7 1.101 Pb 10.00 PF 3.2 3 30.0 0.0 14.5 0.0 9.7 150 FTG 2E PE 4.3 64 20.0 0.0 22.0 0.0 0.133 TL 24.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOE TITLE: 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 -45.2 1.101 PL 2.75 PF 2.4 63 20.0 0.0 22.4 0.0 15.2 150 FTG T PE 0.0 65 20.0 0.0 24.8 0.0 0.307 TL 7.75 PV Pipe: 66 -45.2 1.101 PL 10.50 PF 9.7 65 20.0 0.0 24.8 0.0 15.2 150 FTG 3E PE 4.5 66 9.5 0.0 39.0 0.0 0.307 TL 31.50 PV Pipe: 67 -45.2 1.654 PL 7.00 PF 1.0 66 9.5 0.0 39.0 0.0 6.7 120 FTG T PE 0.0 67 9.5 0.0 40.0 0.0 0.064 TL 16.12 PV Pipe: 68 0.0 1.083 PL 0.50 PF 0.0 67 9.5 0.0 40.0 0.0 0.0 120 FTG E PE -0.2 68 10.0 0.0 39.8 0.0 0.000 TL 2.84 PV Pipe: 69 0.0 1.083 PL 1.50 PF 0.0 68 10.0 0.0 39.8 0.0 0.0 120 FTG ---- PE 0.0 69 10.0 0.0 39.8 0.0 0.000 TL 1.50 PV Pipe: 70 0.0 1.083 PL 10.00 PF 0.0 69 10.0 0.0 39.8 0.0 0.0 120 FTG ---- PE 0.0 70 10.0 0.0 39.8 0.0 0.000 TL 10.00 PV Pipe: 71 -45.2 1.654 PL 13.25 PF 0.8 67 9.5 0.0 40.0 0.0 6.7 120 FTG ---- PE 0.0 71 9.5 0.0 40.9 0.0 0.064 TL 13.25 PV Pipe: 72 0.0 1.083 PL 0.50 PF 0.0 71 9.5 0.0 40.9 0.0 0.0 120 FTG T PE -0.2 72 10.0 0.0 40.6 0.0 0.000 TL 6.34 PV Pipe: 73 0.0 1.083 PL 1.50 PF 0.0 72 10.0 0.0 40.6 0.0 0.0 120 FTG T PE 0.0 73 . .. 10.0 0.0. 40.6 0.0 .. 0.000 TL 7.34 P.V. ... Pipe: 74 0.0 1.083 PL 3.00 PF 0.0 73 10.0 0.0 40.6 0.0 .0.0 120 FTG T PE 0.0 74 10.0 0.0 40.6 0.0 0.000 TL 8.84 PV Pipe: 75 0.0 1.083 PL 13.00 PF 0.0 73 10.0 0.0 40.6 0.0 0.0 120 FTG E PE 0.0 75 10.0 0.0 40.6 0.0 0.000 TL 15.34 PV Pipe: 76 -45.2 1.654 PL 30.00 PF 2.5 71 9.5 0.0 40.9 0.0 6.7 120 FTG 2E PE 0.0 76 9.5 0.0 43.4 0.0 0.064 TL 39.12 PV Pipe: 77 -45.2 1.654 FL 26.00 PF 2.2 76 9.5 0.0 43.4 0.0 6.7 120 FTG 2E FE 0.0 77 9.5 0.0 45.6 0.0 0.064 TL 35.12 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HN(C) (FT) SUM. NODES'('FT) (K) (PSI) (GPM) FL/FT - (PSI) Pipe: 78 -45.2 1.654 PL 26.00 PF 2.2 77 9.5 0.0 45.6 0.0 6.7 120 FTC 2E PE 0.0 78 9.5 0.0 47.9 0.0 0.064 TL 35.12 PV Pipe: 79 -45.2 1.654 PL 26.00 PF 2.2 78 9.5 0.0 47.9 0.0 6.7 120 FTG 2E PE 0.0 79 9.5 0.0 50.1 0.0 0.064 TL 35.12 PV Pipe: 80 -45.2 1.654 PL 29.75 PF 3.1 79 9.5 0.0 50.1 0.0 6.7 120 FTG 4E PE 0.0 ' 80 9.5 0.0 53.2 0.0 0.064 TL 47.99 PV Pipe: 81 25.2 1.654 PL 4.25 PF 0.3 80 9.5 0.0 53.2 0.0 3.8 120 FTG T PE 0.0 81 9.5 0.0 52.9 0.0 0.022 TL 13.37 PV Pipe: 82 12.7 1.083 PL 0.50 PF 0.3 81 9.5 0.0 52.9 0.0 4.4 120 FTG T PE -0.2 82 10.0 0.0 52.4 0.0 0.048 TL 6.34 PV Pipe: 83 12.7 1.083 PL 6.75 PF 0.7 82 10.0 0.0 52.4 0.0 4.4 120 FTG ET PE 0.0 83 10.0 0.0 51.6 0.0 0.048 TL 14.93 PV Pipe: 84 12.7 1.101 PL 57.25 PF 3.4 83 10.0 0.0 51.6 0.0 4.3 120 FTG 2E3T PE 0.0 84 10.0 0.0 48.2 0.0 0.045 TL 76.44 PV Pipe: 85 -12.7 1.101 PL 10.00 PF 0.7 41 20.0 0.0 43.2 0.0 4.3 120 FTG E PE 4.3 84 10.0 0.0 48.2 0.0 0.045 TL 14.63 PV Pipe: 86 12.5 1.654 PL 37.00 PF 0.3 81 9.5 0.0 52.9 0.0 1.9 120 FTG 4E PE 0.0 85 9.5 0.0 52.6 0.0 0.006 TL 55.24 PV Pipe: 87 12.5 1.654 PL 31.50 PF 0.2 85 9.5 0.0 52.6 0.0 1.9 120 FTG E PE 0.0 86 9.5 0.0 52.3 0.0 0.006 TL 36.06 PV Pipe: 88 12.5 1.654 PL 16.75 PF 0.1 86 9.5 0.0 52.3 0.0 1.9 120 FTG E PE 0.0 87 9.5 0.0 52.2 0.0 0.006 TL 21.31 PV Pipe: 89 -12.5 1.101 PL 10.50 PF 0.8 40 20.0 0.0 46.8 0.0 4.2 120 FTG 2E PS 4.5 87 9.5 0.0 52.2 0.0 0.043 TL 19.76 PV Pipe: 90 -70.4 2.705 PL 17.75 PF 0.7 80 9.5 0.0 53.2 0.0 3.9 120 FTC 2ET PE 0.0 TOP 9.5 0.0 53.9 0.0 0.013 TL 55.19 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 2/19/2016KLER5\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VELPS) HN(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 91 -70.4 2.705 PL 5.50 PF 0.4 TOP 9.5 0.0 53.9 0.0 3.9 120 •FTG C PE 2.4 MID 4.0 0.0 56.7 0.0 0.013 TL 27.34 PV Pipe: 92 -70.4 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 56.7 0.0 3.9 120 FTG ---- PE 1.3 BTM 1.0 0.0 58.0 0.0 0.013 TL 3.00 PV Pipe: 93 -70.4 4.026 PL 10.00 PF 0.0 BTM 1.0 0.0 58.0 0.0 1.8 120 FTG E PE 2.2 Ui -4.0 0.0 60.2 0.0 0.002 TL 20.00 PV Pipe: 94 -70.4 4.240 PL 43.80 PF 0.1 Ui -4.0 0.0 60.2 0.0 1.6 150 FTG 3E PE 0.0 U2 -4.0 0.0 60.3 0.0 0.001 TL 103.80 PV Pipe: 95 -70.4 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 60.3 0.0 1.6 150 FTG ---- PE 0.0 U3 -4.0 0.0 60.3 0.0 0.001 TL 3.50 PV Pipe: 96 -70.4 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 60.3 0.0 1.6 140 FTG 2E PE -3.0 U4 3.0 0.0 57.3 0.0 0.001 TL 41.00 PV Pipe: 97 FIXED PRESSURE LOSS DEVICE US 3.0 0.0 65.3 0.0 8.0 psi, 70.4 gpm U4 3.0 0.0 57.3 0.0 Pipe: 98 -70.4 4.220 PL 7.00 PF 0.0 US 3.0 0.0 65.3 0.0 1.6 140 FTG E PE 3.0 U6 -4.0 0.0 68.4 0.0 0.001 TL 24.00 PV Pipe: 99 -70.4 4.240 PL 2.2.50 PF 0.0 U6 -4.0 0.0 68.4 0.0 1.6 150 FTG E PE 0.0 SRC -4.0 SBCE 68.4 (N/A) 0.0.01 TL 42.50 PV NOTES (HASS) : Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.152 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 15.2 ft/sec at pipe 66. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 13 DATE: 2/19/2016KLER5\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 84.17 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd 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 NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12- 0.00 -- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 14 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PAGE: X MATERIAL: EdF1w HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEl1 ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 e U E ci) 000 (D cc) 0 CO 0O-4-) )-1 co,- QE U) ccac(D 0w ccU)Jcf)-1 0 -1(DEU) -U) U)UU) - (0 l( -1() ,-4C')0>, --1Cc) DC1)W )111 ,> Q) co SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 15 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 0 0 0 LU 0 44 H 04 0 0 (N -H C)) 0 co 0 Ln co a4 4J C,) z H I I .4 .4 0 0 .4 cUD I I I / .. 4* / I I / $ CD I H 40, / I / / / cc N 0 C-) cUD C) CD cc CD 0 0 CD CD 0 CC) 31 (N 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 16 DATE: 2/19/2016KLERS\CALCS\DELTA 2\BUILDING 1 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ I 0\ I \ 80+ \ I \ I \\ 72+ I \ - ix \ I \ P 64+ \ R I \ E \\ S \ S56+ \ U \ R \ E I \ 48+ \\ ( I P t \ S I \ I 40+ \ \ \\ 32+ \ I \ I \ 24+ I \ I * <-20.0 psi 8 1500 gpm I ============-====--=========== Flow Test Point * 16+ LEGEND I X = Required Water Supply I 68.42 psi 8 170.4 gpm 8+ I 0 = Available Water Supply I 84.33 psi @ 170.4 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ( ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 2 - 1ST FLOOR GARAGE FILE NUMBER: 9301 DATE: FEB 1, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: ORDINARY (GROUP 1) HAZARD DENSITY: 0.15 gpm/sq. ft. AREA OF APPLICATION: 520 sq. ft. COVERAGE PER SPRINKLER: 130 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 79.2 gpm TOTAL WATER REQUIRED (including hose) : 179.2 gpm FLOW AND PRESSURE (8 BOR) : 79.2 gpm @ 29.0 Psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS, INC. DESIGN/LAYOUT BY: RAFAEL E. AUTHORITY HAVING JURISDICTION: CARLSBAD FIRE DEPARTMENT CONTRACTOR CERTIFICATION NUMBER: C-16 #786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38561304 ) HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\EUILDING 2 - 1ST FLOOR GARAGE.SDF JOE TITLE: MATER 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 85.5 20.0 1500.0 84.2 179.2 39.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 179.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 79.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 - - - - 10.4 - - 2 30.0 - - - - 10.4 - - - 3 30.0 - - - 10.4 - - - 4 30.0 - - - - 10.1 - - - 5 30.0 - - - - 10.6 - - - 6 30.0 - - - - 10.6 - - - 7 30.0 - - - - 10.6 - - - 8 30.0 - - - - 10.6 - - - 9 30.0 - - - - 10.6 - - - 10 30.0 - - - - 10.6 - - - 11 30.0 - - - - 10.7 - - - 12 30.0 - - - - 10.7 - - - 13 30.0 - - - - 10.7 - - - 14 30.0 - - - - 10.7 - - - 15 30.0 - - - - 10.7 - - - 16 30.0 - - - - 10.7 - - - 17 30.0 - - - - 11.3 .-.- - 18 30.0 - - - - 12.8 - - - 19 30.0 - - - - 13.6 - - - 20 30.0 - - - - 13.8 - - - 21 20.0 - - - - 18.4 - - 22 20.0 - - - - 15.1 - - - 23 20.0 - - - - 15.1 - - - 24 20.0 - - - - 15.0 - - - 25 20.0 - - - - 15.0 - - - 26 20.0 - - - - 15.0 - - 27 20.0 - - - - 15.0 - - - 28 20.0 - - - - 14.7 - - - 29 20.0 - - - - 14.7 - - - 30 20.0 - - - - 14.1 - - - 31 20.0 - - - - 13.8 - - - 32 9.5 - - - - 18.0 - - - 33 9.5 - - - - 17.9 - - - 14 i w SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\EUILDING 2 - 1ST FLOOR GARAGE.SDF JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 10.0 - - - - 15.2 - - - 35 10.0 - - - - 13.5 - - - 36 10.0 K= 5.60 12.6 19.9 37 10.0 K= 5.60 12.1 19.5 38 9.5 - - - - 18.3 - - - 39 10.0 - - - - 15.6 - - - 40 10.0 - - - - 13.8 - - - 41 10.0 K= 5.60 13.0 20.2 42 10.0 K= 5.60 12.3 19.7 43 9.5 - - - - 24.0 - - - 44 9.5 - - - - 23.6 - - - TOP 9.5 - - - - 24.9 - - - MID 4.0 - - - - 27.7 - - - ETM 1.0 - - - - 29.0 - - - Ui -4.0 - - - - 31.3 - - - U2 -4.0 - - - - 31.6 - - - U3 -4.0 - - - - 31.6 - - - U4 3.0 - - - - 28.6 - - - U5 3.0 - - - - 36.6 - - - U6 -4.0 - - - - 39.7 - - - SRC -4.0 SOURCE 39.7 79.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOE TITLE: 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 1.101 PL 8.00 PF 0.0 1 30.0 0.0 10.4 0.0 0.0 150 FTG T PE 0.0 2 30.0 0.0 10.4 0.0 0.000 TL 13.00 PV Pipe: 2 0.0 1.101 PL 1.25 PF 0.0 2 30.0 0.0 10.4 0.0 0.0 150 FTG ---- PE 0.0 3 30.0 0.0 10.4 0.0 0.000 TL 1.25 PV Pipe: 3 10.2 1.101 PL 5.00 PF 0.3 3 30.0 0.0 10.4 0.0 3.4 150 FTG ET PE 0.0 4 30.0 0.0 10.1 0.0 0.020 TL 17.00 PV Pipe: 4 -10.2 1.101 PL 4.75 PF 0.2 3 30.0 0.0 10.4 0.0 3.4 150 FTG T PE 0.0 5 30.0 0.0 10.6 0.0 0.020 TL 9.75 PV Pipe: 5 0.0 1.101 PL 0.50 PP 0.0 5 30.0 0.0 10.6 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 10.6 0.0 0.000 TL 5.50 PV Pipe: 6 -10.2 1.101 PL 2.25 PF 0.0 5 30.0 0.0 10.6 0.0 3.4 150 FTG ---- PE 0.0 7 30.0 0.0 10.6 0.0 0.020 TL 2.25 PV Pipe: 7 0.0 1.101 PL 8.25 PF 0.0 7 30.0 0.0 10.6 0.0 0.0 150 FTG T PE 0.0 8 30.0 0.0 10.6 0.0 0.000 TL 13.25 PV Pipe: 8 0.0 1.101 PL 2.50 PF 0.0 8 30.0 0.0 10.6 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 10.6 0.0 0.000 TL 7.50 PV Pipe: 9 . 0.0 1.101 PL 7.00 PF 0.0 8 30.0 0.0 10.6 0.0 0.0 150 FTG ---- PE 0.0 10 30.0 0.0 10.6 0.0 0.000 TL 7.00 PV Pipe: 10 -10.2 1.101 PL 4.00 PF 0.1 7 30.0 0.0 10.6 0.0 3.4 150 FTG ---- PE 0.0 11 30.0 0.0 10.7 0.0 0.020 TL 4.00 PV Pipe: 11 0.0 1.101 PL 1.25 PF 0.0 11 30.0 0.0 10.7 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 10.7 0.0 0.000 TL 6.25 PV Pipe: 12 -10.2 1.101 PL 1.75 PF 0.0 11 30.0 0.0 10.7 0.0 3.4 150 FTG ---- PE 0.0 13 30.0 0.0 10.7 0.0 0.020 TL 1.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 0.0 1.101 PL 9.00 PF 0.0 13 30.0 0.0 10.7 0.0 0.0 150 FTG T PE 0.0 14 30.0 0.0 10.7 0.0 0.000 TL 14.00 PV Pipe: 14 0.0 1.101 FL 1.75 PF 0.0 14 30.0 0.0 10.7 0.0 0.0 150 FTG ---- PE 0.0 15 30.0 0.0 10.7 0.0 0.000 TL 1.75 PV Pipe: 15 0.0 1.101 FL 2.00 PF 0.0 14 30.0 0.0 10.7 0.0 0.0 150 FTG T FE 0.0 16 30.0 0.0 10.7 0.0 0.000 TL 7.00 PV Pipe: 16 -10.2 1.101 PL 26.50 PF 0.6 13 30.0 0.0 10.7 0.0 3.4 150 FTG 4F PE 0.0 17 30.0 0.0 11.3 0.0 0.020 TL 30.50 PV Pipe: 17 -10.2 1.101 PL 48.00 PF 1.4 17 30.0 0.0 11.3 0.0 3.4 150 FTG 4F3E FE 0.0 18 30.0 0.0 12.8 0.0 0.020 TL 73.00 PV Pipe: 18 -10.2 1.101 FL 21.75 PF 0.9 18 30.0 0.0 12.8 0.0 3.4 150 FTG 4F2ET FE 0.0 19 30.0 0.0 13.6 0.0 0.020 TL 44.75 PV Pipe: 19 -10.2 1.101 FL 1.50 PF 0.1 19 30.0 0.0 13.6 0.0 3.4 150 FTG T FE 0.0 20 30.0 0.0 13.8 0.0 0.020 TL 6.50 PV Pipe: 20 -10.2 1.101 FL 10.00 PF 0.3 20 30.0 0.0 13.8 0.0 3.4 150 FTG E FE 4.3 21 20.0 0.0 18.4 0.0 0.020 TL 17.00 PV Pipe: 21 0.0 1.101 FL 10.00 PF 0.0 15 30.0 0.0 10.7 0.0 0.0 150 FTG E FE 4.3 22 20:0 0.0 15.1 0.0 0.000 TL 17.00 PV Pipe: 22 0.0 1.101 FL 3.75 PF 0.0 22 20.0 0.0 15.1 0.0 0.0 150 FTG 2E FE 0.0 q 23 20.0 0.0 15.1 0.0 0.000 TL 17.75 PV Pipe: 23 0.0 1.101 FL 10.00 PF 0.0 12 30.0 0.0 10.7 0.0 0.0 150 FTG E FE 4.3 24 20.0 0.0 15.0 0.000 TL 17.00 PV Pipe: 24 0.0 1.101 PL 4.00 PF 0.0 24 20.0 0.0 15.0 0.0 0.0 150 FTG 2E FE 0.0 25 20.0 0.0 15.0 0.0 0.000 TL 18.00 PV Pipe: 25 0.0 1.101 FL 10.00 FE 0.0 10 30.0 0.0 10.6 0.0 0.0 150 FTG E FE 4.3 26 20.0 0.0 15.0 0.0 0.000 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.101 PL 9.00 PF 0.0 26 20.0 0.0 15.0 0.0 0.0 150 FTG ET PE 0.0 27 20.0 0.0 15.0 0.0 0.000 TL 21.00 PV Pipe: 27 0.0 1.101 PL 10.00 PF 0.0 2 30.0 0.0 10.4 0.0 0.0 150 FTG T PE 4.3 28 20.0 0.0 14.7 0.0 0.000 TL 15.00 PV Pipe: 28 0.0 1.101 PL 3.50 PF 0.0 4 28 20.0 0.0 14.7 0.0 0.0 150 FTG 2E FE 0.0 29 20.0 0.0 14.7 0.0 0.000 TL 17.50 PV Pipe: 29 10.2 1.101 FL 10.00 PF 0.3 4 30.0 0.0 10.1 0.0 3.4 150 FTG E PE 4.3 30 20.0 0.0 14.1 0.0 0.020 TL 17.00 PV Pipe: 30 10.2 1.101 FL 4.25 PE 0.3 30 20.0 0.0 14.1 0.0 3.4 150 FTG ET FE 0.0 31 20.0 0.0 13.8 0.0 0.020 TL 16.25 PV Pipe: 31 10.2 1.101 PL 10.50 FE 0.3 31 20.0 0.0 13.8 0.0 3.4 150 FTG E FE 4.5 32 9.5 0.0 18.0 0.0 0.020 TL 17.50 PV Pipe: 32 10.2 1.654 FL 3.75 PF 0.0 32 9.5 0.0 18.0 0.0 1.5 120 FTG E PE 0.0 33 9.5 0.0 17.9 0.0 0.004 TL 8.31 PV Pipe: 33 39.4 1.083 FL 0.50 PF 2.5 33 9.5 0.0 17.9 0.0 13.7 120 FTG T FE -0.2 34 10.0 0.0 15.2 0.0 0.390 TL 6.34 PV Pipe: 34 39.4 1.083 FL 2.00 PF 1.7 34 10.0 0.0 15.2 0.0 13.7 120 FTG E FE 0.0 35, 10.0. 0.0 13.5 0.0 0.390 TL 4.34 PV Pipe: 35 19.9 1.083 PL 2.75 PF 0.9 35 10.0 0.0 13.5 0.0 6.9 120 FTG T FE 0.0 36 10.0 5.6 12.6 19.9 0.110 TL 8.59 PV P Pipe: 36 19.5 1.083 FL 11.00 PE 1.4 35 10.0 0.0 13.5 0.0 6.8 120 FTG E FE 0.0 37 10.0 5.6 12.1 19.5 0.106 TL 13.34 PV Pipe: 37 -29.2 1.654 FL 13.50 FE 0.4 33 9.5 0.0 17.9 0.0 4.4 120 FTG ---- FE 0.0 38 9.5 0.0 18.3 0.0 0.029 TL 13.50 PV Pipe: 38 39.8 1.083 FL 0.50 PF 2.5 38 9.5 0.0 18.3 0.0 13.9 120 FTG T FE -0.2 39 10.0 0.0 15.6 0.0 0.398 TL 6.34 PV I 3.- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA i\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 39.8 1.083 PL 2.00 PF 1.7 39 10.0 0.0 15.6 0.0 13.9 120 FTG E PE 0.0 40 10.0 0.0 13.8 0.0 0.398 TL 4.34 PV Pipe: 40 20.2 1.083 PL 2.00 PF 0.9 40 10.0 0.0 13.8 0.0 7.0 120 FTG T PE 0.0 41 10.0 5.6 13.0 20.2 0.113 TL 7.84 PV Pipe: 41 19.7 1.083 PL 11.50 PP 1.5 40 10.0 0.0 13.8 0.0 6.9 120 FTG E PE 0.0 42 10.0 5.6 12.3 19.7 0.108 TL 13.84 PV Pipe: 42 -69.0 1.654 PL 27.00 PF 5.7 38 9.5 0.0 18.3 0.0 10.3 120 FTG 3E PE 0.0 43 9.5 0.0 24.0 0.0 0.140 TL 40.68 PV Pipe: 43 10.2 1.654 PL 74.75 PP 0.5 43 9.5 0.0 24.0 0.0 1.5 120 FTG GET PE 0.0 44 9.5 0.0 23.6 0.0 0.004 TL 111.23 PV Pipe: 44 -10.2 1.101 PL 10.50 PF 0.6 21 20.0 0.0 18.4 0.0 3.4 120 FTG 2E PE 4.5 44 9.5 0.0 23.6 0.0 0.029 TL 19.76 PV Pipe: 45 -79.2 2.705 PL 14.00 PF 0.8 43 9.5 0.0 24.0 0.0 4.4 120 FTG 2ET PE 0.0 TOP 9.5 0.0 24.9 0.0 0.016 TL 51.44 PV Pipe: 46 -79.2 2.705 PL 5.50 PF 0.5 TOP 9.5 0.0 24.9 0.0 4.4 120 FTG C PE 2.4 MID 4.0 0.0 27.7 0.0 0.016 TL 27.34 PV Pipe: 47 -79.2 2.705 PL 3.00 PP 0.0 MID 4.0 0.0 27.7 0.0 4.4 120 FTG ---- PE 1.3 BTM 1.0 0.0 29.0 0.0 0.016 TL 3.00 PV Pipe: 48 -79.2 4.026 PL 10.00 PP 0.0 BTM 1.0 0.0 29.0 0.0 2.0 120 FTG E PE 2.2 Ui -4.0 0.0 31.3 0.0 0.002 TL 20.00 PV Pipe: 49 -79.2 4.240 PL 219.75 PF 0.3 Ui -4.0 0.0 31.3 0.0 1.8 150 FTG 3E PE 0.0 U2 -4.0 0.0 31.6 0.0 0.001 TL 279.75 PV Pipe: 50 -79.2 4.240 PL 3.50 PP 0.0 U2 -4.0 0.0 31.6 0.0 1.8 150 FTG ---- PE 0.0 U3 -4.0 0.0 31.6 0.0 0.001 TL 3.50 PV Pipe: 51 -79.2 4.220 PL 7.00 PF 0.1 U3 -4.0 0.0 31.6 0.0 1.8 140 FTG 2E PE -3.0 U4 3.0 0.0 28.6 0.0 0.001 TL 41.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 36.6 0.0 8.0 psi, 79.2 gpm U4 3.0 0.0 28.6 0.0 Pipe: 53 -79.2 4.220 PL 7.00 PF 0.0 U5 3.0 0.0 36.6 0.0 1.8 140 FTG E PE 3.0 U6 -4.0 0.0 39.7 0.0 0.001 TL 24.00 PV Pipe: 54 -79.2 4.240 PL 22.50 PF 0.1 U6 -4.0 0.0 39.7 0.0 1.8 150 FTG E PE 0.0 SRC -4.0 SRCE 39.7 (N/A) 0.001 TL 42.50 PV NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.080 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 13.9 ft/sec at pipe 38. 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.. 83.41 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C 0 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd 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 NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 PAGE: X MATERIAL: EdFlw 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 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 1 $ I I I I I I I .4 * / I .4 .4 .4 .4 I 41P I / / 4f I I I I C C bo C H C Ci) 000 kc') C(J (ID • II >d UD0 C-(04J U) r- iDr-0CiCi a) 1-1 11) OWU) 0- co C) 04 WI -OD C(CiOCi)-I (Ci OOD(Ci '0>( dc') SCIDCID • U'. 7r Ci)0 C C C C C C • C C C C C 00 1-0 (N —QU)-H--. SPRINKLER SYSTEM 8YDRAULIC ANALYSIS Page 10 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\EUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: C C C C H C 0 C co C C C -zr C C SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/1/2016 SPRINKLERS\CALCS\DELTA 1\BUILDING 2 - 1ST FLOOR GARAGE.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ *\ I 0\ 80+ \ \ \ 72+ \ P64+ \ R I \ E I \\ S I 5 56+ \ U I R I E I \ 48+ \\ \ P I \ S \ I 40+X \ I \\ 32+ \ 24+ \: I * <-20.0 psi 8 1500 gpm Flow Test Point 16+ LEGEND I X = Required Water Supply I 39.74 psi 8 179.2 gpm 8+ I 0 = Available Water Supply I 84.21 psi 8 179.2 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) X 4 RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 2 - 2ND FLOOR RESIDENTIAL FILE NUMBER: 9301 DATE: FEB 1, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (8 BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER LIGHT HAZARD 0.10 gpm/sq. ft. 4 HEADS 8 18'X18' 18 'X18 4 sprinklers 70.2 gpm 170.2 gpm 70.2 gpm 8 49.3 psi 7/16 inch RESIDENTIAL FIRE SYSTEMS, INC. RAFAEL E. CARLSBAD FIRE DEPARTMENT C-16 #786965 CALCULATIONS BYHASS COMPUTER PROGRAM (LICENSE # 38061304 ) HRS SYSTEMS, INC. 1 NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE (FT) (PSI) 1 30.0 - - - - 11.9 2 30.0 - - - - 11.9 3 30.0 - - - - 11.9 4 30.0 - - - - 16.9 5 30.0 - - - - 10.9 6 30.0 - - - - 10.9 7 30.0 - - - - 10.6 8 30.0 - - - - 10.0 9 30.0 - - - - 10.0 10 30.0 - - - - 9.6 11 30.0 - - - 10.6 12 30.0 - - - - 10.2 13 30.0 - - - - 10.6 14 30.0 - - - - 9.9 15 30.0 - - - - 9.8 16 30.0 - - - - 9.9 17 30.0 - - - 14.0 18 18 30.0 - - - - 22.1 19 30.0 - - - - 27.1 20 30.0 - - - - 27.8 21 20.0 - - - - 34.1 22 20.0 - - - - 13.3 23 20.0 K= 4.90 12.3 24 20.0 - - - - 13.7 25 20:0 K= 4.90 12.7 26 20.0 - - - - 13.1 27 20.0 K= 4.90 12.0 28 20.0 - - - - 15.3 29 20.0 K= 4.90 14.3 30 20.0 - - - - 26.2 31 20.0 - - - - 31.0 32 9.5 - - - - 40.7 33 9.5 - - - - 41.2 DISCHARGE (GPM) 17.2 17.5 17.0 18.5 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: 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 85.5 20.0 1500.0 84.3 170.2 59.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 170.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 70.2 GPM SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/1/2016NKLER5\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 10.0 - - - - 41.0 - - - 35 10.0 - - - - 41.0 - - - 36 10.0 - - - - 41.0 - - - 37 10.0 - - - - 41.0 - - - 38 9.5 - - - - 42.0 - - - 39 10.0 - - - - 41.8 - - - 40 10.0 - - - - 41.8 - - - 41 10.0 - - - - 41.8 - - - 42 10.0 - - - - 41.8 - - - 43 9.5 - - - - 44.5 - - - 44 9.5 - - - - 41.9 - - - TOP 9.5 - - - - 45.2 - - - MID 4.0 - - - - 47.9 - - - BTM 1.0 - - - - 49.3 - - - Ui -4.0 - - - - 51.5 - - - U2 -4.0 - - - - 51.8 - - - U3 -4.0 - - - - 51.8 - - - U4 3.0 - - - - 48.8 - - - U5 3.0 - - - - 56.8 U6 -4.0 - - - - 59.8 - - - SRC -4.0 SOURCE 59.9 70.2 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\EUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 8.00 PF 0.0 1 30.0 0.0 11.9 0.0 0.0 150 FTG T PE 0.0 2 30.0 0.0 11.9 0.0 0.000 TL 13.00 PV Pipe: 2 -18.5 1.101 PL 1.25 PF 0.1 2 30.0 0.0 11.9 0.0 6.2 150 FTG ---- PE 0.0 3 30.0 0.0 11.9 0.0 0.059 TL 1.25 PV Pipe: 3 -44.1 1.101 PL 5.00 PF 5.0 3 30.0 0.0 11.9 0.0 14.9 150 FTG ET PE 0.0 4 30.0 0.0 16.9 0.0 0.294 TL 17.00 PV Pipe: 4 25.6 1.101 PL 4.75 PF 1.0 3 30.0 0.0 11.9 0.0 8.6 150 FTG T PE 0.0 5 30.0 0.0 10.9 0.0 0.107 TL 9.75 PV Pipe: 5 0.0 1.101 PL 0.50 PF 0.0 5 30.0 0.0 10.9 0.0 0.0 150 FTG T PE 0.0 6 30.0 0.0 10.9 0.0 0.000 TL 5.50 PV Pipe: 6 25.6 1.101 PL 2.25 PF 0.2 5 30.0 0.0 10.9 0.0 8.6 150 FTG ---- PE 0.0 7 30.0 0.0 10.6 0.0 0.107 TL 2.25 PV Pipe: 7 17.0 1.101 PL 8.25 PF 0.7 7 30.0 0.0 10.6 0.0 5.7 150 FTG T PE 0.0 8 30.0 0.0 10.0 0.0 0.050 TL 13.25 PV Pipe: 8 0.0 1.101 PL 2.50 PF 0.0 8 30.0 0.0 10.0 0.0 0.0 150 FTG T PE 0.0 9 30.0 0.0 10.0 0.0 0.000 TL 7.50 PV Pipe: 9 17.0 1.101 PL 7.00 PF 0.4 8 30.0 0.0 10.0 0.0 5.7 150 FTG ---- PE 0.0 10 30.0 0.0 9.6 0.0 0.050 TL 7.00 PV Pipe: 10 8.6 1.101 PL 4.00 PF 0.1 7 30.0 0.0 10.6 0.0 2.9 150 FTG ---- PE 0.0 11 30.0 0.0 10.6 0.0 0.014 TL 4.00 PV ci Pipe: 11 17.5 1.101 PL 1.25 PF 0.3 11 30.0 0.0 10.6 0.0 5.9 150 FTG T PE 0.0 12 30.0 0.0 10.2 0.0 0.053 TL 6.25 PV Pipe: 12 -8.9 1.101 PL 1.75 PF 0.0 11 30.0 0.0 10.6 0.0 3.0 150 FTG ---- PE 0.0 13 30.0 0.0 10.6 0.0 0.015 TL 1.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: 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 17.2 1.101 PL 9.00 PP 0.7 13 30.0 0.0 10.6 0.0 5.8 150 FTG T PE 0.0 14 30.0 0.0 9.9 0.0 0.052 TL 14.00 PV Pipe: 14 17.2 1.101 PL 1.75 PP 0.1 14 30.0 0.0 9.9 0.0 5.8 150 FTG ---- PE 0.0 15 30.0 0.0 9.8 0.0 0.052 TL 1.75 PV Pipe: 15 0.0 1.101 PL 2.00 PF 0.0 14 30.0 0.0 9.9 0.0 0.0 150 FTG T PE 0.0 16 30.0 0.0 9.9 0.0 0.000 TL 7.00 PV Pipe: 16 -26.1 1.101 FL 26.50 PP 3.4 13 30.0 0.0 10.6 0.0 8.8 150 FTG 4F PE 0.0 17 30.0 0.0 14.0 0.0 0.111 TL 30.50 PV Pipe: 17 -26.1 1.101 PL 48.00 PP 8.1 17 30.0 0.0 14.0 0.0 8.8 150 FTG 4F3E PE 0.0 18 30.0 0.0 22.1 0.0 0.111 TL 73.00 PV Pipe: 18 -26.1 1.101 PL 21.75 PF 5.0 18 30.0 0.0 22.1 0.0 8.8 150 FTG 4F2ET PE 0.0 19 30.0 0.0 27.1 0.0 0.111 TL 44.75 PV Pipe: 19 -26.1 1.101 PL 1.50 PF 0.7 19 30.0 0.0 27.1 0.0 8.8 150 FTG T FE 0.0 20 30.0 0.0 27.8 0.0 0.111 TL 6.50 PV Pipe: 20 -26.1 1.101 PL 10.00 PF 1.9 20 30.0 0.0 27.8 0.0 8.8 150 FTG E PE 4.3 21 20.0 0.0 34.1 0.0 0.111 TL 17.00 PV Pipe: 21 17.2 1.101 PL 10.00 PF 0.9 15 30.0 0.0 9.8 0.0 5.8 150 FTG E PE 4.3 22 20.0 0.0 13.3 0.0 0.052 TL 17.00 PV Pipe: 22 17.2 1.101 PL 3.75 PF 0.9 22 20.0 0.0 13.3 0.0 5.8 150 FTG 2E FE 0.0 23 20.0 4.9 12.3 17.2 0.052 TL 17.75 PV Pipe: 23 17.5 1.101 PL 10.00 PP 0.9 12 30.0 0.0 10.2 0.0 5.9 150 FTG E PE 4.3 24 20.0 0.0 13.7 -'0.0' 0.053 TL 17.00 PV Pipe: 24 17.5 1.101 PL 4.00 PP 1.0 24 20.0 0.0 13.7 0.0 5.9 150 FTG 2E PE 0.0 25 20.0 4.9 12.7 17.5 0.053 TL 18.00 PV Pipe: 25 17.0 1.101 PL 10.00 PF 0.9 10 30.0 0.0 9.6 0.0 5.7 150 FTG E PE 4.3 26 20.0 0.0 13.1 0.0 0.050 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: 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 17.0 1.101 PL 9.00 PF 1.1 26 20.0 0.0 13.1 0.0 5.7 150 FTG ET PE 0.0 27 20.0 4.9 12.0 17.0 0.050 TL 21.00 PV Pipe: 27 18.5 1.101 PL 10.00 PF 0.9 2 30.0 0.0 11.9 0.0 6.2 150 FTG T PE 4.3 28 20.0 0.0 15.3 0.0 0.059 TL 15.00 PV Pipe: 28 18.5 1.101 PL 3.50 PP 1.0 * 28 20.0 0.0 15.3 0.0 6.2 150 FTG 2E PS 0.0 29 20.0 4.9 14.3 18.5 0.059 TL 17.50 PV Pipe: 29 -44.1 1.101 FL 10.00 PF 5.0 4 30.0 0.0 16.9 0.0 14.9 150 FTG E PE 4.3 30 20.0 0.0 26.2 0.0 0.294 TL 17.00 PV Pipe: 30 -44.1 1.101 PL 4.25 PP 4.8 30 20.0 0.0 26.2 0.0 14.9 150 FTG ST PE 0.0 31 20.0 0.0 31.0 0.0 0.294 TL 16.25 PV Pipe: 31 -44.1 1.101 PL 10.50 PF 5.1 31 20.0 0.0 31.0 0.0 14.9 150 FTG E PS 4.5 32 9.5 0.0 40.7 0.0 0.294 TL 17.50 PV Pipe: 32 -44.1 1.654 PL 3.75 PF 0.5 32 9.5 0.0 40.7 0.0 6.6 120 FTG S PE 0.0 33 9.5 0.0 41.2 0.0 0.061 TL 8.31 PV Pipe: 33 0.0 1.083 PL 0.50 PP 0.0 33 9.5 0.0 41.2 0.0 0.0 120 FTG T PE -0.2 34 10.0 0.0 41.0 0.0 0.000 TL 6.34 PV Pipe: 34 0.0 1.083 FL 2.00 PF 0.0 34 10.0 0.0 41.0 0.0 0.0 120 FTG S PS 0.0 35.. 10.0 0.0 41.0 0.0 0.00.0 TL PV. Pipe: 35 0.0 1.083 PL 2.75 PF 0.0 35 10.0 0.0 41.0 0.0 0.0 120 FTG T PS 0.0 36 10.0 0.0 41.0 0.0 0.000 TL 8.59 PV Pipe: 36 0.0 1.083 PL 11.00 PP 0.0 35 10.0 0.0 41.0 0.0 0.0 120 FTG E PS 0.0 37 10.0 0.0 41.0 0.0 0.000 TL 13.34 PV Pipe: 37 -44.1 1.654 PL 13.50 PF 0.8 33 9.5 0.0 41.2 0.0 6.6 120 FTG ---- PE 0.0 38 9.5 0.0 42.0 0.0 0.061 TL 13.50 PV Pipe: 38 0.0 1.083 PL 0.50 PF 0.0 38 9.5 0.0 42.0 0.0 0.0 120 FTG T PS -0.2 39 10.0 0.0 41.8 0.0 0.000 TL 6.34 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 0.0 1.083 PL 2.00 PF 0.0 39 10.0 0.0 41.8 0.0 0.0 120 FTG E PE 0.0 40 10.0 0.0 41.8 0.0 0.000 TL 4.34 PV Pipe: 40 0.0 1.083 PL 2.00 PF 0.0 40 10.0 0.0 41.8 0.0 0.0 120 FTG T PE 0.0 41 10.0 0.0 41.8 0.0 0.000 TL 7.84 PV Pipe: 41 0.0 1.083 PL 11.50 PF 0.0 40 10.0 0.0 41.8 0.0 0.0 120 FTG E PE 0.0 42 10.0 0.0 41.8 0.0 0.000 TL 13.84 PV Pipe: 42 -44.1 1.654 PL 27.00 PF 2.5 38 9.5 0.0 42.0 0.0 6.6 120 FTG 3E PE 0.0 43 9.5 0.0 44.5 0.0 0.061 TL 40.68 PV Pipe: 43 26.1 1.654 PL 74.75 PF 2.6 43 9.5 0.0 44.5 0.0 3.9 120 FTG 6ET PE 0.0 44 9.5 0.0 41.9 0.0 0.023 TL 111.23 PV Pipe: 44 -26.1 1.101 PL 10.50 PF 3.3 21 20.0 0.0 34.1 0.0 8.8 120 FTG 2E PE 4.5 44 9.5 0.0 41.9 0.0 0.168 TL 19.76 PV Pipe: 45 -70.2 2.705 PL 14.00 PF 0.7 43 9.5 0.0 44.5 0.0 3.9 120 FTG 2ET PE 0.0 TOP 9.5 0.0 45.2 0.0 0.013 TL 51.44 PV Pipe: 46 -70.2 2.705 PL 5.50 PF 0.4 TOP 9.5 0.0 45.2 0.0 3.9 120 FTG C PE 2.4 MID 4.0 0.0 47.9 0.0 0.013 TL 27.34 PV Pipe: 47 -70.2 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 47.9 0.0 3.9 120 FTG ---- PE 1.3 BTM 1.0 0.0 49.3 0.0 0.013 TL 3.00 PV Pipe: 48 -70.2 4.026 PL 10.00 PF 0.0 ETM 1.0 0.0 49.3 0.0 1.8 120 FTG E PE 2.2 Ui -4.0 0.0 51.5 0.0 0.002 TL 20.00 PV Pipe: 49 -70.2 4.240 PL 219.75 PF 0.3 Ui -4.0 0.0 51.5 0.0 1.6 150 FTG 3E PE 0.0 U2 -4.0 0.0 51.8 0.0 0.001 TL 279.75 PV • Pipe: 50 -70.2 4.240 PL 3.50 PF 0.0 U2 -4.0 0.0 51.8 0.0 1.6 150 FTG ---- PE 0.0 U3 -4.0 0.0 51.8 0.0 0.001 TL 3.50 PV Pipe: 51 -70.2 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 51.8 0.0 1.6 140 FTG 2E PE -3.0 U4 3.0 0.0 48.8 0.0 0.001 TL 41.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 56.8 0.0 8.0 psi, 70.2 gpm U4 3.0 0.0 48.8 0.0 Pipe: 53 -70.2 4.220 PL 7.00 PF 0.0 U5 3.0 0.0 56.8 0.0 1.6 140 FTG E PE 3.0 U6 -4.0 0.0 59.8 0.0 0.001 TL 24.00 PV Pipe: 54 -70.2 4.240 PL 22.50 PF 0.0 U6 -4.0 0.0 59.8 0.0 1.6 150 FTG E PE 0.0 SRC -4.0 SRCE 59.9 (N/A) 0.001 TL 42.50 PV NOTES (BASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 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 0.068 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.9 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 condition.sis 84.08 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE '4 Pipe Table Name: STANDARD.PIP U SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/1/2016NKLER5\CALCS\DELTA l\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd 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 NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 PAGE: X MATERIAL: EdF1w HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) B T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPV1v NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\EUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOE TITLE: E 0 ci) 000 C) C'J D . dc') C/) L • u) c) 0-c4-) o CON 01.-I CON0dCO CO.-I00 L0 QCO) (I 0G)d) L4COC/)I)-1 .0 .-IU) -(010(d '001001.--I .0 04 (ci w0I4-•-( 1-4 (O (O o dc') 4 OD 0>( ) OD CI)C/)< cl(ci• CO' 0'. (1)O (3 114 CD co Lf) Ln co co I I I I 0 I I .. II / 'I / I I / I 0 / 0 lop / I / -I 4 0 0 0 0 0 0 0 C) 0 o o 0 0 (N C) W(3t 0U)W E —Q0-H-- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/l/2016NKLER5\CALCS\DELTA l\BUILDING 2 - 2ND FLOOR RESIDENTIAL.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ *\ 0\ 80+ \ I \ 72+ I \ I \ P 64+ R I \ E IX \\ S I S 56+ U I \ R I \ E I \ 48+ \\ ( I \ P I \ S I \ I 40+ \ I \\ 32+ 24+ \ * <-20.0 psi 8 1500 gpm Flow Test Point 16+ LEGEND I X = Required Water Supply I 59.88 psi 8 170.2 gpm 8+ 0 = Available Water Supply 84.33 psi 8 170.2 gpm +------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 E. CRYSTAL DRIVE ANAHEIM,CA 92807 HYDRAULIC CALCULATIONS FOR VILLAGE 201 - CARLSBAD BUILDING 2 - 3RD FLOOR RESIDENTIAL FILE NUMBER: 9301 DATE: FEB 1, 2016 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (8 BOR) SPRINKLER ORIFICE SIZE: NAME OF CONTRACTOR: DESIGN/LAYOUT BY: AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER LIGHT HAZARD 0.10 gpm/sq. ft. 4 HEADS 8 18'X18' 18'X18 ' 4 sprinklers 69.5 gpm 169.5 gpm 69.5 gpm 8 51.2 psi 7/16 inch RESIDENTIAL FIRE SYSTEMS, INC. RAFAEL E. CARLSBAD FIRE DEPARTMENT C-16 #786965 CALCULATIONS BYHASS COMPUTER PROGRAM (LICENSE # 38061304 ) HRS SYSTEMS, INC. * SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 85.5 20.0 1500.0 84.3 169.5 61.8 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 169.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 69.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 30.0 K= 4.90 13.4 17.9 2 30.0 - - - - 14.1 - - - 3 30.0 - - - - 14.2 - - - 4 30.0 - - - - 19.1 - - - 5 30.0 - - - - 13.1 - - - 6 30.0 K= 4.90 12.8 17.5 7 30.0 - - - - 13.1 - - - 8 30.0 - - - - 12.4 - - - 9 30.0 K= 4.90 12.0 17.0 10 30.0 - - - - 12.4 - - - 11 30.0 - - - - 13.1 - - - 12 30.0 - - - - 13.1 - - - 13 30.0 - - - - 13.2 - - - 14 30.0 - - - - 12.5 - - 15 30.0 - - - - 12.5 - - - 16 30.0 K= 4.90 12.1 17.0 17 30.0 - - 16.5. - - 18 30.0 - - - - 24.4 - - - 19 30.0 - - - - 29.3 - - - 20 30.0 - - - - 30.0 - - - 21 20.0 - - - - 36.1 - - - 22 20.0 - - - - 16.8 - - - 23 20.0 - - - - 16.8 - - - 24 20.0 - - - - 17.5 - - - 25 20.0 - - - - 17.5 - - - 26 20.0 - - - - 16.7 - - - 27 20.0 - - - - 16.7 - - - 28 20.0 - - - - 18.4 - - - 29 20.0 - - - 18.4 - - - 30 20.0 - - - - 28.4 - - - 31 20.0 - - - - 33.1 - - - 32 9.5 - - - - 42.7 - - - 33 9.5 - - - - 43.2 - - - I 4,' 4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/i/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 10.0 - - - - 43.0 - - - 35 10.0 - - - - 43.0 - - - 36 10.0 - - - - 43.0 - - - 37 10.0 - - - - 43.0 - - - 38 9.5 - - - - 44.0 - - - 39 10.0 - - - - 43.8 - - - 40 10.0 - - - - 43.8 - - - 41 10.0 - - - - 43.8 - - - 42 10.0 - - - - 43.8 - - - 43 9.5 - - - - 46.5 - - - 44 9.5 - - - - 43.9 - - - TOP 9.5 - - - - 47.1 - - - MID 4.0 - - - - 49.9 - - - ETM 1.0 - - - - 51.2 - - - Ui -4.0 - - - - 53.4 - - - U2 -4.0 - - - - 53.7 U3 -4.0 - - - - 53.7 U4 3.0 - - - - 50.7 US 3.0 - - - - 58.7 - - - U6 -4.0 - - - - 61.7 - - - SRC -4.0 SOURCE 61.8 69.5 .1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 -17.9 1.101 PL 8.00 PF 0.7 1 30.0 4.9 13.4 17.9 6.0 150 FTG T PE 0.0 2 30.0 0.0 14.1 0.0 0.056 TL 13.00 PV Pipe: 2 -17.9 1.101 PL 1.25 PF 0.1 2 30.0 0.0 14.1 0.0 6.0 150 FTG ---- PE 0.0 3 30.0 0.0 14.2 0.0 0.056 TL 1.25 PV Pipe: 3 -43.8 1.101 PL 5.00 PF 4.9 3 30.0 0.0 14.2 0.0 14.7 150 FTG ET FE 0.0 4 30.0 0.0 19.1 0.0 0.290 TL 17.00 PV Pipe: 4 25.8 1.101 PL 4.75 PF 1.1 3 30.0 0.0 14.2 0.0 8.7 150 FTG T PE 0.0 5 30.0 0.0 13.1 0.0 0.109 TL 9.75 PV Pipe: 5 17.5 1.101 PL 0.50 PF 0.3 5 30.0 0.0 13.1 0.0 5.9 150 FTG T PE 0.0 6 30.0 4.9 12.8 17.5 0.053 TL 5.50 PV Pipe: 6 8.3 1.101 PL 2.25 PF 0.0 5 30.0 0.0 13.1 0.0 2.8 150 FTG ---- PE 0.0 7 30.0 0.0 13.1 0.0 0.013 TL 2.25 PV Pipe: 7 17.0 1.101 PL 8.25 PF 0.7 7 30.0 0.0 13.1 0.0 5.7 150 FTG T FE 0.0 8 30.0 0.0 12.4 0.0 0.050 TL 13.25 PV Pipe: 8 17.0 1.101 PL 2.50 PF 0.4 8 30.0 0.0 12.4 0.0 5.7 150 FTG T PE 0.0 9 30.0 4.9 12.0 17.0 0.050 TL 7.50 PV Pipe: 9 0.0 1.101 FL 7.00 . PF .0.5 8 30.0 0.0 12.4 0.0 0.0 150 FTG ---- PE 0.0 10 30.0 0.0 12.4 0.0 0.000 TL 7.00 PV Pipe: 10 -8.7 1.101 FL 4.00 PF 0.1 7 30.0 0.0 13.1 0.0 2.9 150 FTG ---- FE 0.0 11 30.0 0.0 13.1 0.0 0.015 TL 4.00 PV Pipe: 11 0.0 1.101 PL 1.25 PF 0.0 11 30.0 0.0 13.1 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 13.1 0.0 0.000 TL 6.25 PV Pipe: 12 -8.7 1.101 FL 1.75 PF 0.0 11 30.0 0.0 13.1 0.0 2.9 150 FTG ---- FE 0.0 13 30.0 0.0 13.2 0.0 0.015 TL 1.75 PV 0' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 17.0 1.101 PL 9.00 PF 0.7 13 30.0 0.0 13.2 0.0 5.7 150 FTG T PE 0.0 14 30.0 0.0 12.5 0.0 0.051 TL 14.00 PV Pipe: 14 0.0 1.101 PL 1.75 PP 0.0 14 30.0 0.0 12.5 0.0 0.0 150 FTG ---- PE 0.0 15 30.0 0.0 12.5 0.0 0.000 TL 1.75 PV Pipe: 15 17.0 1.101 PL 2.00 PF 0.4 14 30.0 0.0 12.5 0.0 5.7 150 FTG T PE 0.0 16 30.0 4.9 12.1 17.0 0.051 TL 7.00 PV Pipe: 16 -25.8 1.101 PL 26.50 PP 3.3 13 30.0 0.0 13.2 0.0 8.7 150 FTG 4F PE 0.0 17 30.0 0.0 16.5 0.0 0.109 TL 30.50 PV Pipe: 17 -25.8 1.101 PL 48.00 PF 7.9 17 30.0 0.0 16.5 0.0 8.7 150 FTG 4F3E PE 0.0 18 30.0 0.0 24.4 0.0 0.109 TL 73.00 PV Pipe: 18 -25.8 1.101 PL 21.75 PP 4.9 18 30.0 0.0 24.4 0.0 8.7 150 FTG 4F2ET PE 0.0 19 30.0 0.0 29.3 0.0 0.109 TL 44.75 PV Pipe: 19 -25.8 1.101 PL 1.50 PF 0.7 19 30.0 0.0 29.3 0.0 8.7 150 FTG T PE 0.0 20 30.0 0.0 30.0 0.0 0.109 TL 6.50 PV Pipe: 20 -25.8 1.101 PL 10.00 PF 1.8 20 30.0 0.0 30.0 0.0 8.7 150 FTG E PE 4.3 21 20.0 0.0 36.1 0.0 0.109 TL 17.00 PV Pipe: 21 0.0 1.101 PL 10.00 PP 0.0 15 30.0 0.0 12.5 0.0 0.0 150 FTG E PE 4.3 22 20.0 0.0 16.8 0.0 0.000 TL 17.00 PV Pipe: 22 0.0 1.101 PL 3.75 PF 0.0 22 20.0 0.0 16.8 0.0 0.0 150 FTG 2E PE 0.0 23 20.0 0.0 16.8 0.0 0.000 TL 17.75 PV Pipe: 23 0.0 1.101 PL 10.00 PF 0.0 12 30.0 0.0 13.1 0.0 0.0 150 FTG E PE 4.3 24 20.0 0.0 17.5 0.0 0.000 TL 17.00 PV Pipe: 24 0.0 1.101 PL 4.00 PP 0.0 24 20.0 0.0 17.5 0.0 0.0 150 FTG 2E PE 0.0 25 20.0 0.0 17.5 0.0 0.000 TL 18.00 PV Pipe: 25 0.0 1.101 PL 10.00 PF 0.0 10 30.0 0.0 12.4 0.0 0.0 150 FTG E PE 4.3 26 20.0 0.0 16.7 0.0 0.000 TL 17.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 1.101 PL 9.00 PP 0.0 26 20.0 0.0 16.7 0.0 0.0 150 FTG ET PE 0.0 27 20.0 0.0 16.7 0.0 0.000 TL 21.00 PV Pipe: 27 0.0 1.101 PL 10.00 PF 0.0 2 30.0 0.0 14.1 0.0 0.0 150 FTG T PE 4.3 28 20.0 0.0 18.4 0.0 0.000 TL 15.00 PV Pipe: 28 0.0 1.101 PL 3.50 PP 0.0 28 20.0 0.0 18.4 0.0 0.0 150 FTG 2E PE 0.0 29 20.0 0.0 18.4 0.0 0.000 TL 17.50 PV Pipe: 29 -43.8 1.101 PL 10.00 PP 4.9 4 30.0 0.0 19.1 0.0 14.7 150 FTG E PE 4.3 30 20.0 0.0 28.4 0.0 0.290 TL 17.00 PV Pipe: 30 -43.8 1.101 PL 4.25 PF 4.7 30 20.0 0.0 28.4 0.0 14.7 150 FTG ET PE 0.0 31 20.0 0.0 33.1 0.0 0.290 TL 16.25 PV Pipe: 31 -43.8 1.101 FL 10.50 PF 5.1 31 20.0 0.0 33.1 0.0 14.7 150 FTG E PE 4.5 32 9.5 0.0 42.7 0.0 0.290 TL 17.50 PV Pipe: 32 -43.8 1.654 PL 3.75 PF 0.5 32 9.5 0.0 42.7 0.0 6.5 120 FTG E PE 0.0 33 9.5 0.0 43.2 0.0 0.060 TL 8.31 PV Pipe: 33 0.0 1.083 PL 0.50 PF 0.0 33 9.5 0.0 43.2 0.0 0.0 120 FTG T PE -0.2 34 10.0 0.0 43.0 0.0 0.000 TL 6.34 PV Pipe: 34 0.0 1.083 PL 2.00 PF 0.0 34 10.0 0.0 43.0 0.0 0.0 120 FTG E PE 0.0 35 10.0 0.0. 43.0 .0.0 0.000 TL.. 4.34 PV . Pipe: 35 0.0 1.083 PL 2.75 PF 0.0 35 10.0 0.0 43.0 0.0 0.0 120 FTG T PE 0.0 36 10.0 0.0 43.0 0.0 0.000 TL 8.59 PV 4 Pipe: 36 0.0 1.083 PL 11.00 PF 0.0 35 10.0 0.0 43.0 0.0 0.0 120 FTG E PE 0.0 37 10.0 0.0 43.0 0.0 0.000 TL 13.34 PV Pipe: 37 -43.8 1.654 PL 13.50 PF 0.8 33 9.5 0.0 43.2 0.0 6.5 120 FTG ---- PE 0.0 38 9.5 0.0 44.0 0.0 0.060 TL 13.50 PV Pipe: 38 0.0 1.083 PL 0.50 PF 0.0 38 9.5 0.0 44.0 0.0 0.0 120 FTG T PE -0.2 39 10.0 0.0 43.8 0.0 0.000 TL 6.34 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/1/2016NKLERS\CALCS\DELTA i\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOE TITLE: 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 0.0 1.083 PL 2.00 PF 0.0 39 10.0 0.0 43.8 0.0 0.0 120 FTG E PE 0.0 40 10.0 0.0 43.8 0.0 0.000 TL 4.34 PV Pipe: 40 0.0 1.083 PL 2.00 PF 0.0 40 10.0 0.0 43.8 0.0 0.0 120 FTG T PE 0.0 41 10.0 0.0 43.8 0.0 0.000 TL 7.84 PV Pipe: 41 0.0 1.083 PL 11.50 PF 0.0 40 10.0 0.0 43.8 0.0 0.0 120 FTG E PE 0.0 42 10.0 0.0 43.8 0.0 0.000 TL 13.84 PV Pipe: 42 -43.8 1.654 PL 27.00 PF 2.5 38 9.5 0.0 44.0 0.0 6.5 120 FTG 3E PE 0.0 43 9.5 0.0 46.5 0.0 0.060 TL 40.68 PV Pipe: 43 25.8 1.654 PL 74.75 PF 2.5 43 9.5 0.0 46.5 0.0 3.8 120 FTG 6ET PE 0.0 44 9.5 0.0 43.9 0.0 0.023 TL 111.23 PV Pipe: 44 -25.8 1.101 PL 10.50 PF 3.2 21 20.0 0.0 36.1 0.0 8.7 120 FTG 2E PE 4.5 44 9.5 0.0 43.9 0.0 0.164 TL 19.76 PV Pipe: 45 -69.5 2.705 PL 14.00 PF 0.7 43 9.5 0.0 46.5 0.0 3.9 120 FTG 2ET FE 0.0 TOP 9.5 0.0 47.1 0.0 0.013 TL 51.44 PV Pipe: 46 -69.5 2.705 PL 5.50 PF 0.4 TOP 9.5 0.0 47.1 0.0 3.9 120 FTG C PE 2.4 MID 4.0 0.0 49.9 0.0 0.013 TL 27.34 PV Pipe: 47 -69.5 2.705 PL 3.00 PF 0.0 MID 4.0 0.0 49.9 0.0 3.9 120 FTG ---- PE 1.3 ETM 1.0 0.0 51.2 0.0 0.013 TL 3.00 PV Pipe: 48 -69.5 4.026 PL 10.00 PF 0.0 ETM 1.0 0.0 51.2 0.0 1.8 120 FTG E PE 2.2 Ui -4.0 0.0 53.4 0.0 0.002 TL 20.00 PV Pipe: 49 -69.5 4.240 PL 219.75 PF 0.3 Ui -4.0 0.0 53.4 0.0 1.6 150 FTG 3E PE 0.0 U2 -4.0 0.0 53.7 0.0 0.001 TL 279.75 PV Pipe: 50 -69.5 4.240 FL 3.50 PF 0.0 U2 -4.0 0.0 53.7 0.0 1.6 150 FTG ---- PE 0.0 U3 -4.0 0.0 53.7 0.0 0.001 TL 3.50 PV Pipe: 51 -69.5 4.220 PL 7.00 PF 0.0 U3 -4.0 0.0 53.7 0.0 1.6 140 FTG 2E FE -3.0 U4 3.0 0.0 50.7 0.0 0.001 TL 41.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HM(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 FIXED PRESSURE LOSS DEVICE U5 3.0 0.0 58.7 0.0 8.0 psi, 69.5 gpm U4 3.0 0.0 50.7 0.0 Pipe: 53 -69.5 4.220 PL 7.00 PF 0.0 U5 3.0 0.0 58.7 0.0 1.6 140 FTG E PE 3.0 U6 -4.0 0.0 61.7 0.0 0.001 TL 24.00 PV Pipe: 54 -69.5 4.240 PL 22.50 PF 0.0 U6 -4.0 0.0 61.7 0.0 1.6 150 FTG E PE 0.0 SRC -4.0 SRCE 61.8 (N/A) 0.001 TL 42.50 PV NOTES (HASS) Calculations were performed by the HASS 8.5 computer program under license no. 38061304 granted by MRS 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 0.073 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.7 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.. 84.09 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: 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 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 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 4.220 17.00 34.00 10.00 37.00 20.00 3.00 34.00 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 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.00 PAGE: F MATERIAL: CPVC HNC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G 45 El Tee RunT Kplg ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 PAGE: V MATERIAL: EdThrd 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 NPTee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 5.84 0.00 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.00 PAGE: X MATERIAL: EdFlw 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 DPViv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 A SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: S E a)cDG) 0 cL 000 D Lr) . a)Lfl (D U)O o a)'.0 a)0a)a) O 0.a) a) oaa )()1 04 .0 w.1 Ha)(a -a) u) u Q) a) .0 04 a QJH o 0> -() c;• N(0Cfl co 04 CD CN cf) CD 00 -H 4J 4J H 0 0 0 0 0 0 0 0 C') C/)Wc —00-H.--- 0 0 0 0 0 00 Y 0 0 0 C-.- 0 C) I I 4. 4. 0 CD 4. 4. .4 / I I / I I / I 0 I / 0 I 4,I / I / / / SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 DATE: 2/1/2016NKLERS\CALCS\DELTA 1\BUILDING 2 - 3RD FLOOR RESIDENTIAL.SDF JOB TITLE: WATER SUPPLY CURVE 96+ 88+ I 0\ \ 80+ \ I \ I \ 72+ \ I \ I \ P 64+ R IX \ E I \\ S I S 56+ \ U I R I E I \ 48+ \\ I \ I \ S I \ I 40+ \ 32+ \ \ 24+ I • V I * <-20.0 psi @ 1500 gpm I ============================== Flow Test Point 16+ LEGEND I X = Required Water Supply I 61.78 psi 8 169.5 gprn 8+ I 0 = Available Water Supply I 84.34 psi 8 169.5 gprn 0++-+---+----+-----+------+--------+--------+---------+-----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) FireLock® V27, K5.6 \/(ctauUi Models V2703, V2707, V2704, V2708 40.10 Standard Spray Upright, Pendent and Recessed Pendent Standard and Quick Response 4 72 V2703/V2704 V2707/V2708 V2707/V2 708 Upright Pendent Recessed Pendent Approvals/Listings: c®us j © 0786 See Victaulic Publication 10.01 for more details. Product Description: These Model V27 standard spray sprinklers are designed to produce a hemispherical spray pattern for standard commercial applications. They are available with either standard or quick response bulbs. It is cast with a hex-shaped wrench boss to allow easy tightening from many angles, reducing assembly effort. This sprinkler is available in various temperature ratings (see chart on page 3) and finishes to meet many design requirements. The recessed pendent should be utilized with a Model V27 recessed escutcheon which provides Up to I411 /19 mm of adjustments. Coverage For coverage area and sprinkler placement, refer to NFPA 13 or applicable standard. Technical Specifications: Models: V2703, V2704, V2707, V2708 Style: Pendent, Upright or Recessed Pendent Nominal Orifice Size: 1/2 I13 mm K Factor: 5.6 Imp./8.1 SI.' Nominal Thread Size: ½" NFl/iS mm Max. Working Pressure: 175 psi/1200 kPa (FM) 250 psi/1725 kPa (UL) Factory Hydrostatic Test: 100% @ 500 psi/3450 kPa Mm. Operating Pressure: 7 psi/48 kPa 0.35 bar/5 psi (VdS for upright only) Temperature Rating: See chart I For K-Factor when pressure is measured in Bar, multiply S.I. units by 10.0. Exaggerated for clarity Job/Owner Engineer System No. Spec Section Location Paragraph Contractor Approved Submitted By Date Date victaulic.com I Sprinklers I FireLockw I K5.6, V27 I Publication 40.10 40.10 2544 Rev. J Updated 07/2014 0 2014 victaulic company. All rights reserved. 1 JctauIic victaulic.com I Sprinklers I FireLock I K5.6, V27 I Publication 40.10 Material Specifications: Upright Deflector: Bronze per UNS C11000 Pendent Deflector: Bronze per UNS C51000 Bulb: Glass with glycerin solution Bulb Nominal Diameter: Standard: 5.0 mm Quick Response: 3.0 mm Load Screw: Bronze per UNS 065100 Pip Cap: Bronze per UNS 065100 Spring: Beryllium nickel Seal: Teflon2 tape Frame: Die cast brass 65-30 Lodgement Spring: Stainless steel per UNS S30200 Accessories Installation Wrench: Open End: V27 Recessed: V27-2 Sprinkler Finishes: Plain Brass Chrome plated White painted3 Black painted3 Custom painted3 Proprietary Nickel Teflon2 coating3 VC-2504 3 155, 200, 286 SR Only: Wax3 For cabinets and other accessories refer to separate sheet. 2 Teflon is a registered trademark of Dupont Co. UL Listed for corrosion resistance. UL Listed and FM Approved for corrosion resistance. 'I 40.10 2544 Rev. J Updated 07/2014 © 2014 Victaulic Company. All rights reserved. tcta!!c.corn 2 ictaUlic 4 vctau!ic.co..Sprinklers I FireLock' I K5.6, V27 I Publication 40.10 Approvals/Listings: Model APP OV R ALSILISTINGS V2703 V2707 V2707 V2704 V2708 V2708 Orifice Size (inches) 1/2° 1/2' 1/2" 1/2" 1/2 ' 1/2 Orifice Size (mm) 13 13 13 13 13 13 Nom.na.KFactorlmperia......5.6 5.6 ... ...5.6 ... Nominal K Factor S.1.5 8.1 8.1 8.1 8.1 8.1 8.1 Re2_ Standard i Standard Standard Quick Quick Quick Deflector Type Upright Pendent Recessed Upright Pendent Recessed Pendent Pendent Approved Temperature Ratings F°/C° 135°F/57°C 135°F/57°C 135°F157°C 135°F/57°C 135°F 57°C 155'F/68'C 155'F/68'C 155:F/68:C 1550Ff680C 155°Ff68°C 135oF/57oC cULus 2 0°F • 175 Ff79 C 175 Ff79 C 175'F/79'C 20 °F ° 20'F/9 o286°F/141°C 200'F/93'C 7 0 7 286°F/141°C :4310CC 200°F/93°C 360°F/182°C 360°F/182 °C 135°Ff57°C 135°Ff57°C 135°F 7 /5°C 135° C Ff57 155°F/68°C 155°F/68°C 135°F/57°C 155 Ff68 C 155 Ff68 C 135°Ff57°C FM 175°F/79°C 175°F/79°C 155°F/68°C 175F 79 j 1757/79T 155°F/68°C 200°F/93°C 200°Ff93°C 175°F/79°C 175°Ff79°C 360*F/182oC 200°F/93°C 2007/93 200oF/93*C 200°Ff93°C 360'F/182'C 135°F/57°C 135°F/57°C 135°F/57°C 135°F/57°C 135°Ff57°C 155°F/68°C 155°Ff68°C 155°Ff68°C 155°F/68°C 135°Ff57°C NYC/MEA 62-99-E 1757/79oC 155°F/68°C175'F/79'C 175°F/79°C 175°F/79°C 175°Ff79°C 155'F/68'C 200°Ff93°C 200°F/93°C 175°F/79°C 286°F/141°C 286'F/ 141'C 200°F/93°C 360°F/182°C 360°Ff182°C 135°Ff57°C 135°F/57°C 135°F/57°C 135°F/57°C 135°F/57°C 155:F/68:C 155F/68°C 155°F/68°C 155°F/68°C 155°F/68°C 135:F/57:C CSFM 7690-0531:112 175 Ff79 C 175 Ff79 C 175°F/79°C 175°F/79°C 175°Ff79°C 155 Ff68 C 286°F/141°C 286°F/14C 200°F/93°C 360°F/182°C 360°F/182°C 135°Ff57°C 155°F/68°C 135°F/57°C LPCB 175°F/79°C None None 155°F/68°C None None 200°F/93°C 175°Ff79°C 286°Ff 141°C i200°F/93°C VN II PO 360°Ff 182°C 1357f57°C 155°F/68°C 175°F/79°C 135°F/57°C 155°Ff68°C 175°F/79°C 135°F/57°C 155°F/68°C 135'F/57'C 15 °F 68°C 175°F/79°C 1 °F 1°F° 175°F 79°C 135°Ff57°C 155°F/68°C 200°Ff93°C 286°F/141°C I 360°F/182°C .. ZSTZ 200°Ff93°C 286°Ff141°C 360°F/182°C ZSTX 175°Ff79°C 200°F/93°C 200°F" °C 1 286°F/141°C K-ZSTZ 200'F/93'C 2 86°Ff141°C K-ZSTZ 175°Ff79°C 200°F/93°C CCC 155°F/68°C 155°Ff68°C None 1557f68°C 155°F/68°C None 200°Ff93°C 200°F/93°C 200°Ff93°C 200°Ff93°C 135°Ff57°C 135°Ff57°C 1551F/681C 155°F/68°C .VdS .............175 Ff79 C None . None-. - 175°F/79°C . None None 286° Ff141 °C 286°F 3607/182°C - 135°F/57°C 135°F / 57°C 155°F/68°C 155 • CE 175°Ff79°C None None 175 Ff79 C None None °F 3°C 286°F/141°C 3607/182°C For K Factor when pressure is measured in Bar, multiply S.I. units by 10.0 FM Approved with /2" adjustment escutcheon only - quick response Note: Listings and Approvals as of printing. All are approved open. 40.10 2544 Rev. J Updated 07/2014 © 2014 Victaulic company. All rights reserved. victaulic,com 3 ___________ vctaulic.comI Sprinklers I FireLocke I K5.6, V27 I Publication 40.10 Dimensions: 2 60 1W! 2W/ 41 mm 60 mm 1516/ 37 mm Standard Pendent - Standard Upright - V2707, V2708 V2703, V2704 2W/hO mm Max. Hole 2"/51 mm Mix. Hole !IT _______________________________________________ 515"/ Typical CeihxgTile 1 1 30 mm 7mm lflx"/ Finished Surface 3Onm 43mm MAXIMUM RECESS 2516"! 75 mm MAXIMUM EXTENSION ½ Adjustment Recessed - V2707, V2708 (drawing not to scale) s'a]nu mm Max. Hole Min. Hole mM 1 Typical Ceiling Tile 24 \—Finished Isurface 24 mm MAXIMUM RECESS 75 mm MAXIMUM EXTENSION 34 Adjustment Recessed - V2707, V2708 (drawing not to scale) 40.10 2544 Rev. J Updated 07/2014 © 2014 Victaulic Company. All rights reserved. vctauIc.com 4 \j.tauIic" victaulic.com I Sprinklers I FireLock® I K5.6, V27 I Publication 40.10 Distribution Patterns: Models V2707, V2708 7 psi 48 kPa 15 psi 103 kPa 30 psi 207 kPa 7 psi 48 kPa ts psi 103 kPa 30 psi 207 kPa '4 NOTES: Data shown is approximate and can vary due to differences in installation. These graphs illustrate approximate trajectories, floor-wetting, and wall-wetting patterns for these specific Victaulic FireLock Automatic Sprinklers. They are provided as information for guidance in avoiding obstructions to sprinklers and should not be used as minimum sprinkler spacing rules for installation. Referto the appropriate NFPA National Fire Code or the Authority Having Jurisdiction for specific information regarding obstructions, spacing limitations and area of coverage requirements. Failure to follow these guidelines could adversely affect the performance of the Sprinkler and will void all Listings, Approvals and Warranties. All patterns are symmetrical to the centerline of the waterway. 40.10 2544 Rev. J Updated 07/2014 © 2014 Victaulic company. All rights reserved. victauic.com 5 -Ill. /(CtauIi Available Wrenches: victaulic.comI Sprinklers I FireLock® I K5.6, V27 I Publication 40.10 Ratings: All glass bulbs are rated for temperatures from -67°F (-55°C) to those shown in the table below. Temperature - nFIoC Maximum Sprinkler Victaulic Nominal Ambient Glass Temperature Part Temperature Temperature Bulb Classification Identification Rating Allowed Color Ordinary A 135°F/57°C 1000F/38°C Orange Ordinary C 155°F/680C 1001F/38°C Red Intermediate E 175°F/790C 150°F/650C Yellow Intermediate F 200°F/93°C 150°F/65°C Green High J 2860F/1410C 225°F°I107°C Blue Extra High 7 i K 360°F/182°C I 300°F/149°C I Purple - M Open - No Bulb Standard response only. 8 150/65 if wax coated. WARNING Always read and understand installation, care, and maintenance instructions, supplied with each box of sprin- klers, before proceeding with installation of any sprinklers. Always wear safety glasses and foot protection. Depressurize and drain the piping system before attempting to install, remove, or adjust any Victaulic piping products. Installation rules, especially those governing obstruction, must be strictly followed. Painting, plating, or any re-coating of sprinklers (other than that supplied by Victaulic) is not allowed. O Failure to follow these instructions could result in serious personal injury and/or property damage. The owner is responsible for maintaining the fire protection system and devices in proper operating condition. For minimum maintenance and inspection requirements, refer to the current National Fire Protection Association pam- phlet that describes care and maintenance of sprinkler systems. In addition, the authority having jurisdiction may have additional maintenance, testing, and inspection requirements that must be followed. If you need additional copies of this publication, or if you have any questions about the safe installation of this 10 product, contact Victaulic World Headquarters: P.O. Box 31, Easton, Pennsylvania 1804470031 USA, Telephone: 001-610-559-3300. . . .- -. - .. ... IN I Installation Reference should always be made to the 1-40 Victaulic FireLock Automatic Sprinklers Installation and Maintenance Sheet for the product you are installing. This installation sheet is included with each shipment of Victaulic products for complete installation and assembly data, and is available in POF format on our website at victaulic.com. Warranty Refer to the Warranty section of the current Price List or contact Victaulic for details, Note This product shall be manufactured by Victaulic or 'to Victaulic specifications. All products to be installed in accordance with current Victaulic installation/assembly instructions. Victaulic reserves the right to change product specifications, designs and standard equipment without notice and without incurring obligations. Trademarks Victaulic is a registered trademark of Victaulic Company. 40.10 2544 Rev. J Updated 07/2014 © 2014 Victaulic Company. All rights reserved. victau.rc.com 6 X/C_t814_hCf