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HomeMy WebLinkAbout6172 COLT PL; ; FPR2018-0210; Permit(City of Carlsbad Print Date: 04/20/2022 Job Address: 6172 COLT PL, CARLSBAD, CA 92009-1728 Permit Type: FIRE-Construction Residential Work Class: Parcel #: 2132621820 Track #: Valuation: $0.00 Lot #: Occupancy Group: Project #: #of Dwelling Units: Plan #: Bedrooms: Construction Type: Bathrooms: Orig. Plan Check #: Plan Check #: Permit No: FPR2018-0210 Status: Closed - Finaled Multifamily Fire Sprinkler Applied: 11/13/2018 Issued: 02/21/2019 Finaled Close Out: 12/01/2020 Inspector: Final Inspection: Project Title: Description: KENSINGTON AT THE SQUARE BLDG 4-NEW SPRINKLER SYSTEM REVISED PLANS Applicant: RESIDENTIAL FIRE SYSTEMS INC RUBI GUTIERREZ 8085 E CRYSTAL DR ANAHEIM, CA 92807-2523 (714) 666-8450 FPContractor: RESIDENTIAL FIRE SYSTEMS INC-INACTIVE 8085 E. CRYSTAL DR ANAHEIM, CA 92807 (714) 666-8450 FEE AMOUNT FIRE NFPA 13 System > 100 heads (includes 1 riser) $858.00 FIRE Plan Resub (3rd&Subsequent Submittal/hr) $136.00 Total Fees: $994.00 Total Payments To Date: $994.00 Balance Due: $0.00 Fire Department Page 1 of 1 1635 Faraday Avenue, Carlsbad CA 92008-7314 1 760-602-4665 760-602-8561 f I www.carlsbadca.gov KENSINGTON AT THE SQUARE Rvvm @) 0 BLDG PLAN TYPE # STREET # STREET NAME BLDG PERMIT # FIRE PERMIT # 4 4B 6172 COLT PLACE FPR2018-0210 5 4A 6140 COLT PLACE FPR2018-0211 6 5A 6124 COLT PLACE FPR2018-0212 11 5A 6100 COLT PLACE FPR2018-0213 14 513 6002 COLT PLACE PC2017-0029 FPR2019-0006 15 6B 6018 COLT PLACE PC2018-0052 FPR2019-0007 16 6A 6026 COLT PLACE PC2018-0053 FPR2019-0008 17 hA 6034 COLT PLACE PC2018-0054 FPR2019-0009 18 5A 6010 COLT PLACE FPR2019-0010 19 hA 6042 COLT PLACE PC2018-0055 FPR2019-0011 20 4B 6082 COLT PLACE FPR2019-0012 21 4B 6050 COLT PLACE PC2018-0056 FPR2019-0013 22 5A 6074 COLT PLACE FPR2019-0014 23 6B 6058 COLT PLACE PC2018-0057 FPR2019-0015 1 5B 6156 COLT PLACE FPR2019-0016 2 5A 6164 COLT PLACE FPR2019-0017 3 6A 6180 COLT PLACE FPR2019-0018 7 6B 6108 COLT PLACE FPR2019-0019 8 4B 6148 COLT PLACE FPR2019-0020 9 4A 6132 COLT PLACE FPR2019-0021 10 SB 6116 COLT PLACE FPR2019-0022 12 SB 6066 COLT PLACE FPR2019-0023 13 4A 6090 COLT PLACE FPR2019-0024 RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 6-PLEX GARAGE 4HD CALC FILE NUMBER: 12063 DATE: OCT 11, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, ORDINARY HAZARD DENSITY: 0.15 gpm/sq. ft. AREA OF APPLICATION: 520.0 sq. ft. COVERAGE PER SPRINKLER: 130.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 83.2 gpm TOTAL WATER REQUIRED (including hose) : 183.2 gpm FLOW AND PRESSURE (8 BOR) : 83.2 gpm 8 25.3 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION.: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 1t 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/11/2018IRE SPRINKLERS\CALCS\INITIAL6-PLEX-4HD CALC (GARAGE) .SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQD NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM (PSI i (GPM) (PSI) SR 51.7 39.0 6000.0 183.2 35.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 183.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 83.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI (GPM) 1 32.0 - - - - 10.6 - - - 2 30.0 - - - - 11.5 - - - 3 30.0 - - - - 11.5 - - - 4 30.0 - - - - 11.5 - - - 5 30.0 - - - - 11.5 - - - 6 30.0 - - - - 11.5 - - - 7 32.0 - - - - 10.6 - - - 8 30.0 - - - - 11.5 - - - 9 30.0 - - - - 11.5 - - - 10 30.0 - - - - 11.5 - - - 11 30.0 - - - 11.5 - - - 12 30.0 - - - - 11.' - - - 13 30.0 - - - - 11.7 - - - 14 30.0 - - - - 11.5 - - - 15 32.0 - - - - 10.6 - - - 16 30.0 - - - - 11.5 - - - 17 32.0 - - - - 10.6 - - - 18 30.0 - - - - 11.4 - - - 19 32.0 - - - - 10.6 - - - 20 30.0 - - - - 11.4 - - - 21 30.0 - - - - 11.4 - - 22 20.0 - - - 16.2 - - 23 20.0 - - - - 16.3 - - - 24 20.0 - - - - 16.3 - - - 25 10.0 - - - 20.7 - - - 26 10.0 - - - - 20.9 - - - 27 10.0 - - - - 20.7 28 10.0 - - - - 20.3 - - - 29 10.0 - - - - 19.9 - - - 30 10.0 - - - - 19.7 - - - 31 10.0 - - - - 19.7 - - - 32 10.0 - - - - 16.6 - - - 33 10.0 K= 5.60 13.4 20.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 0/11/2018IRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (GARAGE) .SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (ET) (PSI) (GPM) 34 10.0 K= 5.60 12.1 19.5 35 10.0 - - - - 19.6 - - - 36 10.0 - - - - 19.6 - - - 37 10.0 - - - - 16.1 - - - 38 10.0 K= 5.60 15.1 21.8 39 10.0 K= 5.60 14.6 21.4 40 10.0 - - - - 19.8 - - - 41 20.0 - - - - 15.5 - - - 42 20.0 - - - - 15.6 - - - 43 20.0 - - - - 15.6 - - - TR 10.0 - - - - 21.0 - - - ES 5.0 - - - - 23.5 - - - BR 1.0 - - - - 25.3 - - - Ui -3.0 - - - - 27.2 - - - U2 -4.0 - - - - 27.9 - - - U3 2.0 - - - - 25.3 - - - U4 2.0 - - - - 32.3 - - - U5 -4.0 - - - - 35.0 - - - SR -4.0 SOURCE 35.1 83.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/11/20181RE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (GARAGE) .SJE JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUN. NODES (FT) (K) (PSI) (GPM) FL/FT ' (PSI) Pipe: 1 0.0 1.101 PL 3.08 PF 0.0 1 32.0 0.0 10.6 0.0 0.0 150 FTG E FE 0.9 2 30.0 0.0 11.5 0.0 0.000 TL 10.08 PV Pipe: 2 -9.8 1.598 PL 4.66 PF 0.0 2 30.0 0.0 11.5 0.0 1.6 150 FTG ---- FE 0.0 3 30.0 0.0 11.5 0.0 0.003 TL 4.66 PV Pipe: 3 0.0 1.101 PL 2.50 PF 0.0 3 30.0 0.0 11.5 0.0 0.0 150 FTG 2T PE 0.0 4 30.0 0.0 11.5 0.0 0.000 TL 12.50 PV Pipe: 4 0.0 1.101 FL 9.00 PF 0.0 4 30.0 0.0 11.5 0.0 0.0 150 FTG E PE 0.0 5 30.0 0.0 11.5 0.0 0.000 TL 16.00 PV Pipe: 5 -9.8 1.598 PL 5.00 PF 0.0 3 30.0 0.0 11.5 0.0 1.6 150 FTG ---- PE 0.0 6 30.0 0.0 11.5 0.0 0.003 TL 5.00 PV Pipe: 7 0.0 1.101 PL 3.08 PF 0.0 6 30.0 0.0 11.5 0.0 0.0 150 FTG ET PE -0.9 7 32.0 0.0 10.6 0.0 0.000 TL 15.08 PV Pipe: 8 -9.8 1.598 FL 3.50 PF 0.0 6 30.0 0.0 11.5 0.0 1.6 150 FTG ---- FE 0.0 8 30.0 0.0 11.5 0.0 0.003 TL 3.50 PV Pipe: 9 0.0 1.101 PL 9.00 PF 0.0 8 30.0 0.0 11.5 0.0 0.0 150 FTG ET PE 0.0 9 30.0 0.0 11.5 0.0 0.000 TL 21.00 PV Pipe: 10 -9.8 1.598 PL 2.00 PF 0.0 8 30.0 0.0 11.5 0.0 1.6 150 FTG ---- PE 0.0 10 30.0 0.0 11.5 0.0 0.003 TL 2.00 PV Pipe: 11 0.0 1.101 FL 4.08 PP 0.0 10 30.0 0.0 11.5 0.0 0.0 150 FTG ET FE 0.0 11 30.0 0.0 11.5 0.0 0.000 TL .16.08 PV Pipe: 12 -9.8 1.598 FL 84.16 PP 0.2 10 30.0 0.0 11.5 0.0 1.6 150 FTC ---- FE 0.0 12 30.0 0.0 11.7 0.0 0.003 TL 84.16 PV Pipe: 13 1.4 1.598 FL 27.00 PF 0.0 12 30.0 0.0 11.7 0.0 0.2 150 FTC ---- PE 0.0 13 30.0 0.0 11.7 0.0 0.000 TL 27.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: '10/11/20181RE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (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: 14 9.8 1.598 PL 84.16 PF 0.3 13 30.0 0.0 11.7 0.0 1.6 150 FTG T PE 0.0 14 30.0 0.0 11.5 0.0 0.003 TL 92.16 PV Pipe: 15 0.0 1.101 PL 12.42 PF 0.0 14 30.0 0.0 11.5 0.0 0.0 150 FTG ET PH -0.9 15 32.0 0.0 10.6 0.0 0.000 TL 24.42 PV Pipe: 16 9.8 1.598 PL 7.00 PF 0.0 14 30.0 0.0 11.5 0.0 1.6 150 FTG ---- PE 0.0 16 30.0 0.0 11.5 0.0 0.003 TL 7.00 PV Pipe: 17 0.0 1.101 PL 15.00 PF 0.0 16 30.0 0.0 11.5 0.0 0.0 150 FTG 2ET PE -0.9 17 32.0 0.0 10.6 0.0 0.000 TL 34.00 PV Pipe: 18 9.8 1.598 PL 6.00 PF 0.0 16 30.0 0.0 11.5 0.0 1.6 150 FTG ---- PE 0.0 18 30.0 0.0 11.4 0.0 0.003 TL 6.00 PV Pipe: 19 0.0 1.101 PL 12.58 PF 0.0 18 30.0 0.0 11.4 0.0 0.0 150 FTG ET PE -0.9 19 32.0 0.0 10.6 0.0 0.000 TL 24.58 PV Pipe: 20 9.8 1.598 PL 21.33 PF 0.1 18 30.0 0.0 11.4 0.0 1.6 150 FTG ---- PE 0.0 20 30.0 0.0 11.4 0.0 0.003 TL 21.33 PV Pipe: 21 1.3 1.598 PL 27.00 PF 0.0 20 30.0 0.0 11.4 0.0 0.2 150 FTG T PE 0.0 21 30.0 0.0 11.4 0.0 0.000 TL 35.00 PV Pipe: 22 -9.8 1.598 PL 20.00 PF 0.1 21 30.0 0.0 11.4 0.0 1.6 150 FTG T PE 0.0 2 30.0 0.0 11.5 0.0 0.003 TL 28.00 PV Pipe: 23 11.1 1.598 PL 21.00 PF 0.1 21 30.0 0.0 11.4 0.0 1.8 150 FTG 2E PE 4.3 43 20.0 0.0 15.6 0.0 0.004 TL 39.00 PV Pipe: 24 11.1 1.598 PL 10.00 PF 0.1 43 20.0 0.0 15.6 0.0 1.8 150 FTG T PE 4.3 40 10.0 0.0 19.8 0.0 0.004 TL 18.00 PV Pipe: 25 11.1 1.598 PL 31.33 PF 0.2 40 10.0 0.0 19.8 0.0 1.8 150 FTG 2E PH 0.0 35 10.0 0.0 19.6 0.0 0.004 TL 49.33 PV Pipe: 26 -8.3 1.598 PL 22.33 PP 0.1 13 30.0 0.0 11.7 0.0 1.3 150 FTG 3E PE 4.3 22 20.0 0.0 16.2 0.0 0.002 TL 49.33 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/11/20181RE SPRINKLERS'CALCS\INITIAL\6-PLEX-4HD CALC (GARAGE) .SDP JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENG?H PRESS. END ELEV. NOZ. PT D:SC. VEL(FPS) HWOG) (F SUM. NODES (PT) (K) (PSI) (:SPM) FL/PT (PSI) Pipe: 27 -8.3 1.598 PL 36 00 ?F 0.1 22 20.0 0.0 16.2 0.0 1.3 150 FTG 2E ?E 0.0 23 20.0 0.0 16.3 0.0 0.002 TL 5.00 SV Pipe: 28 -8.3 1.598 PL 15.58 ?P 0.1 23 20.0 0.0 16.3 0.0 1.3 150 FTG 2ET SE 4.3 25 10.0 0.0 20.7 0.0 0.002 TL 41-58 PV Pipe: 29 -71.9 2.705 PL 8.75 PP 0.1 25 10.0 0.0 20.7 0.0 4.0 120 FTC ---- PE 0.0 26 10.0 0.0 20.9 0.0 0.014 TL 8.75 PV Pipe: 30 11.2 1.598 PL 31.33 PF 0.2 26 10.0 0.0 20.9 0.0 1.8 150 FTG ES PE 0.0 27 10.0 0.0 20.7 0.0 0.004 TL 48.33 PV Pipe: 31 11.2 1.598 PL 10.03 PP o.- 27 10.0 0.0 20.7 0.0 1.8 150 FTG H PE -4.3 24 20.0 0.0 16.3 0.0 0.004 TL 19.03 PV Pipe: 32 11.2 1.598 PL 23.0J PP 0.2 24 20.0 0.0 16.3 0.0 1.8 150 FTC 2ET PE -4.3 12 30.0 0.0 11.7 0.0 0.004 TL 4-,.OD PV Pipe: 33 63.6 2.705 PL 4.0J PP 0.5 25 10.0 0.0 20.7 0.0 3.6 120 FTG ---- PE 0.0 28 10.0 0.0 20.3 0.0 0.011 TL 43.03 PV Pipe: 34 63.6 2..705 PL 32.00 PF 0.4 28 10.0 0.0 20.3 0.0 3.6 120 FTG ---- PE 0.0 29 10.0 0.0 19,9 0.0 0.011 TL 32.00 PV Pipe: 35 63.6 2.705 PL 18.58 PP 0.2 29 10.0 0.0 19.9 0.0 3.6 120 FTG ---- PE 0.0 30 10.0 0.0 19.7 0.0 0.011 TL 18.58 PV Pipe: 36 -8.5 1.598 PL 15.58 PP 0.1 30 10.0 0.0 19.7 0.0 1.4 150 FTG 2ET PE -4.3 41 20.0 0.0 15.5 0.0 0.002 TL 41.58 PV Pipe: 37 -8.5 1.598 PL 36.00 PP 0.1 41 20.0 0.0 15.5 0.0 1.4 150 FTG 2E2R PE O.C. 42 20.0 0.0 15.6 0.0 0.002 TL 56.00 PV Pipe: 38 -8.5 1.598 PL 22.33 PP 0.1 42 20.0 0.0 15.6 0.0 1.4 150 FTG 3E2R PE -4. 20 30.0 0.0 11.4 0.0 0.002 TL 51.33 PV Pipe: 39 72.1 2.705 PL 3.08 PF 0.0 30 10.0 0.0 19.7 0.0 4.0 120 FTG ---- PH 0.0 31 10.0 0.0 19.7 0.0 0.014 TL 3.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 PATE: 10/11/2018IRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (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: 40 40.0 1.101 PL 7.33 PF 3.0 31 10.0 0.0 19.7 0.0 13.5 150 FTG T PE 0.0 32 10.0 0.0 16.6 0.0 0.246 TL 12.33 PV Pipe: 41 40.0 1.101 PL 1.00 PF 3.2 32 10.0 0.0 16.6 0.0 13.5 150 FTG ET PE 0.0 33 10.0 5.6 13.4 20.5 0.246 TL 13.00 PV Pipe: 42 19.5 1.101 PL 6.25 PF 1.3 33 10.0 5.6 13.4 20.5 6.6 150 FTG 2E PE 0.0 34 10.0 5.6 12.1 19.5 0.065 TL 20.25 PV Pipe: 43 32.1 2.705 PL 5.58 PF 0.0 31 10.0 0.0 19.7 0.0 1.8 120 FTG ---- PE 0.0 35 10.0 0.0 19.6 0.0 0.003 TL 5.58 PV Pipe: 44 43.1 2.705 PL 5.50 PF 0.0 35 10.0 0.0 19.6 0.0 2.4 120 FTG ---- PS 0.0 36 10.0 0.0 19.6 0.0 0.005 TL 5.50 PV Pipe: 45 43.1 1.101 PL 7.33 PF 3.5 36 10.0 0.0 19.6 0.0 14.5 150 FTG T PE 0.0 37 10.0 0.0 16.1 0.0 0.282 TL 12.33 PV Pipe: 46 21.8 1.101 PL 1.00 PF 1.0 37 10.0 0.0 16.1 0.0 7.3 150 FTG ST PE 0.0 38 10.0 5.6 15.1 21.8 0.080 TL 13.00 PV Pipe: 47 21.4 1.101 PL 6.25 PF 1.6 37 10.0 0.0 16.1 0.0 7.2 150 FTG 2E PE 0.0 39 10.0 5.6 14.6 21.4 0.077 TL 20.25 PV Pipe: 48 -83.2 2.705 PL 10.66 PF 0.2 26 10.0 0.0 20.9 0.0 4.6 120 FTG ---- PE 0.0 TR 10.0 0.0 21.0 0.0 0.018 TL 10.66 PV Pipe: 49 -83.2 2.705 PL 5.00 PF 0.3 TR 10.0 0.0 21.0 0.0 4.6 120 FTG S PE 2.2 FS 5.0 0.0 23.5 0.0 0.018 TL 14.36 PV Pipe: 50 -83.2 2.705 PL 4.00 PF 0.1 FS 5.0 0.0 23.5 0.0 4.6 120 FTG ---- PE 1.7 BR 1.0 0.0 25.3 0.0 0.018 TL 4.00 PV Pipe: 51 -83.2 2.705 PL 4.00 PF 0.2 BR 1.0 0.0 25.3 0.0 4.6 120 FTG E PE 1.7 Ui -3.0 0.0 27.2 0.0 0.018 TL 13.36 PV Pipe: 52 -83.2 4.240 PL 74.00 PF 0.2 Ui -3.0 0.0 27.2 0.0 1.9 150 FTG 4E PS 0.4 U2 -4.0 0.0 27.9 0.0 0.001 TL 154.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/11/20181RE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (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: 53 -83.2 4.220 PL €.00 PF 0.1 U2 -4.0 0.0 27.9 0.0 1.9 140 FTG 2E PE -2.6 U3 2.0 0.0 25.3 0.0 0.002 TL 4C.00 PV Pipe: 54 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 32.3 0.0 7.0 psi, 83.2 gpm U3 2.0 0.0 25.3 0.0 Pipe: 55 -83.2 4.220 PL 6,00 PF 0.1 U4 2.0 0.0 32.3 0.0 1.9 140 FTG 2E PE 2.6 U5 -4.0 0.0 35.0 0.0 0.002 TL 4C:.00 PV Pipe: 56 -83.2 4.220 PL 32.75 PF 0.1 US -4.0 0.0 35.0 0.0 1.9 140 FTG ET PE 0.0 SR -4.0 SRCE 35.1 (N/A) 0.002 TL 8:.75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.066 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.5 ft/sec at pipe 45. Items listed in bold print on the cover sheet are automatically transferred from the calculation repor. Available pressure at source node SR under full flow conditions is 51.67 psi with a flow of 210.87 gpm. PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: io/11/20181RE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (GARAGE) .SDF JOB TITLE: 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 Kpig ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 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 WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm G A U G E P R E S S U R E p S i 60.0 50.0 40.0 4 30.0 20.0 10.0 0.0 00 - FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 PATE: JO/11/20181RE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (GARAGE) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ 0\\\ 50+ \\\\ I \\\\ I \\\ 45+ I \\\\ I \\\\ P 40+ \\\ R I * <-39.0 psi 8 6000 gpm E I Flow Test Point S I S 35X U I R I E I 30+ P I S I I 25+ 20+ 15+ 10+ LEGEND 0 I X = Required Water Supply 35.14 psi 8 183.2 gpm 5+ I 0 = Available Water Supply I 51.68 psi 8 183.2 gpm +------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 5600 6400 7200 8000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 6-PLEX 4HD CALC AT UNIT 2 FILE NUMBER: 12063 DATE: OCT 11, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 1296.0 sq. ft. COVERAGE PER SPRINKLER: 324.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 71.3 gpm TOTAL WATER REQUIRED (including hose) : 171.4 gpm FLOW AND PRESSURE (@ BOR) : 71.4 gpm 8 31.3 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR 51.7 39.0 6000.0 51.7 171.4 41.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 171.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100..0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 71.4 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (ET) (PSI) (GPM) 1 32.0 - - - - 14.5 - - - 2 30.0 - - - - 15.4 - - - 3 30.0 - - - - 15.2 .- - - 4 30.0 K= 4.90 12.6 17.6 5 30.0 K= 4.90 12.0 17.0 6 30.0 - - - - 15.2 - - - 7 32.0 - - - - 14.3 - - - 8 30.0 - - - - 15.2 - - - 9 30.0 K= 4.90 14.3 18.3 10 30.0 - - - - 15.2 - - - 11 30.0 K= 4.90 14.2 18.5 12 30.0 - - - - 17.1 - - - 13 30.0 - - - - 17.2 - - - 14 30.0 - - - - 17. - - - 15 32.0 - - - - 16.2 - - - 16 30.0 - - - - 17.0 - - - 17 32.0 - - - - 16.2 - - - 18 30.0 - - - - 17.0 - - - 19 32.0 - - - - 16.2 - - - 20 30.0 - - - - 17.0 - - - 21 30.0 - - - - 16.6 - - - 22 20.0 - - - - 21.9 - - - 23 20.0 - - - - 22.3 - - - 24 20.0 - - - - 21.9 - - - 25 10.0 - - - - 26.9 - - - 26 10.0 - - - - 27.0 - - - 27 10.0 - - - - 26.5 - - - 28 10.0 - - - - 26.E - - - 29 10.0 - - - - 26.6 - - - 30 10.0 - - - - 26.6 - - - 31 10.0 - - - - 26.6 - - - 32 10.0 - - - - 26.6 - - - 33 10.0 - - - - 26.6 - - - 11 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .5DB' JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 10.0 - - - - 26.6 - - - 35 10.0 - - - - 26.6 - - - 36 10.0 - - - - 26.6 - - - 37 10.0 -- - - 26.6 - - - 38 10.0 - - - - 26.6 - - - 39 10.0 - - - - 26.6 - - - 40 10.0 - - - - 26.0 - - - 41 20.0 - - - - 22.0 - - - 42 20.0 - - - - 21.7 - - 43 20.0 - - - - 21.4 - - - TR 10.0 - - - - 27.1 - - - ES 5.0 - - - - 29.5 - - - ER 1.0 - - - - 31.3 - - - Ui -3.0 - - - - 33.2 - - - U2 -4.0 - - - - 33.8 - - - U3 2.0 - - - - 31.2 - - - U4 2.0 - - - - 38.2 - - - U5 -4.0 - - - - 40.9 - - - SR -4.0 SOURCE 41.0 71.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (Fl) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 0.0 1.101 PL 3.08 PF 0.0 1 32.0 0.0 14.5 0.0 0.0 150 FTG E PE 0.9 2 30.0 0.0 15.4 0.0 0.000 TL 13.08 PV Pipe: 2 41.8 1.598 PL 4.66 PF 0.2 2 30.0 0.0 15.4 0.0 6.7 150 FTG ---- PE 0.0 3 30.0 0.0 15.2 0.0 0.043 TL 4.66 PV Pipe: 3 34.6 1.101 PL 2.50 PP 2.3 3 30.0 0.0 15.2 0.0 11.6 150 FTG 2T PE 0.0 4 30.0 4.9 12.8 17.6 0.187 TL 12.50 PV Pipe: 4 17.0 1.101 PL 9.00 PF 0.8 4 30.0 4.9 12.8 17.6 5.7 150 FTG E PE 0.0 5 30.0 4.9 12.0 17.0 0.050 TL 16.00 PV Pipe: 5 7.2 1.598 PL 5.00 PP C.0 3 30.0 0.0 15.2 0.0 1.2 150 FTG ---- PE C.0 6 30.0 0.0 15.2 0.0 0.002 TL 5.00 PV Pipe: 7 0.0 1.101 PL 3.08 PF 0.0 6 30.0 0.0 15.2 0.0 0.0 150 FTG ET PE -0.9 7 32.0 0.0 14.3 0.0 0.000 TL 15.08 PV Pipe: 8 7.2 1.598 PL 3.50 PF 0.0 6 30.0 0.0 15.2 0.0 1.2 150 FTG ---- PE 0.0 8 30.0 0.0 15.2 0.0 0.002 TL 3.50 PV Pipe: 9 18.3 1.101 PL 9.00 PP 1.2 8 30.0 0.0 15.2 0.0 6.2 150 FTG ET PE 0.0 9 30.0 4.9 14.0 18.3 0.058 TL 21.00 PV Pipe: 10 -11.1 1.598 PL 2.00 PP 0.0 8 30.0 0.0 15.2 0.0 1.8 150 FTG ---- PE 0.0 10 30.0 0.0 15.2 0.0 0.004 TL 2.00 PV Pipe: 11 18.5 1.101 PL 4.08 PF 0.9 10 30.0 0.0 15.2 0.0 6.2 150 FTG ET PE 0.0 11 30.0 4.9 14.2 18.5 0.059 TL 16.08 PV Pipe: 12 -29.5 1.598 PL 84.16 PF 1.9 10 30.0 0.0 15.2 0.0 4.7 150 FTG ---- PE 3.0 12 30.0 0.0 17.1 0.0 0.023 TL 84.16 PV Pipe: 13 -9.9 1.598 PL 27.30 PF 0.1 12 30.0 0.0 17.1 0.0 1.6 150 FTG ---- PE 0.0 13 30.0 0.0 17.2 0.0 0.003 TL 27.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 1O/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOE TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 6.3 1.598 PL 84.16 PF 0.1 13 30.0 0.0 17.2 0.0 1.0 150 FTG T PE 0.0 14 30.0 0.0 17.1 0.0 0.001 TL 92.16 PV Pipe: 15 0.0 1.101 PL 12.42 PF 0.0 14 30.0 0.0 17.1 0.0 0.0 150 FTG ST PE -0.9 15 32.0 0.0 16.2 0.0 0.000 TL 24.42 PV Pipe: 16 6.3 1.598 PL 7.00 PP 0.0 14 30.0 0.0 17.1 0.0 1.0 150 FTG ---- PE 0.0 16 30.0 0.0 17.0 0.0 0.001 TL 7.00 PV Pipe: 17 0.0 1.101 PL 15.00 PP 0.0 16 30.0 0.0 17.0 0.0 0.0 150 FTG 2ET PS -0.9 17 32.0 0.0 16.2 0.0 0.000 TL 34.00 PV Pipe: 18 6.3 1.598 PL 6.00 PP 0.0 16 30.0 0.0 17.0 0.0 1.0 150 FTG ---- PS 0.0 18 30.0 0.0 17.0 0.0 0.001 TL 6.00 PV Pipe: 19 0.0 1.101 PL 12.58 PP 0.0 18 30.0 0.0 17.0 0.0 0.0 150 FTG ET PE -0.9 19 32.0 0.0 16.2 0.0 0.000 TL 24.58 PV Pipe: 20 6.3 1.598 PL 21.33 PP 0.0 18 30.0 0.0 17.0 0.0 1.0 150 FTG ---- PS 0.0 20 30.0 0.0 17.0 0.0 0.001 TL 21.33 PV Pipe: 21 20.7 1.598 PL 27.00 PP 0.4 20 30.0 0.0 17.0 0.0 3.3 150 FTG T PE 0.0 21 30.0 0.0 16.6 0.0 0.012 TL 35.00 PV Pipe: 22 41.8 1.598 PL 20.00 PP 1.2 21 30.0 0.0 16.6 0.0 6.7 150 FTG T PE 0.0 2 30.0 0.0 15.4 0.0 0.043 TL 28.00 PV Pipe: 23 -21.1 1.598 PL 21.00 PP 0.5 21 30.0 0.0 16.6 0.0 3.4 150 FTG 2E PE 4.3 43 20.0 0.0 21.4 0.0 0.012 TL 39.00 PV Pipe: 24 -21.1 1.598 PL 10.00 PP 0.2 43 20.0 0.0 21.4 0.0 3.4 150 FTC T PS 4.3 40 10.0 0.0 26.0 0.0 0.012 TL 18.00 PV Pipe: 25 -21.1 1.598 PL 31.33 PP 0.6 40 10.0 0.0 26.0 0.0 3.4 150 FTG 2E PE 0.0 35 10.0 0.0 26.6 0.0 0.012 TL 49.33 PV Pipe: 26 -16.2 1.598 PL 22.33 PF 0.4 13 30.0 0.0 17.2 0.0 2.6 150 FTG 3E PE 4.3 22 20.0 0.0 21.9 0.0 0.007 TL 49.33 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT SUMP- NODES (FT) (K) (PSI) (GPM) FL/FT (PSI; Pipe: 27 -16.2 1.598 PL 36.00 PF 0.4 22 20.0 0.0 21.9 0.0 2.6 150 FTG 2E PE 0.0 23 20.0 0.0 22.3 0.0 0.007 TL 54.00 PV Pipe: 28 -16.2 1.598 PL 15.58 PF 0.3 23 20.0 0.0 22.3 0.0 2.6 150 FTG 2ET PE 4.3 25 10.0 0.0 26.9 0.0 0.007 TL 4158 PV Pipe: 29 -51.7 2.705 PL 8.75 PF 0. 25 10.0 0.0 26.9 0.0 2.9 120 FTG ---- PE 0.0 26 10.0 0.0 27.0 0.0 0.007 TL 8.75 PV Pipe: 30 19.7 1.598 PL 31.33 PF 0.5 26 10.0 0.0 27.0 0.0 3.1 150 FTG ET PE 0.0 27 10.0 0.0 26.5 0.0 0.011 TL 48.33 PV Pipe: 31 19.7 1.598 PL 10.00 PP 0.2 27 10.0 0.0 26.5 0.0 3.1 . 150 FTG E PE -4.3 24 20.0 0.0 21.9 0.0 0.011 TL 19.00 PV Pipe: 32 19.7 1.598 PL 21.00 PF 0.5 24 20.0 0.0 21.9 0.0 3.1 150 FTG 2ET PE -4.3 12 30.0 0.0 17.1 0.0 0.011 TL 47.00 PV Pipe: 33 35.5 2.705 PL 43.00 SF 0.2 25 10.0 0.0 26.9 0.0 2.0 120 FTG ---- PE 0.0 28 10.0 0.0 26.8 0.0 0.004 TL 43.00 PV Pipe: 34 35.5 2.705 PL 32.00 PP 0. 28 10.0 0.0 26.8 0.0 2.0 120 FTG ---- PE 0.0 29 10.0 0.0 26.6 0.0 0.004 TL 32.00 PV - Pipe: 35 35.5 2.705 PL 1E58 PF 0.: 29 10.0 0.0 26.6 0.0 2.0 120 FTG ---- PE 0.0 30 10.0 0.0 26.6 0.0 0.004 TL 16.58 PV Pipe: 36 14.4 1.598 PL 15.58 PP 0.3 30 10.0 0.0 26.6 0.0 2.3 150 FTG 2ET PE -4.3 41 20.0 0.0 22.0 0.0 0.006 TL 41.58 PV Pipe: 37 14.4 1.598 PL 36.00 PF 0.3 41 20.0 0.0 22.0 0.0 2.3 150 FTG 2E2R PE 0.0 42 20.0 0.0 21.7 0.0 0.006 TL 56.00 PV Pipe: 38 14.4 1.598 PL 22.33 PF 0.3 42 20.0 0.0 21.7 0.0 2.3 150 FTG 3E2R PE -4.3 20 30.0 0.0 17.0 0.0 0.006 TL 51.33 PV Pipe: 39 21.1 2.705 PL 3.08 PF 0.0 30 10.0 0.0 26.6 0.0 1.2 120 FTG ---- PE 0.0 31 10.0 0.0 26.6 0.0 0.001 TL 3.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .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: 40 0.0 1.101 PL 7.33 PF 0.0 31 10.0 0.0 26.6 0.0 0.0 150 FTG T PH 0.0 32 10.0 0.0 26.6 0.0 0.000 TL 12.33 PV Pipe: 41 0.0 1.101 PL 1.00 PF 0.0 32 10.0 0.0 26.6 0.0 0.0 150 FTG ET PH 0.0 33 10.0 0.0 26.6 0.0 0.000 TL 13.00 PV Pipe: 42 0.0 1.101 PL 6.25 PF 0.0 33 10.0 0.0 26.6 0.0 0.0 150 FTG 2E PH 0.0 34 10.0 0.0 26.6 0.0 0.000 TL 20.25 PV Pipe: 43 21.1 2.705 PL 5.58 PF 0.0 31 10.0 0.0 26.6 0.0 1.2 120 FTG ---- PE 0.0 35 10.0 0.0 26.6 0.0 0.001 TL 5.58 PV Pipe: 44 0.0 2.705 PL 5.50 PH 0.0 35 10.0 0.0 26.6 0.0 0.0 120 FTG ---- PE 0.0 36 10.0 0.0 26.6 0.0 0.000 TL 5.50 PV Pipe: 45 0.0 1.101 PL 7.33 PH 0.0 36 10.0 0.0 26.6 0.0 0.0 150 FTG T PE 0.0 37 10.0 0.0 26.6 0.0 0.000 TL 12.33 PV Pipe: 46 0.0 1.101 PL 1.00 PH 0.0 37 10.0 0.0 26.6 0.0 0.0 150 FTG ET PH 0.0 38 10.0 0.0 26.6 0.0 0.000 TL 13.00 PV Pipe: 47 0.0 1.101 PL 6.25 PH 0.0 37 10.0 0.0 26.6 0.0 0.0 150 FTG 2E PH 0.0 39 10.0 0.0 26.6 0.0 0.000 TL 20.25 PV Pipe: 48 -71.3 2.705 PL 10.66 PH 0.1 26 10.0 0.0 27.0 0.0 4.0 120 FTG ---- PH 0.0 TR 10.0 0.0 27.1 0.0 0.014 TL 10.66 PV Pipe: 49 -71.3 2.705 PL 5.00 PF 0.2 TR 10.0 0.0 27.1 0.0 4.0 120 FTG E PE 2.2 FS 5.0 0.0 29.5 0.0 0.014 TL 14.36 PV Pipe: 50 -71.3 2.705 PL 4.00 PH 0.1 FS 5.0 0.0 29.5 0.0 4.0 120 FTG ------ PE 1.7 BR 1.0 0.0 31.3 0.0 0.014 TL 4.00 PV Pipe: 51 -71.3 2.705 PL 4.00 PF 0.2 BR 1.0 0.0 31.3 0.0 4.0 120 FTG H PH 1.7 Ui -3.0 0.0 33.2 0.0 0.014 TL 13.36 PV Pipe: 52 -71.3 4.240 PL 74.00 PH 0.2 Ui -3.0 0.0 33.2 0.0 1.6 150 FTG 4E PE 0.4 U2 -4.0 0.0 33.8 0.0 0.001 TL 154.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM -FF. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 -71.3 4.220 PL 6.00 PF 0.0 U2 -4.0 0.0 33.8 0.0 1.6 140 FTG 2E PE -2.6 U3 2.0 0.0 31.2 0.0 0.001 TL 40.00 PV Pipe: 54 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 38.2 0.0 7.0 psi, 71.3 gpm U3 2.0 0.0 31.2 0.0 Pipe: 55 -71.3 4.220 PL 6.00 PF 0.0 U4 2.0 0.0 38.2 0.0 1.6 140 FTG 2E PE 2.6 U5 -4.0 0.0 40.9 0.0 0.001 TL 40.00 PV Pipe: 56 -71.4 4.220 PL 32.75 PF 0.1 US -4.0 0.0 40.9 0.0 1.6 140 FTG ET PE 0.0 SR. -4.0 SRCE 41.0 (N/A) 0.001 TL 83.75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.123 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 11.6 ft/sec at pipe 3. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.68 psi with a flow of 189.46 gpm. PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 1O/11/2018D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOB TITLE: PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B C 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: 5 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 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 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 DPV1v NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 60.0 50.0 G A U G 40.0 E 30.0 20.0 0.0 -14.7 P R E S S U R E WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 .DATE: 10/11/20l8D\FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (RES) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ O\\\ 50+ \\\\ \\\\ \\\ 45+ I \\\\ x \\\\ P 40+ \\\ R I * <-39.0 psi 8 6000 gpm E Flow Test Point S I 5 35+ U I R I E I 30+ P I S I 25+ 20+ 15+ 10+ LEGEND I X = Required Water Supply I 40.98 psi @ 171.4 gpm 5+ I 0 = Available Water Supply 51.68 psi 8 171.4 gpm 0++-+---+----+-----+------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 5600 6400 7200 8000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 6-PLEX ATTIC AP HEADS FILE NUMBER: 12063 DATE: OCT 11, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 400.0 sq. ft. COVERAGE PER SPRINKLER: 160.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 5 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 103.7 gpm TOTAL WATER REQUIRED (including hose) : 203.7 gpm FLOW AND PRESSURE (8 BOR) : 103.7 gpm @ 33.3 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY BASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/11/2018FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: WATER SUPPLY DATA T/1 SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR 51.7 39.0 6000.0 51.7 203.7 43.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 203.7 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 103.7 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 32.0 K= 5.60 14.8 21.5 2 30.0 - - - - 16.4 - - - 3 30.0 - - - - 16.4 - - - 4 30.0 - - - - 16.4 - - - 5 30.0 - - - - 16.4 - - - 6 30.0 - - - - 16.4 - - - 7 32.0 K= 5.60 14.4 21.2 8 30.0 - - - - 16.5 - - - 9 30.0 - - - - 16.5 - - - 10 30.0 - - - - 16.5 - - - 11 30.0 - - - - 16.5 - - - 12 30.0 - - - - 17.7 - - - 13 30.0 - - - - 17.7 - - - 14 30.0 - - - - 15.9 - - - 15 32.0 K= 5.60 13.3 20.5 16 30.0 - - - - 15.9 - - - 17 32.0 K= 5.60 12.8 200 18 30.0 - - - - 16.0 - - - 19 32.0 K= 5.60 13.4 20.5 20 30.0 - - - - 16.6 - - - 21 30.0 - - - - 16.7 - - - 22 20.0 - - - - 22.7 - - - 23 20.0 - - - - 23.5 - - - 24 20.0 - - - - 23.0 - - - 25 10.0 - - - - 28.5 - - - 26 10.0 - - - 28.6 - - - 27 10.0 - - - - 27.7 - - - 28 10.0 - - - - 28.1 - - - 29 10.0 - - - - 27.9 - - 30 10.0 - - - - 27.7 - - - 31 10.0 - - - - 27.7 - - - 32 10.0 - - - - 27.7 - - - 33 10.0 - - - - 27.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE:' 10/11/2018F1R5 SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 10.0 - - - - 27.7 - - - 35 10.0 - - - - 27.7 - - - 36 10.0 - - - - 27.7 - - - 37 10.0 - - - - 27.7 - - - 38 10.0 - - - - 27.7 - - - 39 10.0 - - - - 27.7 - - - 40 10.0 - - - - 26.6 - - - 41 20.0 - - - - 22.7 - - - 42 20.0 - - - - 21.8 - - - 43 20.0 - - - - 21.9 - - - TR 10.0 - - - - 28.9 - - - FS 5.0 - - - - 31.4 - - - ER 1.0 - - - - 33.3 - - - Ui -3.0 - - - - 35.4 - - - U2 -4.0 - - - - 36.1 - - - U3 2.0 - - - - 33.6 - - - U4 2.0 - - - - 40.6 - - - U5 -4.0 - - - - 43.3 - - - SR -4.0 SOURCE 43.5 103.7 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/11/2018F1RE SPRINKLERS\CALCS\INITThL\6-PLEX-4HD CALC (ATTIC .SDF JOB TITLE: PIPE DATA I 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 -21.5 1.101 PL 3.08 ?F 0.8 1 32.0 5.6 14.8 21.5 7.2 150 FTG E FE 0.9 2 30.0 0.0 16.4 0.0 0.078 TL 10.08 PV Pipe: 2 -2.0 1.598 PL 4.66 PF 0.0 2 30.0 0.0 16.4 0.0 0.3 150 FTC ---- PE 0.0 3 30.0 0.0 16.4 0.0 0.000 TL 4.66 PV Pipe: 3 0.0 1.101 PL 2.50 PF 0.0 3 30.0 0.0 16.4 0.0 0.0 150 FTG 2T PE 0.0 4 30.0 0.0 16.4 0.0 0.000 TL 12.50 PV Pipe: 4 0.0 1.101 PL 9.00 PF 0.0 4 30.0 0.0 16.4 0.0 0.0 150 FTG E PE 0.0 5 30.0 0.0 16.4 0.0 0.000 TL 16.00 PV Pipe: 5 -2.0 1.598 FL 5.00 FE 0.0 3 30.0 0.0 16.4 0.0 0.3 150 FTG ---- FE 0.0 6 30.0 0.0 16.4 0.0 0.000 TL 5.00 PV Pipe: 7 21.2 1.101 PL 3.08 PF 1.1 6 30.0 0.0 16.4 0.0 7.2 150 FTG ET FE -0.9 7 32.0 5.6 14.4 21.2 0.076 TL 15.08 PV Pipe: 8 -23.3 1.598 PL 3.50 FF 0.1 6 30.0 0.0 16.4 0.0 3.7 150 FTG ---- FE 0.0 8 30.0 0.0 16.5 0.0 0.015 TL 3.50 EV Pipe: 9 0.0 1.101 FL 9.00 FF 0.0 8 30.0 0.0 16.5 0.0 0.0 150 FTG ET FE 0.0 9 30.0 0.0 16.5 0.0 0.000 TL 21.00 PV Pipe: 10 -23.3 1.598 PL 2.00 FE 0.0 8 30.0 0.0 16.5 0.0 3.7 150 FTG ---- FE 0.0 10 30.0 0.0 16.5 0.0 0.015 TL 2.00 PV Pipe: 11 0.0 1.101 PL 4.08 PF 0.3 10 30.0 0.0 16.5 0.0 0.0 150 FTG ET FE 0.3 11 30.0 0.0 16.5 0.0 0.000 TL 16.08 PV Pipe: 12 -23.3 1.598 PL 84.16 FF 1.2 10 30.0 0.0 16.5 0.0 3.7 150 FTG ---- PE 0.3 12 30.0 0.0 17.7 0.0 0.015 TL 84.16 PV Pipe: 13 3.8 1.598 PL 27.00 PF 0.0 12 30.0 0.0 17.7 0.0 0.6 150 FTG ---- P 0.0 13 30.0 0.0 17.7 0.0 0.001 TL 27.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/11/2O18PIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDP JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 26.8 1.598 PL 84.16 PP 1.8 13 30.0 0.0 17.7 0.0 4.3 150 FTC T PE 0.0 14 30.0 0.0 15.9 0.0 0.019 TL 92.16 PV Pipe: 15 20.5 1.101 PL 12.42 PP 1.7 14 30.0 0.0 15.9 0.0 6.9 150 FTG ET PE -0.9 15 32.0 5.6 13.3 20.5 0.071 TL 24.42 PV Pipe: 16 6.4 1.598 PL 7.00 PP 0.0 14 30.0 0.0 15.9 0.0 1.0 150 FTG ---- PE 0.0 16 30.0 0.0 15.9 0.0 0.001 TL 7.00 PV Pipe: 17 20.0 1.101 PL 15.00 PP 2.3 16 30.0 0.0 15.9 0.0 6.7 150 FTG 2ET PE -0.9 17 32.0 5.6 12.8 20.0 0.068 TL 34.00 PV Pipe: 18 -13.6 1.598 PL 6.00 PP 0.0 16 30.0 0.0 15.9 0.0 2.2 150 FTG ---- PE 0.0 18 30.0 0.0 16.0 0.0 0.005 TL 6.00 PV Pipe: 19 20.5 1.101 PL 12.58 PP 1.7 18 30.0 0.0 16.0 0.0 6.9 150 FTG ET PE -0.9 19 32.0 5.6 13.4 20.5 0.071 TL 24.58 PV Pipe: 20 -34.1 1.598 PL 21.33 PP 0.6 18 30.0 0.0 16.0 0.0 5.5 150 FTG ---- PE 0.0 20 30.0 0.0 16.6 0.0 0.030 TL 21.33 PV Pipe: 21 -9.4 1.598 PL 27.00 PP 0.1 20 30.0 0.0 16.6 0.0 1.5 150 FTG T PE 0.0 21 30.0 0.0 16.7 0.0 0.003 TL 35.00 PV Pipe: 22 19.5 1.598 PL 20.00 PP 0.3 21 30.0 0.0 16.7 0.0 3.1 150 FTG T PE 0.0 2 30.0 0.0 16.4 0.0 0.011 TL 28.00 PV Pipe: 23 -28.9 1.598 PL 21.00 PP 0.9 21 30.0 0.0 16.7 0.0 4.6 150 FTG 2E PE 4.3 43 20.0 0.0 21.9 0.0 0.022 TL 39.00 PV Pipe: 24 -28.9 1.598 PL 10.00 PP 0.4 43 20.0 0.0 21.9 0.0 4.6 150 FTG T PE 4.3 40 10.0 0.0 26.6 0.0 0.022 TL 18.00 PV Pipe: 25 -28.9 1.598 PL 31.33 PP 1.1 40 10.0 0.0 26.6 0.0 4.6 150 FTG 2E PE 0.0 35 10.0 0.0 27.7 0.0 0.022 TL 49.33 PV Pipe: 26 -23.1 1.598 PL 22.33 PP 0.7 13 30.0 0.0 17.7 0.0 3.7 150 FTG 3E PE 4.3 22 20.0 0.0 22.7 0.0 0.014 TL 49.33 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/11/2018FIRE SPRINKLERS\CALCS\INITIA1\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) -IW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI Pipe: 27 -23.1 1.98 PL 36.00 PP 0.8 22 20.0 0.0 22.7 0.0 3.7 150 FTG 2E PE 0.0 23 20.0 0.0 23.5 0.0 J.J14 TL 54.00 PV Pipe: 28 -23.1 1.598 PL 15.58 PP :0.6 23 20.0 0.0 23.5 0.0 3.7 150 FTG 2ET PE 4.3 25 10.0 0.0 28.5 0.0 0.014 TL 41.58 PV Pipe: 29 -76.6 2.705 PL 8.75 PP 0.1 25 10.0 0.0 28.5 0.0 4.3 120 FTC ---- PE 10.0 26 10.0 0.0 28.6 0.0 LOiS TL 8.75 PV Pipe: 30 27.0 1.598 PL 31.33 PP 0.9 26 10.0 0.0 28.6 0.0 4.3 150 FTG ET PE 0.0 27 10.0 0.0 27.7 0.0 3.319 TL 48.33 PV Pipe: 31 27.0 1.598 PL 10.00 PP 0.4 27 10.0 0.0 27.7 0.0 4.3 150 FTG E PE -4.3 24 20.0 0.0 23.0 0.0 3.319 TL 19.00 PV Pipe: 32 27.0 1.598 PL 21.00 PP 0.9 24 20.0 0.0 23.0 0.0 4.3 150 FTG 2ET PE -4.3 12 30.0 0.0 17.7 0.0 0.)19 TL 47.00 PV Pipe: 33 53.6 2.705 PL 43.00 PP 0.3 25 10.0 0.0 28.5 0.0 3.0 120 FTG ---- PE 0.0 28 10.0 0.0 28.1 0.0 3.308 TL 43.00 PV Pipe: 34 53.6 2.705 PL 32.00 PP 0.3 28 10.0 0.0 28.1 0.0 3.0 120 FTG ---- PE 0.0 29 10.0 0.0 27.9 0.0 0.008 TL 32.00 PV Pipe: 35 53.6 2.705 PL 18.58 PP 0.1 29 10.0 0.0 27.9 0.0 3.0 120 FTG ---- PE 0.0 30 10.0 0.0 27.7 0.0 0.008 TL 18.58 PV Pipe: 36 24.7 1.598 PL 15.58 PF 5.7 30 10.0 0.0 27.7 0.0 4.0 150 FTG 2ET PH -4.3 41 20.0 0.0 22.7 0.0 0.016 TL 41.58 PV Pipe: 37 24.7 1.398 PL 36.00 PP 3.9 41 20.0 0.0 22.7 0.0 4.0 150 FTG 2E2R PE 3.0 42 20.0 0.0 21.8 0.0 0.016 TL 56.00 PV Pipe: 38 24.7 1.598 PL 22.33 PF 3.8 42 20.0 0.0 21.8 0.0 4.0 150 FTG 3E2R PE -4.3 20 30.0 0.0 16.6 0.0 0.016 TL 51.33 PV Pipe: 39 28.9 2.705 PL 3.08 PP 0.0 30 10.0 0.0 27.7 0.0 1.6 20 FTG ---- PE 3.0 31 10.0 0.0 27.7 0.0 0.()03 TL 3.08 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 QATE: 10/11/2018FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 40 0.0 1.101 PL 7.33 PP 0.0 31 10.0 0.0 27.7 0.0 0.0 150 FTG T PE 0.0 32 10.0 0.0 27.7 0.0 0.000 TL 12.33 PV Pipe: 41 0.0 1.101 PL 1.00 PP 0.0 32 10.0 0.0 27.7 0.0 0.0 150 FTC ET PE 0.0 33 10.0 0.0 27.7 0.0 0.000 TL 13.00 PV Pipe: 42 0.0 1.101 PL 6.25 PP 0.0 33 10.0 0.0 27.7 0.0 0.0 150 FTG 2E PE 0.0 34 10.0 0.0 27.7 0.0 0.000 TL 20.25 PV Pipe: 43 28.9 2.705 PL 5.58 PP 0.0 31 10.0 0.0 27.7 0.0 1.6 120 FTG ---- PE 0.0 35 10.0 0.0 27.7 0.0 0.003 TL 5.58 PV Pipe: 44 0.0 2.705 PL 5.50 PP 0.0 35 10.0 0.0 2,7.7 0.0 0.0 120 FTG ---- PE 0.0 36 10.0 0.0 27.7 0.0 0.000 TL 5.50 PV Pipe: 45 0.0 1.101 PL 7.33 PP 0.0 36 10.0 0.0 27.7 0.0 0.0 150 FTG T PE 0.0 37 10.0 0.0 27.7 0.0 0.000 TL 12.33 PV Pipe: 46 0.0 1.101 PL 1.00 PP 0.0 37 10.0 0.0 27.7 0.0 0.0 150 FTG ET PE 0.0 38 10.0 0.0 27.7 0.0 0.000 TL 13.00 PV Pipe: 47 0.0 1.101 PL 6.25 PP 0.0 37 10.0 0.0 27.7 0.0 0.0 150 FTG 2E PE 0.0 39 10.0 0.0 27.7 0.0 0.000 TL 20.25 PV Pipe: 48 -103.7 2.705 PL 10.66 PP 0.3 26 10.0 0.0 28.6 0.0 5.8 120 FTG ---- PE 0.0 TR 10.0 0.0 28.9 0.0 0.027 TL 10.66 PV Pipe: 49 -103.7 2.705 PL 5.00 PP 0.4 TR 10.0 0.0 28.9 0.0. 5.8 120 FTG E PE 2.2 FS 5.0 0.0 31.4 0.0 0.027 TL 14.36 PV Pipe: 50 -103.7 2.705 PL 4.00 PP 0.1 PS 5.0 0.0 31.4 0.0 5.8 120 FTG ---- PE 1.7 BR 1.0 0.0 33.3 0.0 0.027 TL 4.00 PV Pipe: 51 -103.7 2.705 PL 4.00 PP 0.4 BR 1.0 0.0 33.3 0.0 5.8 120 FTG E PE 1.7 Ui -3.0 0.0 35.4 0.0 0.027 TL 13.36 PV Pipe: 52 -103.7 4.240 PL 74.00 PF 0.3 Ui -3.0 0.0 35.4 0.0 2.4 150 FTG 4E PE 0.4 U2 -4.0 0.0 36.1 0.0 0.002 TL 154.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/11/2018FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 53 -103.7fl 4.220 PL 6.00 PP 0.1 U2 -4.0 0.0 36.1 0.0 2.4 140 FTG 2E PE -2.6 U3 2.0 0.0 33.6 0.0 0.002 TL 40.00 PV Pipe: 54 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 40.6 0.0 7.0 psi, 103.7 gpm U3 2.0 0.0 33.6 0.0 Pipe: 55 -103.7 4.220 PL 6.00 PP 0.1 U4 2.0 0.0 40.6 0.0 2.4 140 FTG 2E PE 2.6 US -4.0 0.0 43.3 0.0 0.002 TL 40.00 PV Pipe: 56 -103.7 4.220 PL 32.75 PP (:).2 US -4.0 0.0 43.3 0.0 2.4 140 FTG ET PH 0.0 SR -4.0 SRCE 43.5 (N/A) 0.002 TL 83,75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.078 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 7.2 ft/sec at pipe 1. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.67 psi with a flow of 222.80 gpm. PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 10/1l/2018FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOE TITLE: 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 H 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 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 PAGE: X MATERIAL: EdF1w HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) H T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 P R E S S U R E 30.0 20.0 p S 10.0 'WI -14.7 00 - 60.0 50.0 G A U G 40.0 E WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 11 pATE: '10/11/2O18FIRE SPRINKLERS\CALCS\INITIAL\6-PLEX-4HD CALC (ATTIC) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ 0\\\ 50+ \\\\ I \\\\ I \\\ 45+ \\\\ x \\\\ I \\\\ I \\\\ P 40+ \\\ R I * <-39.0 psi @ 6000 gpm E I Flow Test Point S I S 35+ U I R I E I 30+ P I S I 25+ 20+ 15+ 10+ LEGEND U I X = Required Water Supply 43.50 psi @ 203.7 gpm 5+ U I 0 = Available Water Supply I 51.68 psi @ 203.7 gpm I, 0++-+---+----+-----+------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 5600 6400 7200 8000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 11-PLEX FIRST FLOOR 4HD GARAGE CALC FILE NUMBER: 12063 DATE: OCT 12, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, ORDINARY HAZARD DENSITY: 0.15 gpm/sq. ft. AREA OF APPLICATION: 520.0 sq. ft. COVERAGE PER SPRINKLER: 130.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 5 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 99.9 gpm TOTAL WATER REQUIRED (including hose): 349.9 gpm FLOW AND PRESSURE (@ BOR) : 99.9 gpm 8 32.2 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DTflIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 4t 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/12/20181RE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST PLR (GARAGE) .SDF JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SR 51.7 39.0 6000.0 51.6 349.9 42.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 349.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 99.9 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PS) (GPM) 1 32.0 - - - - 17.2 - - - 2 30.0 - - - - 18.1 - - - 3 30.0 -- - - 18.1 - - - 4 30.0 - - - - 17.9 - - - 5 30.0 - - - - 17.8 - - - 6 30.0 - - - - 18.3 - - - 7 30.0 - - - - 18.3 - - - 8 32.0 - - - - 17.4 - - - 9 30.0 - - - - 18.3 - - - 10 32.0 - - - - 17.4 - - - 11 30.0 - - - - 18.4 - - - 12 30.0 - - - - 18.4 - - - 13 32.0 - - - - 17.6 - - - 14 30.0 - - - - 18.4 - - - 15 32.0 - - - - 17.6 - - - 16 30.0 - - - - 18.6 - - - 17 30.0 - - - - 18.6 - - - 18 30.0 - - - - 18.6 - - - 19 30.0 - - - - 18.6 - - - 20 32.0 - - - - 17.7 - - - 21 30.0 - - - - 18.6 - - - 22 30.0 - - - - 18.6 - - - 23 30.0 - - - - 18.6 - - - 24 32.0 - - - - 17.7 - - - 25 30.0 - - - - 18.6 - - - 26 30.0 - - - - 18.7 - - - 27 30.0 - - - - 18.7 - - - 28 32.0 - - - - 17.9 - - - 29 30.0 - - - - 18.7 - - - 30 32.0 - - - - 17.9 - - - 31 30.0 - - - - 18.7 - - - 32 30.0 - - - - 18.8 - - - 33 30.0 - - - - 18.9 - - - I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 bATE: I0/12/20181RE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FLR (GARAGE) .SDF JOE TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION N)DE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 34 30.0 - - - - 18.9 - - - 35 20.0 - - - - 23.3 - - - 36 20.0 - - - - 23.0 - - - 37 20.0 - - - - 22.5 - - - 38 20.0 - - - - 22.5 - - - 39 20.0 - - - - 22.5 - - - 40 20.0 - - - - 22.5 - - - 41 20.0 - - - - 22.5 - - - 42 20.0 - - - - 22.5 - - - 43 20.0 - - - - 22.5 - - - 44 20.0 - - - - 22.5 - - - 45 20.0 - - - - 22.1 - - - 46 10.0 - - - - 26.4 - - - 47 10.0 - - - - 26.3 - - - 48 10.0 - - - - 19.8 - - - 49 10.0 - -, - - 15.5 - - - 50 10.0 K= 5.60 13.4 20.5 51 10.0 - - - - 15.0 - - - 52 10.0 K= 5.60 12.8 20.0 53 10.0 - - - - 14.8 - - - 54 10.0 K= 5.60 12.4 19.7 55 10.0 - - - - 14.4 - - - 56 10.0 K= 5.60 12.1 19.5 57 10.0 K= 5.60 13.0 20.2 58 10.0 - - - - 27.2 - - - 59 10.0 - - - - 27.8 - - - TR 10.0 - - - - 27.8 - - - PS 5.0 - - - - 30.4 - - - BR 1.0 - - - - 32.2 - - - Ui -3.0 - -. - - 34.3 - - - U2 -4.0 - - - - 35.2 - - - U3 2.0 - - - - 32.7 - - - U4 2.0 - - - - 39.7 - - - U5 -4.0 - - - - 42.3 - - - SR -4.0 SOURCE 42.5 99.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Pace 4 DATE: 10/12/2018IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FLR (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 (PT) (K) (PSI) (GPM) FL/FT (PSI) S Pipe: 1 0.0 1.101 PL 2.00 PP 0.0 1 32.0 0.0 17.2 0.0 0.0 150 FTG E PE 0.9 2 30.0 0.0 18.1 0.0 0.000 TL 9.00 PV Pipe: 2 0.0 1.101 FL 6.50 PP 0.0 2 30.0 0.0 18.1 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 18.1 0.0 0.000 TL 18.50 PV Pipe: 3 22.2 1.598 PL 2.75 PF 0.1 3 30.0 0.0 18.1 0.0 3.6 150 FTG T PE 0.0 4 30.0 0.0 17.9 0.0 0.013 TL 10.75 PV Pipe: 4 22.2 2.705 PL 16.00 PP 0.1 4 30.0 0.0 17.9 0.0 1.2 120 FTG ET PE 0.0 5 30.0 0.0 17.8 0.0 0.002 TL 44.08 PV Pipe: 5 -22.2 1.598 PL 10.75 PP 0.3 3 30.0 0.0 18.1 0.0 3.6 150 FTC T PE 0.0 6 30.0 0.0 18.3 0.0 0.013 TL 18.75 PV Pipe: 6 5 0.0 1.101 PL 6.60 PP 0.0 6 30.0 0.0 18.3 0.0 0.0 150 FTG T PE C'.O 7 30.0 0.0 18.3 0.0 3.000 TL 11.60 PV Pipe: 7 0.0 1.101 PL 2.00 PF C.0 7 30.0 0.0 18.3 0.0 0.0 150 FTG T FE -C.9 8 32.0 0.0 17.4 0.0 3.000 TL 7.00 PV Pipe: 8 0.0 1.101 FL 12.25 PP 0.0 7 30.0 0.0 18.3 0.0 0.0 150 FTC ---- PE 0.0 9 30.0 0.0 18.3 0.0 3.000 TL 12.25 PV Pipe: 9 0.0 1.101 PL 2.00 PP 0.0 9 30.0 0.0 18.3 0.0 0.0 150 FTC T PE -0.9 10 32.0 0.0 17.4 0.0 0.000 TL 7.00 PV Pipe: 10 -22.2 .598 PL 10.25 PP 0.1 6 30.0 0.0 18.3 0.0 3.5 150 FTC ---- FE 0.0 11 30.0 0.0 18.4 0.0 0.013 TL 10.25 PV Pipe: 11 0.0 :.101 PL 6.60 PP 0.0 11 30.0 0.0 18.4 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 18.4 0.0 0.000 TL 11.60 PV Pipe: 12 0.0 1.101 PL 2.50 PP 3.0 12 30.0 0.0 18.4 0.0 0.0 150 FTC ET PE -3.9 13 32.0 0.0 17.6 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/12/2018IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FLR (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 13.25 PF 0.0 12 30.0 0.0 18.4 0.0 0.0 150 FTG 2E PE 0.0 14 30.0 0.0 18.4 0.0 0.000 TL 27.25 PV Pipe: 14 0.0 1.101 PL 2.00 PF 0.0 14 30.0 0.0 18.4 0.0 0.0 150 FTG 2E PE -0.9 15 32.0 0.0 17.6 0.0 0.000 TL 16.00 PV Pipe: 15 -22.2 1.598 PL 11.25 PF 0.2 11 30.0 0.0 18.4 0.0 3.6 150 FTG ---- PE 0.0 16 30.0 0.0 18.6 0.0 0.013 TL 11.25 PV Pipe: 16 0.0 1.394 PL 5.75 PF 0.0 16 30.0 0.0 18.6 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 18.6 0.0 0.000 TL 11.75 PV Pipe: 17 0.0 1.101 PL 3.25 PF 0.0 17 30.0 0.0 18.6 0.0 0.0 150 FTG T PE 0.0 18 30.0 0.0 18.6 0.0 0.000 TL 8.25 PV Pipe: 18 0.0 1.101 PL 0.90 PF 0.0 17 30.0 0.0 18.6 0.0 0.0 150 FTG ---- PE 0.0 19 30.0 0.0 18.6 0.0 0.000 TL 0.90 PV Pipe: 19 0.0 1.101 PL 2.00 PF 0.0 19 30.0 0.0 18.6 0.0 0.0 150 FTG T PE -0.9 20 32.0 0.0 17.7 0.0 0.000 TL 7.00 PV Pipe: 20 0.0 1.101 PL 10.25 PF 0.0 19 30.0 0.0 18.6 0.0 0.0 150 FTG ---- PE 0.0 21 30.0 0.0 18.6 0.0 0.000 TL 10.25 PV Pipe: 21 0.0 1.101 PL 5.00 PF 0.0 21 30.0 0.0 18.6 0.0 0.0 150 FTG ET PE 0.0 22 30.0 0.0 18.6 0.0 0.000 TL 17.00 PV Pipe: 22 0.0 1.101 PL 2.60 PF 0.0 21 30.0 0.0 18.6 0.0 0.0 150 FTG ---- PE 0.0 23 30.0 0.0 18.6 0.0 0.000 TL 2.60 PV Pipe: 23 0.0 1.101 PL 2.00 PF 0.0 23 30.0 0.0 18.6 0.0 0.0 150 FTG T PE -0.9 24 32.0 0.0 17.7 0.0 0.000 TL 7.00 PV Pipe: 24 0.0 1.101 PL 10.50 PF 0.0 23 30.0 0.0 18.6 0.0 0.0 150 FTG 2E PE 0.0 25 30.0 0.0 18.6 0.0 0.000 TL 24.50 PV Pipe: 25 -22.2 1.598 PL 10.50 PF 0.1 16 30.0 0.0 18.6 0.0 3.6 150 FTG ---- PE 0.0 26 30.0 0.0 18.7 0.0 0.013 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/12/2018IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FLR (GARAGE) .SEF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SCM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 0.0 1.i01 PL 6.60 PF 0.0 26 30.0 0.0 18.7 0.0 0.0 150 FTG T PE 0.0 27 30.0 0.0 18.7 0.0 0.000 TL 11.60 PV Pipe: 27 0.0 1.101 PL 2.00 PF 0.0 27 30.0 0.0 18.7 0.0 0.0 150 FTG T PE -0.9 28 32.0 0.0 17.9 0.0 0.000 TL 7.00 PV Pipe: 28 0.0 1.101 PL 12.75 PF 0.0 27 30.0 0.0 18.7 0.0 0.0 150 FTC ---- PE 0.0 29 30.0 0.0 18.7 0.0 0.000 TL 12.75 PV Pipe: 29 0.0 1.101 PL 2.00 PF 0.0 29 30.0 0.0 18.7 0.0 0.0 150 FTG T PE -0.9 30 32.0 0.0 17.9 0.0 0.000 TL 7.00 PV Pipe: 30 0.0 1.101 PL 3.50 PF 0.0 29 30.0 0.0 18.7 0.0 0.0 150 FTG 2E PE 0.0 31 30.0 0.0 18.7 0.0 0.000 TL 17.50 PV Pipe: 31 -22.2 2.705 PL 43.25 PF 0.1 26 30.0 0.0 18.7 0.0 1.2 120 FTG ---- PE 0.0 32 30.0 0.0 18.8 0.0 0.002 TL 43.25 PV Pipe: 32 -22.2 2.705 PL 10.10 PF 0.0 32 30.0 0.0 18.8 0.0 1.2 120 FTG T PE 0.0 33 30.0 0.0 18.9 0.0 0.002 TL 28,82 PV Pipe: 33 -22.2 2.705 PL 20.60 PF 0.1 33 30.0 0.0 18.9 0.0 1.2 120 FTC T PE 0.0 34 30.0 0.0 18.9 0.0 0.002 TL 39,32 PV Pipe: 34 -22.2 2.423 PL 1C.00 PF 0.0 34 30.0 0.0 18.9 0.0 1.5 150 FTG E PE 4.3 35 20.0 0.0 23.3 0.0 0.002 TL 22.00 PV Pipe: 35 16.0 1.598 PL 28.50 PF 0.3 35 20.0 0.0 23.3 0.0 2.6 150 FTG 2T PE 0.0 36 20.0 0.0 23.0 0.0 0.007 TL 44.50 PV Pipe: 36 16.0 1.598 PL 56.33 PF 0.5 36 20.0 0.0 23.0 0.0 2.6 150 FTG T PE 0.0 37 20.0 0.0 22.5 0.0 0.007 TL 64,33 PV Pipe: 37 0.0 1.394 PL 9.25 PF 0.0 37 20.0 0.0 22.5 0.0 0.0 150 FTC T PE 0.0 38 20.0 0.0 22.5 0.0 0.000 TL 15.25 PV Pipe: 38 0.0 1.101 PL 8,25 PF 0.0 38 20.0 0.0 22.5 0.0 0.0 150 FTG ET PE 0.0 39 20.0 0.0 22.5 0.0 0.000 TL 20.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: '10/12/20181RE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FLR (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: 39 0.0 1.101 PL 3.00 PF 0.0 38 20.0 0.0 22.5 0.0 0.0 150 FTG ---- PE 0.0 40 20.0 0.0 22.5 0.0 0.000 TL 3.00 PV Pipe: 40 0.0 1.101 PL 0.50 PF 0.0 40 20.0 0.0 22.5 0.0 0.0 150 FTG ET PE 0.0 41 20.0 0.0 22.5 0.0 0.000 TL 12.50 PV Pipe: 41 0.0 1.101 PL 6.66 PF 0.0 40 20.0 0.0 22.5 0.0 0.0 150 FTG ---- PE 0.0 42 20.0 0.0 22.5 0.0 0.000 TL 6.66 PV Pipe: 42 0.0 1.101 PL 2.33 PF 0.0 42 20.0 0.0 22.5 0.0 0.0 150 FTG ET PE 0.0 43 20.0 0.0 22.5 0.0 0.000 TL 14.33 PV Pipe: 43 0.0 1.101 PL 10.50 PF 0.0 42 20.0 0.0 22.5 0.0 0.0 150 FTG ET PE 0.0 44 20.0 0.0 22.5 0.0 0.000 TL 22.50 PV Pipe: 44 16.0 1.598 FL 38.33 PF 0.3 37 20.0 0.0 22.5 0.0 2.6 150 FTG B PE 0.0 45 20.0 0.0 22.1 0.0 0.007 TL 47.33 PV Pipe: 45 -22.2 2.423 FL 10.00 PF 0.0 45 20.0 0.0 22.1 0.0 1.5 150 FTG T PE -4.3 5 30.0 0.0 17.8 0.0 0.002 TL 22.00 PV Pipe: 46 38.3 2.423 PL 10.00 PF 0.1 45 20.0 0.0 22.1 0.0 2.7 150 FTG T PE 4.3 46 10.0 0.0 26.4 0.0 0.005 TL 22.00 PV Pipe: 47 38.3 2.705 PL 6.50 PF 0.1 46 10.0 0.0 26.4 0.0 2.1 120 FTG 2E PE 0.0 47 10.0 0.0 26.3 0.0 0.004 TL 25.22 PV Pipe: 48 99.9 1.654 FL 14.25 PF 6.5 47 10.0 0.0 26.3 0.0 14.9 120 FTG T PE 0.0 48 10.0 0.0 19.8 0.0 0.278 TL 23.37 PV Pipe: 49 99.9 1.654 PL 6.25 PF 4.3 48 10.0 0.0 19.8 0.0 14.9 120 FTG T PE 0.0 49 10.0 0.0 15.5 0.0 0.278 TL 15.37 PV Pipe: 50 20.5 1.083 PL 10.25 PF 2.1 49 10.0 0.0 15.5 0.0 7.1 120 FTG ET PE 0.0 50 10.0 5.6 13.4 20.5 0.116 TL 18.43 PV Pipe: 51 79.4 1.654 PL 2.75 PF 0.5 49 10.0 0.0 15.5 0.0 11.9 120 FTG ---- PE 0.0 51 10.0 0.0 15.0 0.0 0.182 TL 2.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/12/20181RE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST 7-LR (GARAGE).SDF JOB TITLE: PIPE TAG QGPM) DIA(IN) LENGTH PRESS END ELEV. NOZ. PT DISC. VE1(FPS) HW(C) (FT) SUP. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 52 20.0 1.083 PL 8.25 PE 2.2 51 10.0 0.0 15.0 0.0 7.0 120 FTG 2T PE 3.0 52 10.0 5.6 12.8 20.0 0.112 TL 19.93 PV Pipe: 53 59.4 1.654 PL 1.75 PF 0.2 51 10.0 0.0 15.0 0.0 8.9 120 FTG ---- PE 0.0 53 10.0 0.0 14.8 0.0 0.106 TL 1.75 PV Pipe: 54 19.7 1.083 PL 8.75 PF 2.5 53 10.0 0.0 14.8 0.0 6.9 120 FTG E2T PE 0.0 54 10.0 5.6 12.4 19.7 0.108 TL 22.77 PV Pipe: 55 39.7 1.654 PL 8.00 PF 0.4 53 10.0 0.0 14.8 0.0 5.9 120 FTG ---- PE 0.0 55 10.0 0.0 14.4 0.0 0.050 TL 8.00 PV Pipe: 56 19.5 1.083 PL 7.50 PF 2.3 55 10.0 0.0 14.4 0.0 6.8 120 FTG E2T PE 0.0 56 10.0 5.6 12.1 1.5 0.106 TL 21.52 PV Pipe: 57 20.2 1.083 PL 3.90 PF 1.4 55 10.0 0.0 14.4 3.0 7.0 120 FTG ET PE 0.0 57 10.0 5.6 13.0 23.2 0.114 TL 12.08 PV Pipe: 58 -61.6 2.705 PL 9C.00 PF 0.9 47 10.0 0.0 26.3 0.0 3.4 120 FTG ---- PE 0.0 58 10.0 0.0 27.2 0.0 0.010 TL 9C.00 PV Pipe: 59 -61.6 2.705 PL 29.75 PF 0.6 58 10.0 0.0 27.2 0.0 3.4 120 FTG ET PE 0.0 59 10.0 0.0 27.8 0.0 0 ,,010 TL 57.83 PV Pipe: 60 38.3 2.423 PL 10.00 PF 0.2 59 10.0 0.0 27.8 0.0 2.7 150 FTG ET PE -4 •3 35 20.0 0.0 23.3 0.0 0.005 TL 34.00 PV Pipe: 61 -99.9 2.705 PL 2.50 PF 0.1 59 10.0 0.0 27.8 0.0 5.6 120 FTG ---- PE 0.0 TR 10.0 0.0 27.8 0.0 0.025 TL 2.50 PV Pipe: 100 -99.9 2.705 PL 5.00 PF 0.4 TR 10.0 0.0 27.8 0.0 5.6 120 FTG K PE 2.2 FS 5.0 0.0 30.4 0.0 0.025 TL 14.36 PV Pipe: 101 -99.9 2.705 PL 4.00 PF 0.1 KS 5.0 0.0 30.4 0.0 5.6 120 FTG ---- PE 1.7 BR 1.0 0.0 32.2 0.0 0.025 TL 4.00 PV Pipe: 102 -99.9 2.705 PL 4.00 PF 0.3 BR 1.0 0.0 32.2 0.0 5.6 120 FTG E PE 1.7 Ui -3.0 0.0 34.3 0.0 0.025 TL 13.36 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 10/12/2018IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST FIR (GARAGE) .SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (TT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 103 -99.9 4.240 PL 162.00 PF 0.5 Ui -3.0 0.0 34.3 0.0 2.3 150 FIG 4E PE 0.4 U2 -4.0 0.0 35.2 0.0 0.002 TL 242.00 PV Pipe: 104 -99.9 4.220 PL 6.00 PF 0.1 U2 -4.0 0.0 35.2 0.0 2.3 140 FTC 2E PE -2.6 U3 2.0 0.0 32.7 0.0 0.002 TL 40.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 39.7 0.0 7.0 psi, 99.9 gpm U3 2.0 0.0 32.7 0.0 Pipe: 106 -99.9 4.220 PL 6.00 PF 0.1 U4 2.0 0.0 39.7 0.0 2.3 140 FIG 2E PE 2.6 U5 -4.0 0.0 42.3 0.0 0.002 TL 40.00 PV Pipe: 107 -99.9 4.220 PL 32.75 PF 0.2 U5 -4.0 0.0 42.3 0.0 2.3 140 FIG ET PE 0.0 SR -4.0 SRCE 42.5 (N/A) 0.002 TL 83.75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) under license no. 38061304 granted by HRS Systems, Inc. 208 Southside Square Petersburg, IN 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 0.108 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 14.9 ft/sec at pipe 49. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.63 psi with a flow of 364.96 gpm. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page :0 DATE: 10/12/20181RE SPRINKLERS\CALCS\INITIAL\11-PLEX-1ST .FLR 'GARAGE) .SDF JOB TITLE: (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP 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 C 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 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.30 2.423 3.00 12.00 12.00 2.00 2.00 21.00 3.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk Tee 1.083 2.34 5.84 2.34 5.84 7.01 1.17 11.68 584 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 C 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 1560 18.72 P R E S S U R E 30.0 20.0 -14.7 Rej 60.0 1 50.0 G 2 A U G 40.0 E is S ± 10.0 0.0 WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTE4 HYDRAULIC ANALYSIS Page 12 DATE: 10/12/2018IRE SPRINKLERS\CALCS\INTIAL\11-PLEX-1ST FLR (GARAGE) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ 0\\\ 50+ \\\\ I \\\\ I \\\\ I \\\ 45+ \\\\ I \\\\ x \\\\ P 40+ \\\ R I * <-39.0 psi 3 6000 gpm E I Flow Test Point S I S 35+ U I R I E 30+ P S I I 25+ 20+ 15+ 10+ LEGEND I, I X = Required Water Supply 42.53 psi @ 349.9 gpm 5+ I 0 = Available Water Supply 51.63 psi @ 349.9 gpm 0 ++ - +- - - + - - - - +-----+------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 56J0 6400 7200 8000 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 11-PLEX THIRD FLOOR UNIT-4 RESIDENTIAL 4HD CALC FILE NUMBER: 12063 DATE: OCT 12, 2018 -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: NFPA 13, LIGHT HAZARD 0.10 gpm/sq. ft. 1296.0 sq. ft. 324.0 sq. ft. 4 sprinklers 72.1 gpm 172.1 gpm 72.1 gpm @ 31.2 psi 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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) SR 51.7 39.0 6000.0 51.7 172.1 41.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 172.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 72.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 32.0 - - - - 16.8 - - - 2 30.0 - - - - 17.7 - - - 3 30.0 - - - - 17.7 - - - 4 30.0 - - - - 17.9 - - - 5 30.0 - - - - 18.0 - - - 6 30.0 - - - - 17.4 - - - 7 30.0 - - - - 17.4 - - - 8 32.0 - - - - 16.5 - - - 9 30.0 - - - - 17.4 - - - 10 32.0 - - - - 16.5 - - - 11 30.0 - - - 17.2 - - - 12 30.0 - - - - 17.2 - - - 13 32.0 - - - - 16.3 - - - 14 30.0 - - - - 17.2 - - - 15 32.0 - - - - 16.3 - - - 16 30.0 - - - - 17.0 - - -. 17 30.0 - - - - 15.5 - - - 18 30.0 K= 4.90 15.0 18.9 19 30.0 - - - - 15.3 - - - 20 32.0 - - - - 14.4 - - - 21 30.0 - - - - 13.4 - - - 22 30.0 K= 4.90 12.5 17.3 23 30.0 - - - - 13.3 - - - 24 32.0 - - - - 12.4 - - - 25 30.0 K= 4.90 12.0 17.0 26 30.0 - - - - 17.2 - - - 27 30.0 - - - - 16.5 - - - 28 32.0 - - - - 15.7 - - - 29 30.0 - - - - 15.8 - - - 30 32.0 - - - - 14.9 - - - 31 30.0 K= 4.90 14.7 18.8 32 30.0 - - - - 17.5 - - - 33 30.0 - - - - 17.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 'DATE: '10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX--3RD FLR(RES) .SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 34 30.0 - - - - 17.9 - - - 35 20.0 - - - - 22.4 - - - 36 20.0 - - - - 22.4 - - - 37 20.0 - - - - 22.4 - - - 38 20.0 - - - - 22.4 - - - 39 20.0 - - - - 22.4 - - - 40 20.0 - - - - 22.4 - - - 41 20.0 - - - - 22.4 - - - 42 20.0 - - - - 22.4 - - - 43 20.0 - - - - 22.4 - - - 44 20.0 - - - - 22.4 - - - 45 20.0 - - - - 22.4 - - - 46 10.0 - - - - 26.7 - - - 47 10.0 - - - - 26.8 - - - 48 10.0 - - - - 26.8 - - - 49 10.0 - - - - 26.8 - - - 50 10.0 - - - - 26.8 - - - 51 10.0 - - - - 26.8 - - - 52 10.0 - - - - 26.8 - - - 53 10.0 - - - - 26.8 - - - 54 10.0 - - - - 26.8 - - - 55 10.0 - - - - 26.8 - - - 56 10.0 - - - - 26.8 - - - 57 10.0 - - - - 26.8 - - - 58 10.0 - - - - 26.9 - - - 59 10.0 - - - - 27.0 - - - TR 10.0 - - - - 27.0 - - - PS 5.0 - - - - 29.4 - - - BR 1.0 - - - - 31.2 - - - Ui -3.0 - - - - 33.1 - - - U2 -4.0 - - - - 33.8 - - - U3 2.0 - - - - 31.2 - - - U4 2.0 - - - - 38.2 - - - U5 -4.0 - - - - 40.9 - - - SR -4.0 SOURCE 41.0 72.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEIX-3RD FLR(RES) .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 2.00 PF 0.0 1 32.0 0.0 16.8 0.0 0.0 150 FTG E PE 0.9 2 30.0 0.0 17.7 0.0 0.000 TL 9.00 PV Pipe: 2 0.0 1.101 PL 6.50 PF 0.0 2 30.0 0.0 17.7 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 17.7 0.0 0.000 TL 18.50 PV Pipe: 3 -25.3 1.598 PL 2.75 PF 0.2 3 30.0 0.0 17.7 0.0 4.1 150 FTG T PE 0.0 4 30.0 0.0 17.9 0.0 0.017 TL 10.75 PV Pipe: 4 -25.3 2.705 PL 16.00 PF 0.1 4 30.0 0.0 17.9 0.0 1.4 120 FTG ET PE 0.0 5 30.0 0.0 18.0 0.0 0.002 TL 44.08 PV Pipe: 5 25.3 1.598 PL 10.75 PF 0.3 3 30.0 0.0 17.7 0.0 4.1 150 FTG T PE 0,0 6 30.0 0.0 17.4 0.0 0.017 TL 16.75 PV Pipe: 6 0.0 1.101 PL 6.60 PF 0.0 6 30.0 0.0 17.4 0.0 0.0 150 FTG T PE 0.0 7 30.0 0.0 17.4 0.0 0.000 TL 11.60 PV Pipe: 7 0.0 1.101 PL 2.00 PF 0.0 7 30.0 0.0 17.4 0.0 0.0 150 FTG T PE -0.9 8 32.0 0.0 16.5 0.0 0.000 TL 7.00 PV Pipe: 8 0.0 1.101 PL 12.25 PF 0.0 7 30.0 0.0 17.4 0.0 0.0 150 FTG ---- PE 0.0 9 30.0 0.0 17.4 0.0 0.000 TL 12.25 PV Pipe: 9 0.0 1.101 PL 2.00 PP 0.0 9 30.0 0.0 17.4 0.0 0.0 150 FTG T PE -0.9 10 32.0 0.0 16.5 0.0 0.000 TL '.00 PV Pipe: 10 25.3 1.598 PL 10.25 PF 0.2 6 30.0 0.0 17.4 0.0 4.1 150 FTC ---- PP 0.0 11 30.0 0.0 17.2 0.0 0.017 TL 10.25 PV Pipe: 11 0.0 1.101 PL 6.60 PP 0.0 11 30.0 0.0 17.2 0.0 0.0 150 FTC T PE 0.0 12 30.0 0.0 17.2 0.0 0.000 TL 11.60 PV Pipe: 12 0.0 1.101 PL 2.50 PP 0.0 12 30.0 0.0 17.2 0.0 0.0 150 FTG ET PE -0.9 13 32.0 0.0 16.3 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE:1 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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 13.25 PF 0.0 12 30.0 0.0 17.2 0.0 0.0 150 FTC 2E PE 0.0 14 30.0 0.0 17.2 0.0 0.000 TL 27.25 PV Pipe: 14 0.0 1.101 PL 2.00 PF 0.0 14 30.0 0.0 17.2 0.0 0.0 150 FTG 2E PE -0.9 15 32.0 0.0 16.3 0.0 0.000 TL 16.00 PV Pipe: 15 25.3 1.598 PL 11.25 PF 0.2 11 30.0 0.0 17.2 0.0 4.1 150 FTG ---- PE 0.0 16 30.0 0.0 17.0 0.0 0.017 TL 11.25 PV Pipe: 16 53.3 1.394 PL 5.75 PF 1.6 16 30.0 0.0 17.0 0.0 11.2 150 FTG T PE 0.0 17 30.0 0.0 15.5 0.0 0.132 TL 11.75 PV Pipe: 17 18.9 1.101 PL 3.25 PF 0.5 17 30.0 0.0 15.5 0.0 6.4 150 FTG T PE 0.0 18 30.0 4.9 15.0 18.9 0.062 TL 8.25 PV Pipe: 18 34.3 1.101 PL 0.90 PF 0.2 17 30.0 0.0 15.5 0.0 11.6 150 FTG ---- PE 0.0 19 30.0 0.0 15.3 0.0 0.185 TL 0.90 PV Pipe: 19 0.0 1.101 PL 2.00 PF 0.0 19 30.0 0.0 15.3 0.0 0.0 150 FTG T PE -0.9 20 32.0 0.0 14.4 0.0 0.000 TL 7.00 PV Pipe: 20 34.3 1.101 PL 10.25 PF 1.9 19 30.0 0.0 15.3 0.0 11.6 150 FTG ---- PE 0.0 21 30.0 0.0 13.4 0.0 0.185 TL 10.25 PV Pipe: 21 17.3 1.101 PL 5.00 PF 0.9 21 30.0 0.0 13.4 0.0 5.8 150 FTG ET PE 0.0 22 30.0 4.9 12.5 17.3 0.052 TL 17.00 PV Pipe: 22 17.0 1.101 PL 2.60 PF 0.1 21 30.0 0.0 13.4 0.0 5.7 150 FTG ---- PE 0.0 23 30.0 0.0 13.3 0.0 0.050 TL 2.60 PV Pipe: 23 0.0 1.101 PL 2.00 PF 0.0 23 30.0 0.0 13.3 0.0 0.0 150 FTG T PS -0.9 24 32.0 0.0 12.4 0.0 0.000 TL 7.00 PV Pipe: 24 17.0 1.101 PL 10.50 PF 1.2 23 30.0 0.0 13.3 0.0 5.7 150 FTC 2E PE 0.0 25 30.0 4.9 12.0 17.0 0.050 TL 24.50 PV Pipe: 25 -28.0 1.598 PL 10.50 PF 0.2 16 30.0 0.0 17.0 0.0 4.5 150 FTG ---- PE 0.0 26 30.0 0.0 17.2 0.0 0.021 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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 18.8 1.101 PL 6.60 PF 0.7 26 30.0 0.0 17.2 0.0 6.3 150 FTG T PE 0.0 27 30.0 0.0 16.5 0.0 0.061 TL 11.60 PV Pipe: 27 0.0 1.101 PL 2.00 PF 0.0 27 30.0 0.0 16.5 0.0 0.0 150 FTG T PE -0.9 28 32.0 0.0 15.7 0.0 0.000 TL 7.00 PV Pipe: 28 18.8 1.101 FL 12.75 PS 0.8 27 30.0 0.0 16.5 0.0 6.3 150 FTG ---- FE 0.0 29 30.0 0.0 15.8 0.0 0.061 TL 12.75 PV Pipe: 29 0.0 1.101 PL 2.00 PF 0.0 29 30.0 0.0 15.8 0.0 0.0 150 FTG T PE -0.9 30 32.0 0.0 14.9 0.0 0.000 TL 7.00 PV Pipe: 30. 18.8 1.101 PL 3.50 PS 1.1 29 30.0 0.0 15.8 0.0 6.3 150 FTG 2E PE 0.0 31 30.0 4.9 14.7 18.8 0.061 TL 17.50 PV Pipe: 31 -46.7 2.705 FL 43.25 PS 0.3 26 30.0 0.0 17.2 0.0 2.6 120 FTG ---- PE 3.0 32 30.0 0.0 17.5 0.0 0.006 TL 43.25 PV Pipe: 32 -46.7 2.705 PL 10.10 PS 3.2 32 30.0 0.0 17.5 0.0 2.6 120 FTG T PR J.0 33 30.0 0.0 17.7 0.0 0.006 TL 28.82 PV Pipe: 33 -46.7 2.705 PL 20.60 PS 0.2 33 30.0 0.0 17.7 0.0 2.6 120 FTG T FE 0.0 34 30.0 0.0 17.9 . 0.0 0.006 TL 39.32 PV Pipe: 34 -46.7 2.423 FL :0.00 PS 0.2 34 30.0 0.0 17.9 0.0 3.3 150 FTG E FE 4.3 35 20.0 0.0 22.4 0.0 0.007 TL 22.00 PV Pipe: 35 2.9 1.598 FL 28.50 PF 0.0 35 20.0 0.0 22.4 0.0 0.5 150 FTG 2T FE 0.0 36 20.0 0.0 22.4 0.0 0.000 TL 44.50 PV Pipe: 36 2.9 1.598 FL E6.33 PS 0.0 36 20.0 0.0 22.4 0.0 0.5 150 FTG T FE 0.0 37 20.0 0.0 22.4 0.0 0.000 TL €4.33 PV Pipe: 37 0.0 1.394 FL 9.25 PS 0.0 37 20.0 0.0 22.4 0.0 0.0 150 FTG T FE 0.0 38 20.0 0.0 22.4 0.0 0.000 TL 15.25 PV Pipe: 38 0.0 1.101 FL 8.25 PS C.0 38 20.0 0.0 22.4 0.0 0.0 150 FTG ET FE C.0 39 20.0 0.0 22.4 .0.0 0.000 TL 20.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: '10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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 0.0 1.101 PL 3.00 PF 0.0 38 20.0 0.0 22.4 0.0 0.0 150 FTG ---- PH 0.0 40 20.0 0.0 22.4 0.0 0.000 TL 3.00 PV Pipe: 40 0.0 1.101 PL 0.50 PF 0.0 40 20.0 0.0 22.4 0.0 0.0 150 FTG ET PE 0.0 41 20.0 0.0 22.4 0.0 0.000 TL 12.50 PV Pipe: 41 0.0 1.101 PL 6.66 PF 0.0 40 20.0 0.0 22.4 0.0 0.0 150 FTG ---- PE 0.0 42 20.0 0.0 22.4 0.0 0.000 TL 6.66 PV Pipe: 42 0.0 1.101 PL 2.33 PF 0.0 42 20.0 0.0 22.4 0.0 0.0 150 FTG ET PH 0.0 43 20.0 0.0 22.4 0.0 0.000 TL 14.33 PV Pipe: 43 0.0 1.101 PL 10.50 PF 0.0 42 20.0 0.0 22.4 0.0 0.0 150 FTG ET PH 0.0 44 20.0 0.0 22.4 0.0 0.000 TL 22.50 PV Pipe: 44 2.9 1.598 PL 38.33 PF 0.0 37 20.0 0.0 22.4 0.0 0.5 150 FTG E PH 0.0 45 20.0 0.0 22.4 0.0 0.000 TL 47.33 PV Pipe: 45 25.3 2.423 PL 10.00 PF 0.0 45 20.0 0.0 22.4 0.0 1.8 150 FTG T PH -4.3 5 30.0 0.0 18.0 0.0 0.002 TL 22.00 PV Pipe: 46 -22.4 2.423 PL 10.00 PF 0.0 45 20.0 0.0 22.4 0.0 1.6 150 FTG T PE 4.3 46 10.0 0.0 26.7 0.0 0.002 TL 22.00 PV Pipe: 47 -22.4 2.705 PL 6.50 PF 0.0 46 10.0 0.0 26.7 0.0 1.3 120 FTG 2E PH 0.0 47 10.0 0.0 26.8 0.0 0.002 TL 25.22 PV Pipe: 48 0.0 1.654 PL 14.25 PF 0.0 47 10.0 0.0 26.8 0.0 0.0 120 FTC T PH 0.0 48 10.0 0.0 26.8 0.0 0.000 TL 23.37 PV Pipe: 49 0.0 1.654 PL 6.25 PF 0.0 48 10.0 0.0 26.8 0.0 0.0 120 FTG T PH 0.0 49 10.0 0.0 26.8 0.0 0.000 TL 15.37 PV Pipe: 50 0.0 1.083 PL 10.25 PF 0.0 49 10.0 0.0 26.8 0.0 0.0 120 FTG ET PH 0.0 50 10.0 0.0 26.8 0.0 0.000 TL 18.43 PV Pipe: 51 0.0 1.654 PL 2.75 PF 0.0 49 10.0 0.0 26.8 0.0 0.0 120 FTG ---- PH 0.0 51 10.0 0.0 26.8 0.0 0.000 TL 2.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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: 52 0.0 1.083 PL 8.25 PP 3.0 51 10.0 0.0 26.8 0.0 0.0 120 FTG 2T PE 3.0 52 10.0 0.0 26.8 0.0 0.000 TL 19.93 PV Pipe: 53 0.0 1.654 PL 1.75 PP 0.0 51 10.0 0.0 26.8 0.0 0.0 120 FTG ---- PE 3.0 53 10.0 0.0 26.8 0.0 0.000 TL 1.75 PV Pipe: 54 0.0 1.083 PL 8.75 PP 3.0 53 10.0 0.0 26.8 0.0 0.0 120 FTG E2T PE 0.0 54 10.0 0.0 26.8 0.0 0.000 TL 22.77 PV Pipe: 55 0.0 1.654 PL 8.00 PP 0.0 53 10.0 0.0 26.8 0.0 0.0 120 FTG ---- PE 0.0 55 10.0 0.0 26.8 0.0 0.000 TL 8.00 PV Pipe: 56 0.0 1.083 PL 7.50 PP 0.0 55 10.0 0.0 26.8 L O.0 0.0 120 FTG E2T PE 0.0 56 10.0 0.0 26.8 0.0 0.000 TL 21.52 PV Pipe: 57 0.0 1.083 PL 390 PP 0.0 55 10.0 0.0 26.8 0.0 0.0 120 FTG ET PE 0.0 57 10.0 0.0 26.8 0.0 0.000 TL 12.08 PV Pipe: 58 -22.4 2.705 PL 90.00 PF 0.1 47 10.0 0.0 26..8 0.0 1.3 120 FTG ---- PE 0.0 58 10.0 0.0 26.9 0.0 0.002 TL 90.00 PV Pipe: 59 -22.4 2.705 PL 29.75 PP 0.1 58 10.0 0.0 26.9 0.0 1.3 120 FTG ET PE (LU 59 100 0.0 27.0 0.0 0.002 TL 57.83 PV Pipe: 60 49.6 2.423 PL 10.00 PP 0.3 59 10.0 0.0 27.0 0.0 3.5 150 FTG ET PE -4.3 35 20.0 0.0 22.4 0.0 0.008 TL 34.00 PV Pipe: 61 -72.1 2.705 PL 2.50 PP 0.0 59 10.0 0.0 27.0 0.0 4.0 120 FTG ---- PE 0.0 TR 10.0 0.0 27.0 0.0 0.014 TL 2.50 PV Pipe: 100 -72.1 2.705 PL 5.00 PP 0.2 TR 10.0 0.0 27.0 0.0 4.0 120 FTG E PE 2.2 PS 5.0 0.0 29.4 0.0 0.014 TL 14.36 PV Pipe: 101 -72.1 2.705 PL 4.00 PP C.i FS 5.0 0.0 29.4 0.0 4.0 120 FTG ---- PE 1.7 BR 1.0 0.0 31.2 0.0 0.014 TL 4.00 PV Pipe: 102 -72.1 2.705 PL 400 PP 0.2 BR 1.0 0.0 31.2 0.0 4.0 120 FTG E PE 1.7 Ui -3.0 0.0 33.1 0.0 0.014 TL 13.36 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 'DATE: !10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-3RD FLR(RES) .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: 103 -72.1 4.240 PL 162.00 PF 0.2 Ui -3.0 0.0 33.1 0.0 1.6 150 FTG 4E PE 0.4 U2 -4.0 0.0 33.8 0.0 0.001 TL 242.00 PV Pipe: 104 -72.1 4.220 PL 6.00 PF 0.0 U2 -4.0 0.0 33.8 0.0 1.7 140 FTG 2E PE -2.6 U3 2.0 0.0 31.2 0.0 0.001 TL 40.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 38.2 0.0 7.0 psi, 72.1 gpm U3 2.0 0.0 31.2 0.0 Pipe: 106 -72.1 4.220 PL 6.00 PF 0.0 U4 2.0 0.0 38.2 0.0 1.7 140 FTG 2E PE 2.6 U5 -4.0 0.0 40.9 0.0 0.001 TL 40.00 PV Pipe: 107 -72.1 4.220 PL 32.75 PF 0.1 U5 -4.0 0.0 40.9 0.0 1.7 140 FTG ST PE 0.0 SR -4.0 SRCE 41.0 (N/A) 0.001 TL 83.75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.122 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 11.6 ft/sec at pipe 18. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.68 psi with a flow of 190.31 gpm. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX--3RD FLR(RES) .SDF JOB TITLE: 14 (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G U Eli Tee LngEll ChkVlv BfyViv 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 NP?ee 4.240 20.00 39.00 12.00 43.00 23.00 4.00 39.0 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 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.CO 2.423 3.00 12.00 12.00 2.00 2.00 21.00 3.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B C A D N Eli Tee LngEll ChkVlv BfjVlv 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 10.25 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 BfvVlv GatVlv AlmCh1 D?Vlv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 P R E S S U R E 30.0 20.0 p S ± 10.0 0.0 -14.7 Kai 60. 0 50.0 G A U G 40.0 E WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 10/12/2018AD\FIRE SPRINKLERS\CALCS\INIiIAL\11-PLEX-3RD ?LR(RES) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ 50+ \\\\ I \\\\ I \\\ 45+ \\\\ I \\\\ x \\\\ P 40+ \\\ R I * <-39.0 psi @ 6000 gprn E I Flow Test Pcirt S I S 35+ U I R I E I 30+ P I S I I 25+ 20+ 15+ 10+ LEGEND I, I X = Required Water Supply " I 40.99 psi @ 172.1 gprn 5+ I 0 = Available Water Supply I 51.68 psi @ 172.1 gprn I, 0 + + - +- - - +- - - - +-----+------+--------+--------+---------+-----------+ 16002400 3200 4000 4800 5600 6400 720() 8030 FLOW (GPM) RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 11-PLEX SECOND FLOOR UNIT-4 RESIDENTIAL 4HD CALC FILE NUMBER: 12063 DATE: OCT 12, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 1296.0 sq. ft. COVERAGE PER SPRINKLER: 324.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 4 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 71.0 gpm TOTAL WATER REQUIRED (including hose) : 171.0 gpm FLOW AND PRESSURE (0 BOR) : 71.0 gpm 0 30.2 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE 4t 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PL3X-2ND FLR.SJE JOB TITLE: WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVA:L. TOTAL REQD NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (P51) (GPM) (PS:) SR 51.7 39.0 6000.0 51.7 171.0 39.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 11.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 71.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GSM) 1 32.0 - - - - 16.0 - - - 2 30.0 - - - - :6.8 - - - 3 30.0 - - - - 16.8 - - - 4 30.0 - - - - 6.8 - - 5 30.0 - - - - :6.8 - - - 6 30.0 - - - - 16.3 - - - 7 30.0 - - - - :6.9 - - - 8 32.0 - - - - :6.: - - - 9 30.0 - - - - :6.9 - - - 10 32.0 - - - - 11 30.0 - - - - :7.0 - - - 12 30.0 - - - - 17.0 - - - 13 32.0 - - - - 16.: - - - 14 30.0 - - - - 17.0 - - - 15 32.0 - - - - 16.: - - - 16 30.0 - - - - 17.0 - - - 17 30.0 - - - - 17.0 - - - 18 30.0 - - - - 17.0 - - - 19 30.0 - - - - 17.0 - - - 20 32.0 - - - - 16.: - - - 21 30.0 - - - - 17.0 - - - 22 30.0 - - - - 17.0 - - - 23 30.0 - - - - 17.0 - - - 24 32.0 - - - - 16. - - 25 30.0 - - - - 7.0 - - - 26 30.0 - - - - :7.: - - - 27 30.0 - - - - 7. - - - 28 32.0 - - - - 6.2 - - - 29 30.0 - - - - 17.1 - - - 30 32.0 - - - - 16.2 - - - 31 30.0 - - - - 17.1 - - - 32 30.0 - - - - 17.1 - - - 33 30.0 - - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1O/12/2O18ARLSBAD\E'IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (PT) (PSI) (GPM) 34 30.0 - - - - 17.1 - - - 35 20.0 - - - - 21.5 - - - 36 20.0 - - - - 20.5 - - - 37 20.0 - - - - 19.0 - - - 38 20.0 - - - - 15.6 - - - 39 20.0 K= 4.90 14.4 18.6 40 20.0 - - - - 14.4 - - - 41 20.0 K= 4.90 13.7 18.1 42 20.0 - - - - 13.2 - - - 43 20.0 K= 4.90 12.4 17.3 44 20.0 K= 4.90 12.0 17.0 45 20.0 - - - - 21.1 - - - 46 10.0 - - - - 25.5 - - - 47 10.0 - - - - 25.6 - - - 48 10.0 - - - - 25.6 - - - 49 10.0 - - - - 25.6 - - - 50 10.0 - - - - 25.6 - - - 51 10.0 - - - - 25.6 - - - 52 10.0 - - - - 25.6 - - - 53 10.0 - - - - 25.6 - - - 54 10.0 - - - - 25.6 - - - 55 10.0 - - - - 25.6 - - - 56 10.0 - - - - 25.6 - - - 57 10.0 - - - - 25.6 - - - 58 10.0 - - - - 25.8 - - - 59 10.0 - - - - 26.0 - - - TR 10.0 - - - - 26.0 - - - PS 5.0 - - - - 28.4 - - - BR 1.0 - - - - 30.2 - - - Ui -3.0 - - - - 32.1 - - - U2 -4.0 - - - - 32.7 - - - U3 2.0 - - - - 30.2 - - - U4 2.0 - - - - 37.2 - - - U5 -4.0 - - - - 39.8 - - - SR -4.0 SOURCE 39.9 71.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.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 2.00 PF 0.0 1 32.0 0.0 16.0 0.0 0.0 150 FTG E PE 0.9 2 30.0 0.0 16.8 0.0 0.000 TL 9.00 PV Pipe: 2 0.0 1.101 PL 6.50 PF 0.0 2 30.0 0.0 16.8 0.0 0.0 150 FTG ET PE 0.0 3 30.0 0.0 16.8 0.0 0.000 TL 18.50 PV Pipe: 3 11.8 1.598 PL 2.75 PF 0.0 3 30.0 0.0 16.8 0.0 1.9 150 FTG T PE 0.0 4 30.0 0.0 16.8 0.0 0.004 TL 10.75 PV Pipe: 4 11.8 2.705 PL 16.00 PF 0.0 4 30.0 0.0 16.8 0.0 0.7 120 FTG ET PE 0.0 5 30.0 0.0 16.8 0.0 0.000 TL 44.08 PV Pipe: 5 -11.8 1.598 PL 10.75 PF I- 0.1 3 30.0 0.0 16.8 0.0 1.9 150 FTG T PE 0.0 6 30.0 0.0 16.9 0.0 0.004 TL 18.75 PV Pipe: 6 0.0 1.101 PL 6.60 PF 0.0 6 30.0 0.0 16.9 0.0 0.0 150 FTG T PE 0.0 7 30.0 0.0 16.9 0.0 3.000 TL 11.60 PV Pipe: 7 0.0 1.101 PL 2.00 PF 0.0 7 30.0 0.0 16.9 0.0 0.0 150 FTG T PE -0.9 8 32.0 0.0 16.1 0.0 3.000 TL 7.00 PV Pipe: 8 0.0 1.101 PL 12.25 PF 0.0 7 30.0 0.0 16.9 0.0 0.0 150 FTG ---- PE 0.0 9 30.0 0.0 16.9 0.0 0.000 TL 12.25 PV Pipe: 9 0.0 1.101 PL 2.00 PF 0.0 9 30.0 0.0 16.9 C.0 0.0 150 FTG T PE -0.9 10 32.0 0.0 16.1 0.0 0.000 TL 7.00 PV Pipe: 10 -11.8 1.598 PL 10.25 PF 0.0 6 30.0 0.0 16.9 0.0 1.9 150 FTG ---- PE 0.0 11 30.0 0.0 17.0 0.0 0.004 TL 10.25 PV Pipe: 11 0.0 1.101 PL 6.60 PF 0.0 11 30.0 0.0 17.0 0.0 0.0 150 FTG T PE 0.0 12 30.0 0.0 17.0 0.0 0.000 TL 11.60 PV Pipe: 12 0.0 .101 PL 2.50 PF 0.0 12 30.0 0.0 17.0 0.0 0.0 150 FTG ET P -0.9 13 32.0 0.0 16.1 0.0 0.000 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE:' 1O/12/2O18ARLSBAD\F'IRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.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 13.25 PF 0.0 12 30.0 0.0 17.0 0.0 0.0 150 FTG 2E PE 0.0 14 30.0 0.0 17.0 0.0 0.000 TL 27.25 PV Pipe: 14 0.0 1.101 PL 2.00 PP 0.0 14 30.0 0.0 17.0 0.0 0.0 150 FTG 2E PE -0.9 15 32.0 0.0 16.1 0.0 0.000 TL 16.00 PV Pipe: 15 -11.8 1.598 PL 11.25 PF 0.0 11 30.0 0.0 17.0 0.0 1.9 150 FTG ---- PE 0.0 16 30.0 0.0 17.0 0.0 0.004 TL 11.25 PV Pipe: 16 0.0 1.394 PL 5.75 PP 0.0 16 30.0 0.0 17.0 0.0 0.0 150 FTG T PE 0.0 17 30.0 0.0 17.0 0.0 0.000 TL 11.75 PV Pipe: 17 0.0 1.101 PL 3.25 PP 0.0 17 30.0 0.0 17.0 0.0 0.0 150 FTG T PE 0.0 18 30.0 0.0 17.0 0.0 0.000 TL 8.25 PV Pipe: 18 0.0 1.101 PL 0.90 PP 0.0 17 30.0 0.0 17.0 0.0 0.0 150 FTC ---- PE 0.0 19 30.0 0.0 17.0 0.0 0.000 TL 0.90 PV Pipe: 19 0.0 1.101 PL 2.00 PP 0.0 19 30.0 0.0 17.0 0.0 0.0 150 FTG T PE -0.9 20 32.0 0.0 16.1 0.0 0.000 TL 7.00 PV Pipe: 20 0.0 1.101 PL 10.25 PP 0.0 19 30.0 0.0 17.0 0.0 0.0 150 FTG ---- PE 0.0 21 30.0 0.0 17.0 0.0 0.000 TL 10.25 PV Pipe: 21 0.0 1.101 PL 5.00 PP 0.0 21 30.0 0.0 17.0 0.0 0.0 150 FTC ET PE 0.0 22 30.0 0.0 17.0 0.0 0.000 TL 17.00 PV Pipe: 22 0.0 1.101 PL 2.60 PP 0.0 21 30.0 0.0 17.0 0.0 0.0 150 FTG ---- PE 0.0 23 30.0 0.0 17.0 0.0 0.000 TL 2.60 PV Pipe: 23 0.0 1.101 PL 2.00 PF 0.0 23 30.0 0.0 17.0 0.0 0.0 150 FTG T PP -0.9 24 32.0 0.0 16.1 0.0 0.000 TL 7.00 PV Pipe: 24 0.0 1.101 PL 10.50 PP 0.0 23 30.0 0.0 17.0 0.0 0.0 150 FTG 2E PE 0.0 25 30.0 0.0 17.0 0.0 0.000 TL 24.50 PV Pipe: 25 -11.8 1.598 PL 10.50 PP 0.0 16 30.0 0.0 17.0 0.0 1.9 150 FTG ---- PE 0.0 26 30.0 0.0 17.1 0.0 0.004 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\1-?LEX-2D FLR.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 6.60 PF 0.0 26 30.0 0.0 17.1 0.0 0.0 150 FTG T PE 0.0 27 30.0 0.0 17.1 0.0 0.000 TL 11.60 PV Pipe: 27 0.0 1.101 PL 2.00 PF 0.0 27 30.0 0.0 17.1 0.0 0.0 150 FTG T PE -0.9 28 32.0 0.0 16.2 0.0 0.000 TL 7.00 PV Pipe: 28 0.0 1.101 PL 12.75 PF C.0 27 30.0 0.0 17.1 0.0 0.0 150 FTG ---- FE 0.0 29 30.0 0.0 17.1 0.0 0.000 TL 12.75 PV Pipe: 29 0.0 1.101 PL 2.00 PF 0.0 29 30.0 0.0 17.1 0.0 0.0 150 FTG T FE -0.9 30 32.0 0.0 16.2 0.0 0.000 TL 7.00 PV Pipe: 30 0.0 1.101 PL 3.50 PF C.0 29 30.0 0.0 17.1 0.0 0.0 150 FTG 2E PE 0.0 31 30.0 0.0 17.1 0.0 0.000 TL 17.50 PV Pipe: 31 -11.8 2.705 PL 43.25 PF 0.0 26 30.0 0.0 17.1 0.0 0.7 120 FTG ---- FE 0.0 32 30.0 0.0 17.1 0.0 0.000 TL 43.25 PV Pipe: 32 -11.8 2.705 FL 10.10 PF 0.0 32 30.0 0.0 17.1 0.0 0.7 120 FTG T FE 0.0 33 30.0 0.0 17.1 0.0 0.000 TL 2.82 PV Pipe: 33 -11.8 2.705 PL 20.60 PF 0.0 33 30.0 0.0 17.1 0.0 0.7 120 FTG T FE 0.0 34 30.0 0.0 17.1 0.0 0.000 TL 39.32 PV Pipe: 34 -11.8 2.423 PL 1C.00 PP 0.0 34 30.0 0.0 17.1 0.0 0.8 150 FTG E FE 43 35 20.0 0.0 21.5 0.0 0.001 TL 22.00 PV Pipe: 35 29.1 1.598 PL 28.50 PP 1.0 35 20.0 0.0 21.5 0.0 4.7 150 FTG 2T FE 0.0 36 20.0 0.0 20.5 0.0 0.022 TL 44.50 PV Pipe: 36 29.1 1.598 PL 58.33 PP :.4 36 20.0 0.0 20.5 0.0 4.7 150 FTG T PE 0.0 37 20.0 0.0 19.0 0.0 0.022 TL 64.33 PV Pipe: 37 71.0 1.394 PL S.25 PP 3.4 37 20.0 0.0 19.0 0.0 14.9 150 FTG T FE 0.0 38 20.0 0.0 15.6 0.0 0.225 TL 15.25 PV Pipe: 38 18.6 1.101 FL 8.25 PF 38 20.0 0.0 15.6 0.0 6.3 150 FTG ET FE 0.0 39 20.0 4.9 14.4 18.6 0.059 TL 2C.25 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE:' 10/12/2018ARLSBAD\PIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND PLR.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 52.4 1.101 PL 3.00 PP 1.2 38 20.0 0.0 15.6 0.0 17.7 150 FTG ---- PE 0.0 40 20.0 0.0 14.4 0.0 0.404 TL 3.00 PV Pipe: 40 18.1 1.101 PL 0.50 PF 0.7 40 20.0 0.0 14.4 0.0 6.1 150 FTG ET PE 0.0 41 20.0 4.9 13.7 18.1 0.057 TL 12.50 PV Pipe: 41 34.3 1.101 PL 6.66 PP 1.2 40 20.0 0.0 14.4 0.0 11.5 150 FTG ---- PE 0.0 42 20.0 0.0 13.2 0.0 0.184 TL 6.66 PV Pipe: 42 17.3 1.101 PL 2.33 PF 0.7 42 20.0 0.0 13.2 0.0 5.8 150 FTG ET PE 0.0 43 20.0 4.9 12.4 17.3 0.052 TL 14.33 PV Pipe: 43 17.0 1.101 PL 10.50 PP 1.1 42 20.0 0.0 13.2 0.0 5.7 150 FTG ET PE 0.0 44 20.0 4.9 12.0 17.0 0.050 TL 22.50 PV Pipe: 44 -41.9 1.598 PL 38.33 PF 2.1 37 20.0 0.0 19.0 0.0 6.7, 150 FTG K PR 0.0 45 20.0 0.0 21.1 0.0 0.044 TL 47.33 PV Pipe: 45 -11.8 2.423 PL 10.00 PP 0.0 45 20.0 0.0 21.1 0.0 0.8 150 FTG T PR -4.3 5 30.0 0.0 16.8 0.0 0.001 TL 22.00 PV Pipe: 46 -30.1 2.423 PL 10.00 PP 0.1 45 20.0 0.0 21.1 0.0 2.1 150 FTG T PE 4.3 46 10.0 0.0 25.5 0.0 0.003 TL 22.00 PV Pipe: 47 -30.1 2.705 PL 6.50 PP 0.1 46 10.0 0.0 25.5 0.0 1.7 120 FTG 2E PR 0.0 47 10.0 0.0 25.6 0.0 0.003 TL 25.22 PV Pipe: 48 0.0 1.654 PL 14.25 PP 0.0 47 10.0 0.0 25.6 0.0 0.0 120 FTG T PE 0.0 48 10.0 0.0 25.6 0.0 0:000 TL 23.37 PV Pipe: 49 0.0 1.654 PL 6.25 PP 0.0 48 10.0 0.0 25.6 0.0 0.0 120 FTG T PE 0.0 49 10.0 0.0 25.6 0.0 0.000 TL 15.37 PV Pipe: 50 0.0 1.083 PL 10.25 PP 0.0 49 10.0 0.0 25.6 0.0 0.0 120 FTG ET PE 0.0 50 10.0 0.0 25.6 0.0 0.000 TL 18.43 PV Pipe: 51 0.0 1.654 PL 2.75 PP 0.0 49 10.0 0.0 25.6 0.0 0.0 120 FTG ---- PE 0.0 51 10.0 0.0 25.6 0.0 0.000 TL 2.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.SDF JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(PPS) HW(C) (PT) SUM. 'P1 NODES (FT) (K) (PSI) (GPM) FL/FT (PS:) Pipe: 52 0.0 1.083 PL 8.25 PP 0.0 51 10.0 0.0 25.6 0.0 0.0 1 120 FTG 2T PE 0.0 52 10.0 0.0 25.6 0.0 0.000 TL 19.93 PV Pipe: 53 0.0 1.654 PL 1.75 PP 0.0 51 10.0 0.0 25.6 0.0 0.0 120 FTG ---- PE 0.0 53 10.0 0.0 25.6 0.0 0.000 TL 1.75 PV Pipe: 54 0.0 1.083 PL 8.75 PP 0.0 53 10.0 0.0 25.6 0.0 0.0 120 FTG E2T PE 0.0 54 10.0 0.0 25.6 0.0 0.000 TL 22.77 PV Pipe: 55 0:0 1.654 PL 8.00 PP 0.0 53 10.0 0.0 25.6 0.0 0.0 120 FTG ---- PE 0.0 55 10.0 0.0 25.6 0.0 0.000 TL 8.00 PV Pipe: 56 0.0 1.083 PL 7.50 PP 0.0 55 10.0 0.0 25.6 0.0 0.0 120 FTG E2T PE 0.0 56 10.0 0.0 25.6 0.0 0.000 TL 21.52 PV Pipe: 57 0.0 1.083 PL 3.90 PF 0.0 55 10.0 0.0 25.6 0.0 0.0 120 FTG ET PE 0.0 57 10.0 0.0 25.6 0.0 0.000 TL 12.08 PV Pipe: 58 -30.1 2.705 PL 90.00 PF 0.2 47 10.0 0.0 25.6 0.0 1.7 120 FTG ---- PP 0.0 58 10.0 0.0 25.8 0.0 0.003 TL 90.00 PV Pipe: 59 -30.1 2.705 PL 29.75 PP 0.2 58 10.0 0.0 25.8 0.0 1.7 120 FTG ET PE 0.0 59 10.0 0.0 26.0 0.0 0.003 TL 57.83 PV Pipe: 60 40.9 2.423 PL 10.00 PF 0.2 59 10.0 0.0 26.0 0.0 2.8 150 FTG ET PE -4.3 35 20.0 0.0 21.5 0.0 0.005 TL 34.00 PV Pipe: 61 -71.0 2.705 PL 2.50 PP 0.0 59 10.0 0.0 26.0 0.0 4.0 120 FTG ---- PE 0.0 TR 10.0 0.0 26.0 0.0 0.013 TL 2.50 PV Pipe: 100 -71.0 2.705 PL 5.00 PP 0.2 TR 10.0 0.0 26.0 0.0 4.0 120 FTG E PE 2.2 PS 5.0 0.0 28.4 0.0 0.013 TL 14.36 PV Pipe: 101 -71.0 2.705 PL 4.00 PF 0.1 PS 5.0 0.0 28.4 0.0 4.0 120 FTG ---- PE 1.7 BR 1.0 0.0 30.2 0.0 0.013 TL 4.00 PV Pipe: 102 -71.0 2.705 PL 4.00 PP 0.2 BR 1.0 0.0 30.2 0.0 4.0 120 FTG E PE 1.7 Ui -3.0 0.0 32.1 0.0 0.013 TL 13.36 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 10/12/2018ARL5BAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.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: 103 -71.0 4.240 PL 162.00 PP 0.2 Ui -3.0 0.0 32.1 0.0 1.6 150 FTG 4E PE 0.4 U2 -4.0 0.0 32.7 0.0 0.001 TL 242.00 PV Pipe: 104 -71.0 4.220 PL 6.00 PP 0.0 U2 -4.0 0.0 32.7 0.0 1.6 140 FTC 2E PE -2.6 U3 2.0 0.0 30.2 0.0 0.001 TL 40.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 37.2 0.0 7.0 psi, 71.0 gpm U3 2.0 0.0 30.2 0.0 Pipe: 106 -71.0 4.220 PL 6.00 PP 0.0 U4 2.0 0.0 37.2 0.0 1.6 140 FTG 2E PE 2.6 US -4.0 0.0 39.8 0.0 0.001 TL 40.00 PV Pipe: 107 -71.0 4.220 PL 32.75 PP 0.1 US -4.0 0.0 39.8 0.0 1.6 140 FTG ET PE 0.0 SR -4.0 SRCE 39.9 (N/A) 0.001 TL 83.75 PV NOTES (HASS) Calculations were performed by the HASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.143 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 17.7 ft/sec at pipe 39. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.68 psi with a flow of 188.17 gpm. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page :0 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-2ND FLR.SDF JOB TITLE: (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP 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 C 45 El Tee RunT Kpig ChkVlv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.00 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.423 3.00 12.00 12.00 2.00 2.00 21.00 3.00 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 0.0) 1.654 4.56 9.12 2.28 10.26 6.84 1.14 11.40 9.12 0.01D 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 AimChk DPVlv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 P R E S S U R E IWI] 20.0 P S ± 10.0 0.0 -14.7 MCI 60.0 50.0 G A U G 40.0 E WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 10/12/2018ARL5BAD\FIRE SPRINKLERS\cALcS\INITIAL\11-pLEx-2NE FLP.SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ 0\\\ 50+ \\\\ I \\\\ I \\\\ I \\\ 45+ \\\\ I \\\\ \\\\ 40X \\\ * <-39.0 psl 6 6000 gprn Flow Test Pain: 35+ 30+ 25+ 20+ 15+ 10+ LEGEND tT X = Required Water Supply 39.93 psi @ 171.0 gpm 5+ I 0 = Available Water Supply I 51.68 psi @ 171.0 gpm I, 0++-+---+----+-----+------+---------+--------+----------+-----------+ 16002400 3200 4000 4800 5600 6400 7200 8000 FLOW (GPM) P R E S S U R E P S I RESIDENTIAL FIRE SYSTEMS, INC. 8085 EAST CRYSTAL DRIVE ANAHEIM, CA. 92807 HYDRAULIC CALCULATIONS FOR KENSINGTON 11-PLEX ATTIC IC HEADS FILE NUMBER: 12063 DATE: OCT 12, 2018 -DESIGN DATA- OCCUPANCY CLASSIFICATION: NFPA 13, LIGHT HAZARD DENSITY: 0.10 gpm/sq. ft. AREA OF APPLICATION: 1142.0 sq. ft. COVERAGE PER SPRINKLER: 148.0 sq. ft. NUMBER OF SPRINKLERS CALCULATED 9 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 146.5 gpm TOTAL WATER REQUIRED (including hose) : 246.5 gpm FLOW AND PRESSURE (8 BOR) : 146.5 gpm 8 29.1 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: RESIDENTIAL FIRE SYSTEMS DESIGN/LAYOUT BY: RUBI G. AUTHORITY HAVING JURISDICTION: CITY OF CARLSBAD CONTRACTOR CERTIFICATION NUMBER: 786965 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 38061304 HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\1-PLEX--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) SR 51.7 39.0 6000.0 51.7 246.5 40.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 246.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 146.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI (GPM) 1 32.0 K= 5.60 9.D 17.6 2 30.0 - - - - 11.3 - - - 3 30.0 - - - - 12.3 - - - 4 30.0 - - - - 13.2 - - - 5 30.0 - - - - 13.7 - - - 6 30.0 - - - - 11.3 - - - 7 30.0 - - - - 9.5 - - - 8 32.0 K= 5.60 8.3 16.1 9 30.0 - - - - 8.9 - - - 10 32.0 K= 5.60 7.8 15.6 11 30.0 - - - - 11.3 - - - 12 30.0 - - - - 9.5 - - - 13 32.0 K= 5.60 8.0 15.9 14 30.0 - - - - 8.5 - - - 15 32.0 K= 5.60 7.0 14.8 16 30.0 - - - - 11.L. - - - 17 30.0 - - - - 10.7 - - 18 30.0 - - - - 10. - - - 19 30.0 - - - - 10.6 - - - 20 32.0 K= 5.60 9. 17.1 21 30.0 - - - - 10.1 - - - 22 30.0 - - - - 10.1 - - 23 30.0 - - - - 9.9 - - - 24 32.0 K= 5.60 8.7 16.5 25 30.0 - - - - 9.9 - - 26 30.0 - - - - 12.0 - - - 27 30.0 - - - - 10.1 - - - 28 32.0 K= 5.60 8.9 16.7 29 30.0 - - - - 9.5 - - - 30 32.0 K= 5.60 8.3 16.1 31 30.0 - - - - 9.5 - - - 32 30.0 - - - - 12.8 - - - 33 30.0 - - - - 13.4 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 1O/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX- (ATTIC) .SDF JOB TITLE: NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 34 30.0 - - - - 14.1 - - - 35 20.0 - - - - 18.9 - - - 36 20.0 - - - - 18.7 - - - 37 20.0 - - - - 18.5 - - - 38 20.0 - - - - 18.5 - - - 39 20.0 - - - - 18.5 - - - 40 20.0 - - - - 18.5 - - - 41 20.0 - - - - 18.5 - - - 42 20.0 - - - - 18.5 - - - 43 20.0 - - - - 18.5 - - - 44 20.0 - - - - 18.5 - - - 45 20.0 - - - - 18.3 - - - 46 10.0 - - - - 22.8 - - - 47 10.0 - - - - 23.0 - - - 48 10.0 - - - - 23.0 - - - 49 10.0 - - - - 23.0 - - - 50 10.0 - - - - 23.0 - - - 51 10.0 - - - - 23.0 - - - 52 10.0 - - - - 23.0 - - - 53 10.0 - - - - 23.0 - - - 54 10.0 - - - 23.0 - - - 55 10.0 - - - - 23.0 - - - 56 10.0 - - - - 23.0 - - - 57 10.0 - - - - 23.0 - - - 58 10.0 - - - - 23.7 - - - 59 10.0 - - - - 24.1 - - - TR 10.0 - - - - 24.2 - - - ES 5.0 - - - - 27.1 - - - BR 1.0 - - - - 29.1 - - - Ui -3.0 - - - - 31.5 - - - U2 -4.0 - - - - 32.8 - - - U3 2.0 - - - - 30.4 - - - U4 2.0 - - - - 37.4 - - - US -4.0 - - - - 40.2 - - - SR -4.0 SOURCE 40.6 146.5 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX-(.AT?IC) .SDF JOB TITLE: PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGIHi, PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 -17.6 1.101 PL 2.00 PF 0.5 1 32.0 5.6 9.9 17.6 5.9 150 FTG E PE 0.9 2 30.0 0.0 11.3 0.0 0.054 TL 9.00 PV Pipe: 2 -17.6 1.101 PL 6.50 PF 1.0 2 30.0 0.0 11.3 0.0 5.9 150 FTG ET PE 0.0 3 30.0 0.0 12.3 0.0 0.054 TL 18.50 PV Pipe: 3 -62.5 1.598 PL 2.75 PP 1.0 3 30.0 0.0 12.3 0.0 10.0 150 FTG T PH 0.0 4 30.0 0.0 13.2 0.0 0.091 TL 10.75 PV Pipe: 4 -62.5 2.705 PL 16.00 PF 0.5 4 30.0 0.0 13.2 0.0 3.5 120 FTG ET PH 0.0 5 30.0 0.0 13.7 0.0 0.011 TL 44.08 PV Pipe: 5 44.8 1.598 PL 10.75 PP 0.9 3 30.0 0.0 12.3 0.0 7.2 150 FTG T FE 0.0 6 30.0 0.0 11.3 0.0 0.049 TL 18.75 PV Pipe: 6 31.7 1.101 PL 6.60 PP 1.9 6 30.0 0.0 11.3 0.0 10.7 150 FTG T PE 0.0 7 30.0 0.0 9.5 0.0 0.160 TL 11.60 PV Pipe: 7 16.1 1.101 PL 2.00 PF 0.3 7 30.0 0.0 9.5 0.0 5.4 150 FTG T PE -0.9 8 32.0 5.6 8.3 16.1 0.046 TL 7.00 PV Pipe: 8 15.6 1.101 PL 12.25 PP 0.5 7 30.0 0.0 9.5 0.0 5.3 150 FTG ---- PE 0.0 9 30.0 0.0 8.9 0.0 0.043 TL 1225 PV Pipe: 9 15.6 1.101 PL 2.00 PF 0.3 9 30.0 0.0 8.9 0.0 5.3 150 FTG T PE -0.9 10 32.0 5.6 7.8 15.6 0.043 TL 7.00 PV Pipe: 10 13.1 1.598 PL 10.25 PP J.1 6 30.0 0.0 11.3 0.0 2.1 150 FTG ---- PH J.0 11 30.0 0.0 11.3 0.0 0.005 TL 10.25 PV Pipe: 11 30.7 1.101 PL 6.60 PP 1.7 11 30.0 0.0 11.3 0.0 10.3 150 FTG T PE J.0 12 30.0 0.0 9.5 0.0 0.150 TL 11.60 PV Pipe: 12 15.9 1.101 PL 2.50 PP 0.6 12 30.0 0.0 9.5 0.0 5.3 150 FTG ET PE -0.9 13 32.0 5.6 8.0 15.9 0.044 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 10/12/2O18ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX- (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: 13 14.8 1.101 PL 13.25 PF 1.1 12 30.0 0.0 9.5 0.0 5.0 150 FTG 2E PE 0.0 14 30.0 0.0 8.5 0.0 0.039 TL 27.25 PV Pipe: 14 14.8 1.101 PL 2.00 PF 0.6 14 30.0 0.0 8.5 0.0 5.0 150 FTG 2E PE -0.9 15 32.0 5.6 7.0 14.8 0.039 TL 16.00 PV Pipe: 15 -17.6 1.598 PL 11.25 PF 0.1 11 30.0 0.0 11.3 0.0 2.8 150 FTG ---- PE 0.0 16 30.0 0.0 11.4 0.0 0.009 TL 11.25 PV Pipe: 16 33.7 1.394 PL 5.75 PF 0.7 16 30.0 0.0 11.4 0.0 7.1 150 FTG T PE 0.0 17 30.0 0.0 10.7 0.0 0.056 TL 11.75 PV Pipe: 17 0.0 1.101 PL 3.25 PF 0.0 17 30.0 0.0 10.7 0.0 0.0 150 FTG T PE 0.0 18 30.0 0.0 10.7 0.0 0.000 TL 8.25 PV Pipe: 18 33.7 1.101 PL 0.90 PF 0.2 17 30.0 0.0 10.7 0.0 11.3 150 FTG ---- PE 0.0 19 30.0 0.0 10.6 0.0 0.178 TL 0.90 PV Pipe: 19 17.1 1.101 PL 2.00 PF 0.4 19 30.0 0.0 10.6 0.0 5.8 150 FTG T PE -0.9 20 32.0 5.6 9.3 17.1 0.051 TL 7.00 PV Pipe: 20 16.5 1.101 PL 10.25 PF 0.5 19 30.0 0.0 10.6 0.0 5.6 150 FTC ---- PE 0.0 21 30.0 0.0 10.1 0.0 0.048 TL 10.25 PV Pipe: 21 0.0 1.101 PL 5.00 PF 0.0 21 30.0 0.0 10.1 0.0 0.0 150 FTG ET PE 0.0 22 30.0 0.0 10.1 0.0 0.000 TL 17.00 PV Pipe: 22 16.5 1.101 PL 2.60 PF 0.1 21 30.0 0.0 10.1 0.0 5.6 150 FTG ---- PE 0.0 23 30.0 0.0 9.9 0.0 0.048 TL 2.60 PV Pipe: 23 16.5 1.101 PL 2.00 PF 0.3 23 30.0 0.0 9.9 0.0 5.6 150 FTG T PE -0.9 24 32.0 5.6 8.7 16.5 0.048 TL 7.00 PV Pipe: 24 0.0 1.101 PL 10.50 PF 0.0 23 30.0 0.0 9.9 0.0 0.0 150 FTC 2E PE 0.0 25 30.0 0.0 9.9 0.0 0.000 TL 24.50 PV Pipe: 25 -51.2 1.598 PL 10.50 PF 0.7 16 30.0 0.0 11.4 0.0 8.2 150 FTC ---- PE 0.0 26 30.0 0.0 12.0 0.0 0.063 TL 10.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 10/12/2018ARLSBAD\RIRE SPRINKLERS\CALCS\INITIAL\11-PLEX- (ATTIC) .SDF JOB TITLE: PIPE TAG Q(:3PM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) .(R.T) SU11. NODES (FT) (K) (PSI) (GPM) FL/FT (PSU Pipe: 26 32.8 1.101 PL 6.60 SF 2.0 26 30.0 0.0 12.0 0.0 11.1 150 FTG 7 FE 0.0 27 30.0 0.0 10.1 0.0 0.170 TL 11.60 PV Pipe: 27 15.7 1.101 PL 2.00 PR 0.3 27 30.0 0.0 10.1 0.0 5.6 150 FTG '2 PE -0.9 28 32.0 5.6 8.9 16.7 0.049 TL 7.00 PV Pipe: 28 15.1 1.101 PL 12:75 PR 0.6 27 30.0 0.0 10.1 0.0 5.4 150 FTG ---- FE 0.0 29 30.0 0.0 9.5 0.0 0.046 TL 12.75 PV Pipe: 29 15.1 1.101 PL 2.00 PF 0.3 29 30.0 0.0 9.5 0.0 5.4 150 FTG '2 PE -0.9 30 32.0 5.6 8.3 16.1 0.046 TL 7.00 PV Pipe: 30 3.0 1.101 PL 3.50 PR 0.0 29 30.0 0.0 9.5 0.0 3.0 150 FTG 2E PE 0.0 31 30.0 0.0 9.5 0.0 0.000 TL 17.50 PV Pipe: 31 -83.0 2.705 PL 43.25 PF 0.8 26 30.0 0.0 12.0 0.0 4.7 120 FTG PE 0.0 32 30.0 0.0 12.8 0.0 0.018 TL 43.25 PV Pipe: 32 -84.0 2.705 PL 10.10 PR 0.5 32 30.0 0.0 12.8 0.0 3.7 120 FTG T PE 0.0 33 30.0 0.0 13.4 0.0 0.018 TL 28.82 PV Pipe: 33 -84.0 2.705 PL 20.60 PR 0.7 33 30.0 0.0 13.4 0.0 4.7 120 FTGl T PE 0.0 34 30.0 0.0 14.1 0.0 0.018 TL 39.32 PV Pipe: 34 -84.0 2.423 PL 10.00 PR 3.5 34 30.0 0.0 14.1 0.0 5.8 150 FTG E PE 4.3 35 20.0 0.0 18.9 0.0 0.021 TL 22.00 PV Pipe: 35 1.0 1.598 PL 28.50 PR 7.2 35 20.0 0.0 18.9 0.0 1.8 150 FTG 2T PE 3.0 36 20.0 0.0 18.7 0.0 0.004 TL 44.50 PV Pipe: 36 1.0 1.598 PL 56.33 PR 0.2 36 20.0 0.0 18.7 0.0 L.8 150 FTG T PE 0.0 37 20.0 0.0 18.5 0.0 0.004 TL 64.33 PV Pipe: 37 0.0 1.394 PL 9.25 PR 0.0 37 20.0 0.0 18.5 0.0 0.0 150 FTG T PE 0.0 38 20.0 0.0 18.5 0.0 0.000 TL 15.25 PV Pipe: 38 0.0 1.101 PL 8.25 PR 0.0 38 20.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 39 20.0 0.0 18.5 0.0 0.000 TL 20.25 PV • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 10/12/2018ARLSBAD\PIRE SPRINKLPRS\CALCS\INITIAL\11-PLEX- (ATTIC) .SDP JOB TITLE: PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VT-- ',FPS) HW(C) (PT) SUM. NODES (PT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 39 0.0 1.101 PL 3.00 PP 0.0 38 20.0 0.0 18.5 0.0 0.0 150 FTG ---- PE 0.0 40 20.0 0.0 18.5 0.0 0.000 TL 3.00 PV Pipe: 40 0.0 1.101 PL 0.50 PP 0.0 40 20.0 0.0 18.5 0.0 0.0 150 FTG ET PP 0.0 41 20.0 0.0 18.5 0.0 0.000 TL 12.50 PV Pipe: 41 0.0 1.101 PL 6.66 PP 0.0 40 20.0 0.0 18.5 0.0 0.0 150 FTG ---- PE 0.0 42 20.0 0.0 18.5 0.0 0.000 TL 6.66 PV Pipe: 42 0.0 1.101 PL 2.33 PP 0.0 42 20.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 43 20.0 0.0 18.5 0.0 0.000 TL 14.33 PV Pipe: 43 0.0 1.101 PL 10.50 PP 0.0 42 20.0 0.0 18.5 0.0 0.0 150 FTG ET PE 0.0 44 20.0 0.0 18.5 0.0 0.000 TL 22.50 PV Pipe: 44 11.0 1.598 PL 38.33 PP 0.2 37 20.0 0.0 18.5 0.0 1.8 150 FTG E PE 0.0 45 20.0 0.0 18.3 0.0 0.004 TL 47.33 PV Pipe: 45 62.5 2.423 PL 10.00 PP 0.3 45 20.0 0.0 18.3 0.0 4.3 150 FTG T PE -4.3 5 30.0 0.0 13.7 0.0 0.012 TL 22.00 PV Pipe: 46 -51.4 2.423 PL 10.00 PP 0.2 45 20.0 0.0 18.3 0.0 3.6 150 FTG T PP 4.3 46 10.0 0.0 22.8 0.0 0.008 TL 22.00 PV Pipe: 47 -51.4 2.705 PL 6.50 PP 0.2 46 10.0 0.0 22.8 0.0 2.9 120 FTG 2E PP 0.0 47 10.0 0.0 23.0 0.0 0.007 TL 25.22 PV Pipe: 48 0.0 1.654 PL 14.25 PP 0.0 47 10.0 0.0 23.0 0.0 0.0 120 FTG T PE 0.0 48 10.0 0.0 23.0 0.0 0.000 TL 23.37 PV Pipe: 49 0.0 1.654 PL 6.25 PP 0.0 48 10.0 0.0 23.0 0.0 0.0 120 FTG T PP 0.0 49 10.0 0.0 23.0 0.0 0.000 TL 15.37 PV Pipe: 50 0.0 1.083 PL 10.25 PP 0.0 49 10.0 0.0 23.0 0.0 0.0 120 FTG PT PP 0.0 50 10.0 0.0 23.0 0.0 0.000 TL 18.43 PV Pipe: 51 0.0 1.654 PL 2.75 PF 0.0 49 10.0 0.0 23.0 0.0 0.0 120 FTC ---- PP 0.0 51 10.0 0.0 23.0 0.0 0.000 TL 2.75 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-FLEX- (ATTIC) .SDF JOB TITLE: PIPE TAG Q(GPM) DIAIN) LENGTH PRE3S. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (P17) SiJ:J. NODES (PT) (K) (PSI) (GPM) FL/FT (PS) Pipe: 52 :0.0 1.083 PL 8.25 PF 0.0 51 10.0 0.0 23.0 0.0 0.0 120 FTG 2T PE 0.0 52 10.0 0.0 23.0 0.0 0.000 TL 19.93 PV Pipe: 53 0.0 1.654 PL 1.75 PP 0.0 51 10.0 0.0 23.0 0.0 0.0 120 FTG PE 0.0 53 10.0 0.0 23.0 0.0 0.000 TL 1.75 PV Pipe: 54 0.0 1.083 PL 8.75 PP 0.0 53 10.0 0.0 23.0 0.0 0.0 120 FTG E2T PE 0.0 54 10.0 0.0 23.0 0.0 0.000 TL 22.77 PV Pipe: 55 0.0 1.654 PL 8.00 PP 0.0 53 10.0 0.0 23.0 0.0 0.0 120 FTG ---- PE 0.0 55 10.0 0.0 23.0 0.0 0.000 TL 8.00 PV Pipe: 56 0.0 1.083 PL 7.50 PP 0.0 55 10.0 0.0 23.0 0.0 0.0 120 FTG E2T PE 0.0 56 10.0 0.0 23.0 0.0 0.000 TL 21.52 PV Pipe: 57 0.0 1.083 PL 3.90 PF 0.0 55 10.0 0.0 23.0 0.0 0.0 120 FTG ET PE 0.0 57 10.0 0.0 23.0 0.0 0.000 TL 12.08 PV Pipe: 58 -51.4 2.705 PL 90.00 PF 0.7 47 10.0 0.0 23.0 0.0 2.9 120 FTG ---- PP 0.0 58 10.0 0.0 23.7 0.0 0.007 TL 90.00 PV Pipe: 59 -51.4 2.705 PL 29.75 PP 0.4 58 10.0 0.0 23.7 0.0 2.9 120 FTG ET PE 0.0 59 10.0 0.0 24.1 0.0 0.007 TL 5.83 PV Pipe: 60 95.1 2.423 PL 10.00 PP 0.9 59 10.0 0.0 24.1 0.0 6.6 150 FTG ET PE -4.3 35 20.0 0.0 18.9 0.0 0.026 TL 34.00 PV Pipe: 61 -146.5 2.705 PL 2.50 PF 0.1 59 10.0 0.0 24.1 0.0 8.2 120 FTG ---- PE 0.0 TR 10.0 0.0 24.2 0.0 0.051 TL 2.50 PV Pipe: 100 -146.5 2.705 PL 5.00 PP 0.7 TR 10.0 0.0 24.2 0.0 8.2 120 FTG E PE 2.2 FS 5.0 0.0 27.1 0.0 0.051 TL 14.36 PV Pipe: 101 -146.5 2.705 PL i.00 PP 0.2 PS 5.0 0.0 27.1 0.0 8.2 120 FTG ---- PE 1.7 BR 1.0 0.0 29.1 0.0 0.051 TL 0.00 PV Pipe: 102 -146.5 2.705 PL 4.00 PF 0.7 BR 1.0 0.0 29.1 0.0 8.2 120 FTG E PE 1.7 Ui -3.0 0.0 31.5 0.0 0.051 TL 13.36 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE:'10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\ii-PLEX- (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: 103 -146.5 4.240 PL 162.00 PF 0.9 Ui -3.0 0.0 31.5 0.0 3.3 150 FTC 4E PE 0.4 U2 -4.0 0.0 32.8 0.0 0.004 TL 242.00 PV Pipe: 104 -146.5 4.220 FL 6.00 PF 0.2 U2 -4.0 0.0 32.8 0.0 3.4 140 FTG 2E PE -2.6 U3 2.0 0.0 30.4 0.0 0.004 TL 40.00 PV Pipe: 105 FIXED PRESSURE LOSS DEVICE U4 2.0 0.0 37.4 0.0 7.0 psi, 146.5 gpm U3 2.0 0.0 30.4 0.0 Pipe: 106 -146.5 4.220 PL 6.00 PF 0.2 U4 2.0 0.0 37.4 0.0 3.4 140 FTG 2E PE 2.6 U5 -4.0 0.0 40.2 0.0 0.004 TL 40.00 PV Pipe: 107 -146.5 4.220 PL 32.75 PF 0.4 U5 -4.0 0.0 40.2 0.0 3.4 140 FTG ET PE 0.0 SR -4.0 SRCE 40.6 (N/A) 0.004 TL 83.75 PV NOTES (HASS) Calculations were performed by the BASS 8.8 D computer program in accordance with NFPA13 (2016) 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 0.003 gpm and a maximum imbalance at any node of 0.188 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 11.3 ft/sec at pipe 18. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. Available pressure at source node SR under full flow conditions is 51.65 psi with a flow of 288.12 gpm. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-PLEX- (ATTIC) .SDF JOB TITLE: (6) PIPE FITTINGS TABLE User Pipe Table Name: STANDARD.PIP PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) S T L C B G N Eli Tee LngEli ChkViv BfyViv 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 C N Eli Tee LngEll ChkVlv BfyViv 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 ChkViv Gate 1.101 1.00 7.00 5.00 1.00 1.00 8.00 2.0J 1.394 2.00 8.00 6.00 1.00 1.00 11.00 3.00 1.598 2.00 9.00 8.00 1.00 1.00 14.00 3.00 2.423 3.00 12.00 12.00 2.00 2.00 21.00 3.00 PAGE: V MATERIAL: EdThrd HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkViv 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 LngEii ChkViv BfyViv GatVlv AlmChk DPVlv NPTee 2.705 9.36 18.72 6.24 21.84 10.92 1.56 15.60 15.60 18.72 P R E S S U R E 30.0 20.0 p S 10.0 0.0 -14.7 60.0 50.0 0 A U G 40.0 E WATER SUPPLY ANALYSIS Static: 51.70 psi Resid: 39.00 psi Flow: 6000.0 gpm FLOW (GPM) Note: (1) Dashed Lines indicate extrapolated values from Test Results (2) On Site pressures are based on hose stream deduction at the source SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 10/12/2018ARLSBAD\FIRE SPRINKLERS\CALCS\INITIAL\11-?LEX- 'ATTIC) .SDF JOB TITLE: WATER SUPPLY CURVE 60+ 55+ O\\\ 50+ \\\\ \\\\ I \\\\ 45+ \\\\ I \\\\ \\\\ P 40X R * <-39.0 psi 6 6000 gpm E I Flow Test Point S 5 35+ U I R I E 30+ P I S I I 25+ 20+ 15+ 10+ LEGEND X = Required Water Supply " I 40.57 psi @ 246.5 gpm 5+ I 0 = Available Water Supply I 51.67 psi @ 246.5 gpm I' 0++-+---+----+-----+------+--------+--------+---------------------+ 16002400 3200 4000 4800 5600 6400 720C 8000 FLOW (GPM) Model RFC30 & RFC30LL Model RFC43 & RFC43LL Model RFC49 & RFC49LL Model RFC58 5 Model RFC Cover Plate ModeIRFC76 Bulletin 006 September 2018 Reliable Model RFC Series Residential Sprinklers Flat Cover Plate, Concealed Pendent Sprinkler cULus Listed Features cULus Listed as Residential Sprinklers Push-On cover plate installation Low water flow requirements Product Description Model RFC Series residential sprinklers are flat cover plate, concealed pendent sprinklers intended for installation in accordance with NFPA 13, NFPA 13R, or NFPA 130. The sprinklers are cULus Listed as Residential Sprinklers in ac- cordance with UL 1626. In addition, Model RFCLL Series sprinklers are cULus Certified for Health Effects to NSF/ANSI standard 61 Annex G (LL). Model RFC30, RFC43, and RFC49 sprinklers have a 165°F (74°C) temperature rated fusible-link operating element. Model RFC58 and RFC76 sprinklers are offered with either a 165°F (74°C) or 2 12°F (100°C) temperature rated fusible-link operating element. Sprinklers with a 165°F (74°C) tempera- ture rating are ordinary temperature classification and are listed for use with a 135°F (57°C) temperature rated cover plate. Sprinklers with a 212°F (100°C) temperature rating are intermediate temperature classification and are listed for use with a 165°F (74°C) temperature rated cover plate. Model RFC Series sprinklers are installed with a Model RFC cover plate. Model RFC cover plates may be installed by ei- ther pushing or threading the cover plate into the sprinkler cup. Model RFC30, RFC30LL, RFC43, RFC43LL, RFC49 and RFC49LL sprinklers allow 1/2" (13 mm) of cover plate adjust- ment. Model RFC58 and RFC76 sprinklers allow 3/4(19 mm) of cover plate adjustment. Model RFC cover plates are avail- able in a variety of finishes as listed in Table H. Sprinkler Model Nominal K-Factor gpm/psi112 (l/min/bar1"2) Max. Coverage Area ft x ft (m x m) Sprinkler Identification Listings & Approvals Number (SIN) RFC30 3.0(43) 14 x 14 (4.3 x 4.3) cULus RA0611 RFC30LL 3.0(43) 14x 14(4.3x4.3) cULus, LL RA3211 RFC43 4.3(62) 20x20(6.1 x6.1) cULus RA0612 RFC43LL 4.3(62) 20x20(6.1 x6.1) cULus, LL RA3212 RFC49 4.9(71) 20x20(6.1 x6.1) cULus RA0616 RFC49LL 4.9(71) 20x20(6.1 x6.1) cULus, LL RA3216 RFC58 5.8(84) 20x20(6.1 x6.1) cULus RA0613 RFC76 7.6(109) 20 x 20 (6.1 x6.1) cULus RA0618 cULus: cULus Listed to UL1626, Residential Sprinklers for Fire Protection Service. LL: cULus Certified for Health Effects to NSF/ANSI Standard 61 Annex G (Less than 0.25% Lead content). www.reliablesprinkler.com Technical Specifications Style: Flat Concealed Pendent Threads: 1/2" NPT or ISO 7-1 R1/2 Nominal K-Factor: 3.0 (43 metric) Max. Working Pressure: 175 psi (12 bar) Mm. Spacing: 8 ft. (2.4 m) Material Specifications Thermal Sensor: Nickel Alloy Solder Link Sprinkler Body: Brass Alloy Levers: Bronze Alloy Yoke: Brass Alloy Sealing Assembly: Nickel Alloy with PTFE Load Screw: Bronze Alloy Towers: Copper Alloy Pins: Stainless Steel Deflector: Bronze Alloy Cup: Steel Cover Plate Finishes (See Table H) Sensitivity Fast-response Temperature Rating 165°F (74°C) sprinkler 135°F (57°C) cover plate Cover Plate Model RFC cover plate Sprinkler Wrench Model FC (without wrenchable cap) Model W3 (with wrenchable cap) I Listings and Approvals cULus Listed to UL 1626 cULus Certified for Health Effects to NSF/ANSI Standard 61 Annex C (RFC30LL only) Bottom View Model RFC30 & RFC30LL Sprinkler Components and Dimensions 2-5/16" (58 mm) Threads Da. Body — Cup — Tower -.... Fusible Link - Deflector (retracted) Pin (extended) - Deflector (extended) 1-3/4" (44 mm) +1-1/4° (6 mm) Nominal face of fitting to ceiling 13 r36" (5 mm) Model RFC Cover Plate 3-5/16" (84 mm) Die '— Ceiliig Model RFC30 and RFCOLL Rnrink1pr Hudrt i r flinn (ritr. PU ! Minimum Flow and Residual Pressure 0 Max. Coverage Area (2) Flow Pressure ft. xft. gpm . psi (m x m) (I/mm) (bar) 12x12 9.0 (3.6 x 3.6) (34) 1 . (0.62) 14x14 10 . 11.0 (4.3x4.3) (38) (0.76): Notes: - For NFPA 13 installations the flow per sprinkler rust be the greater of: (1) the flow listed in Table B abcve and (2) the flow required to achieve a minimum design density of 0.11 gpm/sq ft over the design area of the sprinkler. For coverage area dimensions less than those listed: above, use the minimum required flow for the nex larger max. coverage area listed. Bulletin 006 ., Page 2 of 8 - September 2018 a www.reliablesprinder.com Technical Specifications Style: Flat Concealed Pendent Threads: 1/2" NPT or ISO 7-1R1/2 Nominal K-Factor: 4.3 (62 metric) Max. Working Pressure: 175 psi (12 bar) Mm. Spacing: 8 ft. (2.4 m) Cover Plate Finishes (See Table H) Sensitivity Fast-response Temperature Rating 165°F (74°C) sprinkler 135°F (57°C) cover plate Cover Plate Model RFC cover plate Sprinkler Wrench Model FC (without wrenchable cap) Model W3 (with wrenchable cap) Listings and Approvals cULus Listed to UL 1626 cULus Certified for Health Effects to NSF/ANSI Standard 61 Annex G (RFC43LL only) Material Specifications Thermal Sensor: Nickel Alloy Solder Link Sprinkler Body: Brass Alloy Levers: Bronze Alloy Yoke: Brass Alloy Sealing Assembly: Nickel Alloy with PTFE Load Screw: Bronze Alloy Towers: Copper Alloy Pins: Stainless Steel Deflector: Bronze Alloy Cup: Steel Bottom View Model RFC43 & RFC43LL Sprinkler Components and Dimensions I nre; Body Cup Towe Fusible Li Deflector (retn Pin (extel Deflector (extend 1-3/4° (44 mm) +1- 1/4" (6 mm) Nominal face of fitting to ceiling 2-5/16" (58 mm) Dia. 00 \\\\\\\ 3/16(5mm) 1. Model RFC Cover Plate 3-5/16° (84 mm) Dia. Ceiling Model RFC43 & RFC43LL Sprinkler Hydraulic Design Criteria ii;ime] Minimum Flow and Residual Pressure Max. Coverage Area (2) Flow Pressure ft. x ft. gpm psi (m x m) (I/mm) (bar) 15x15 12 7.8 (4.6 x 4.6) (45) (0.54) 16x16 13 9.1 (4.9 x 4.9) (49) (0.63) 18x18 18 17.5 (5.5x5.5) (68) (1.21) 20x20 21 23.8 (6.1 x6.1) (79) (1.64) Notes: For NFPA 13 installations the flow per sprinkler must be the greater of: (1)the flow listed in Table C above and (2)the flow required to achieve a minimum design density of 0.1 gpm/sq ft over the design area of the sprinkler. For coverage area dimensions less than those listed above, use the minimum required flow for the next larger max. coverage area listed. Bulletin 006 Page 3 of 8 September 2018 fleliabiC www.reliablesprinkler.com Technical Specifications Style: Flat Concealed Pendent Threads: 1/2" NPT or ISO 7-1R1/2 Nominal K-Factor: 4.9 (71 metric) Max. Working Pressure: 175 psi (12 bar) Mm. Spacing: 8 ft. (2.4 m) Material Specifications Thermal Sensor: Nickel Alloy Solder Link Sprinkler Body: Brass Alloy Levers: Bronze Alloy Yoke: Brass Alloy Sealing Assembly: Nickel Alloy with PTFE Load Screw: Bronze Alloy Towers: Copper Alloy Pins: Stainless Steel Deflector: Bronze Alloy Cup: Steel Cover Plate Finishes (See Table H) Sensitivity Fast-response Temperature Rating 165°F (74°C) sprinkler 135°F (57°C) cover plate Cover Plate Model RFC cover plate Sprinkler Wrench Model FC (without wrenchable cap) Model W3 (with wrenchable cap) Bottom View Listings and Approvals cULus Listed to UL 1626 cULus Certified for HealtV Effects to NSF,'ANS. Standard 61 Annex G (RFC49LL only) Model RFC49 & RFC49LL Sprinkler Components and Dimensions - Threads 2-516(58 mm) Dia. Body Cup Tower .-. Fusible Link - Deflector (retracted) Pin (extended) Deflector (extended) - 1-34" (44 mm) +1- 1/4° (6 mm) Noninal face of fitting to ceiling Model RFC Cover Plate 3-5/,!61.1 (84 mm) Dia (5 mm) Ceilg Model RFC49 & RFC49LL Sprinkler Hydraulic Design Criteria Minimum Flow and Residual Pressure (1) Max. Coverage Area (2) Flow Pressure ft. xft. gpm psi (m x m) . (I/mm) (bar) 16x16 13 7.0 (4.9 x 4.9) (49.0) (0.48) 18x18 17 - 12.0 (5.5 x 5.5) (64.3) . (0.631 20x20 20 16.7 (6.1x6.1) .. (75.7) (1.1: Notes: For NFPA 13 installations the flow per spinkler must be the greater of: (1)the flow listed in Table D aoove and (2)the flow required to achieve a minimum design density of 0.1 gpm/sq f! over the design area of the spr nkler. For coverage area dimensions less than those listed above, use the minimum requred flow for the next larger max. coverage area listed. Bulletin 006 Page 4 of 8 September 2018 Rellabld , wi.reliablesprirkler.com Technical Specifications Cover Plate Finishes Style: Flat Concealed Pendent (See Table H) Threads: 1/2" NPT or ISO 7-1 R1/2 Nominal K-Factor: 5.8 (84 metric) Sensitivity Max. Working Pressure: 175 psi (12 bar) Fast-response Mm. Spacing: 8 ft. (2.4 m) Temperature Ratings 1 Material Specifications Ordinary: Thermal Sensor: Nickel Alloy Solder Link 165°F (74°C) sprinkler Sprinkler Body: Brass Alloy 135°F (57°C) cover plate Levers: Bronze Alloy Intermediate: Yoke: Brass Alloy 212°F (100°C) sprinkler Sealing Assembly: Nickel Alloy with PTFE 165°F (74°C) cover plate Load Screw: Bronze Alloy Towers: Copper Alloy Cover Plate Pins: Stainless Steel Model RFC Cover Plate Deflector: Chrome Plated Bronze Alloy Cup: Steel Sprinkler Wrench Bottom View Model FC Listings and Approvals cULus Listed Model RFC58 Sprinkler Components and Dimensions 2-5/16' (58 mm) Dia. Threads Body Cup Tower al face Deflector (retracted) Nomino fitting to ceiling ____ Pin (extended) Deflector (extended) H 3/16" (5 mm) Model RFC Cover Plate -' - 3-5/16" (84 mm) Dia. Ceiling Model RFC58 Sprinkler Hydraulic Design Criteria Minimum Flow and Residual Pressuret1 Max. Coverage Area (2) Flow Pressure ft. x ft gpm psi (m x m) (I/mm) (bar) 16x16 16 7.6 (4.9 x 4.9) (60.6) (0.53) 18x18 18 9.6 (5.5x5.5) (68.1) (0.66) 20x20 20 11.9 (6.1 x6.1) (75.7) (0.82) Notes: For NFPA 13 installations the flow per sprinkler must be the greater of: (1)the flow listed in Table E above and (2)the flow required to achieve a minimum design density of 0.1 gpm/sq ft over the design area of the sprinkler. For coverage area dimensions less than those listed above, use the minimum required flow for the next larger max. coverage area listed. Bulletin 006 Page 5 of 8 September 2018 Reliable www.reliablesprinkler.com Nominal face of filirg to ceiling \\\\\\\ \\\\\\\ 1-7/8' (48 mm) +,'- 3/8' 9 mm) Technical Specifications Cover Plate Finishes Style: Flat Concealed Pendent (See Table H) Threads: 3/4" NPT or ISO 7-1 R3/4 Nominal K-Factor: 7.6 (109 metric) Sensitivity Max. Working Pressure: 175 psi (12 bar) Fast-response Mm. Spacing: 8 ft. (2.4 m) Temperature Ratings Material Specifications Ordinary: Thermal Sensor: Nickel Alloy Solder Link 165°F (74°C) sprinkler Sprinkler Body: Brass Alloy 135°F (57°C) cover plate Levers: Bronze Alloy Intermediate: Yoke: Brass Alloy 212°F (100°C) sprinkler Sealing Assembly: Nickel Alloy with PTFE 165°F (74°C) cover plate Load Screw: Bronze Alloy Towers: Copper Alloy Cover Plate . Pins: Stainless Steel Model RFC Cover Rate Deflector: Bronze Alloy Cup: Steel Sprinkler Wrench Model FC Bottom View Listings and Approvals cULus Listed Model RFC76 Sprinkler Components and Dimensions 2-5/16" (58 mm) Dia. Threads Body 11, Cup Towei Fusible Li Deflector (retra Pin (exten Deflector (extend Model RFC Cover Rate - H 3-5/16(84 mm) Dia. r-3/165mm) Ceiling Model RFC76 Flat Concealed Sprinkler Hydraulic Design Criteria Minimum Flow and Residual Pressuret1 Max. Coverage Area )2( Flow - Pressure ft. xft. gpm psi (m x m) (I/mm) (bar) 16x16 - 21 7.6 (4.9 x 4.9) (79.5) (0.52) 18x18 24 9.9 (5.5 x 5.5) - 90.8) - (0.68) 20x20 34 20 (6.1x6.1) (128.7) (1.4) Notes: For NFPA 13 installations tl-e flow per sprinkler must be the greate of: (1)the flow listed in Table E above and (2 the flow required to achieve a minimum design density of 0.1 gprn!sq ft over the design area of the sprinkler. For coverage area dimensins less than those listed above, use tte minimum required flow for the next larger Max. coverage area listec Bulletin 006 Fage 6 of B September 2018 IeIiabIe www.reliablesprinkler.ccm Cover Plate Finishes(') Standard Finishes Special Application Finishes White Polyester Off White Paint Black Paint Raw Brass Chrome Plated Bright Brass Finished Bronze Black Plated Satin Chrome Stainless Steel Clad(3) Custom Color Paint(2) Notes: I I I 1 Paint or any other coating applied over the factory finish will void all approvals and warranties. Custom color paint is semi-gloss, unless specified otherwise. Stainless steel clad cover plates are Type 316 Stainless Steel on the finished side and C102 Copper Allow on the backside. Cover plates are not listed or approved as corrosion resistant. Stainless steel clad cover plates are not available perforated. Installation Dimensions Recommended Mm. to Mm. to Max. Cover Cover Plate Hole Diameter Cover Plate Max. Face Dropped Deflector Cover Plate Sprinkler Plate Diameter in Ceiling Adjustment of Fitting to Distance below Temperature Model Model inch inch inch CeiIing1 Ceiling Rating (mm) (mm) (mm) inch inch (mm) (mm) RFC3O, RFC3OLL, RFC431 RFC 3-5/16 2-5/8 1/2 1-1/2 to 2 1/2 to 1 135°F RFC43LL, (84) (67) (13) (38t051) (13t025) (57°C) RFC49, RFC49LL 135°F2 RFC58, 3-5/16 2-5/8 3/4 1-1/2 to 2-1/4 1/4 to 1 (57°C) RFC76 RFC (84) (67) (19) (38 to 57) (6 to 25) or 165°3) F (74°C) Notes: Face of fitting to ceiling dimensions are based on a nominal thread make up. Verify dimensions based on fitting and thread sealing method prior to installation. A 1/2" x 1/2" brass nipple extension (Reliable PIN 6999991900) is available where necessary for replacement of existing sprinklers. For use with 165°F (74°C) temperature rated sprinklers where the Maximum Ceiling Temperature does not exceed 100°F (38°C). For use with 212°F (100°C) temperature rated sprinklers with the Maximum Ceiling Temperature does not exceed 150°F (66°C). Installation Model RFC series sprinklers are intended to be installed in ac- cordance with NFPA 13, NFPA 13R, or NFPA 13D, as well as the requirements of applicable authorities having jurisdiction. Mod- el RFC series sprinklers must not be installed in ceilings with positive pressure in the space above. Ensure that the 4 slots in the cup are open and unobstructed following installation. Model RFC series sprinklers are shipped with a protective cap that should remain on the sprinkler until installed. The protective cap should be replaced following installation of the sprinkler and permanently removed only when the cover plate is installed and the sprinkler system is placed in service following construction. Model RFC series sprinklers are installed with the Model FC wrench. The use of any other wrench to installed Model RFC se- ries sprinklers is not permitted and may damage the sprinkler. Temporarily remove the protective cap during installation of the sprinkler. Insert the Model FC wrench over the sprinkler until the wrench engages the body. Do not wrench any other part of the sprinkler/cup assembly. The Model FC wrench is designed to be turned with a standard 1/2" square drive. Tighten the sprin- kler into the fitting after applying a PTFE based thread sealant to the sprinkler's threads. Recommended installation torque is 8 to 18 ft-lbs (11 to 24 N-m) for 1/2" thread sprinklers and 14 to 20 ft-lbs (19 to 27 N-m) for 3/4" thread sprinklers. Do not exceed the maximum recommended torque. Exceeding the maximum recommended torque may cause leakage or im- pairment of the sprinkler. Use care when inserting or removing the wrench from the sprinkler to avoid damage to the sprinkler. Install the cover plate by hand by pushing the cover plate into the cup and turning the cover in the clockwise direction until it is tight against the ceiling. Application Model RFC series sprinklers are intended for installation where residential sprinklers are permitted or required by NFPA 13, NFPA 13R, and NFPA 13D. The sprinklers are concealed pen- dent residential sprinklers. Model RFC 30, RFC30LL, RFC43, RFC43LL, RFC49 and RFC49 LL sprinklers are available in ordinary temperature classifica- tion for installation where the Maximum Ceiling Temperature does not exceed 100°F (38°C). Model RFC58 and RFC76 sprin- klers are available in either ordinary or intermediate tempera- ture classification for installation where the Maximum Ceiling Temperature does not exceed 100°F (38°C) or 150°F (66°C), respectively. Bulletin 006 Page 7 of 8 September 2018 www.reliablesprinkler.com ':4 (0 (0 (0 (0 0 r') 0) Model FC For use with Models RFC30, RFC43, and RFC 49 without wrenchable cap and Models RFC58 and RFC76 Maintenance Model RFC series sprinklers should be inspected and the sprinkler system maintained in accordance with NFPA 25, Do not clean sprinklers with soap and water, ammonia or any other cleaning fluids. Remove dust by gentle vacuuming. Replace any sprinkler cover plate assembly which has been painted (other than factory applied) or damaged in any way. A stock of spare sprinklers should be maintained to allow quick replace- ment of damaged or operated sprinklers. Prior to installation, sprinklers should be maintained in the original cartons and packaging Lntil used to minimize the potential for damage to sprinklers that would cause improper operation or non-oper- ation. Listings and Approvals Listed by Urderwriters Laboratories, Inc. and UL Certified for Canada to UL1626, Residential Sprinklers for Fire-protection Service (cULus). Certified by Underwriters Laboratories, Inc. and Underwriters Laboratories of Canada for Health Effects to NSF/ANSI Standard 61 Annex G (LL) (RFC30LL, RFC43LL, and RFC49L_ only). Model W3 For use with Mcdels RFC30, RFC43, and RFC49 with wrenchetle cap Guarantee For the Reliable Auto-natic Sprinkler Co. Inc. gLarantee, terms, and conditions, visit www.rehablesprinkler.com. Patents Model RFCSU, RFC:30LL, RC43, RFC43LL, RFC49, RFC49LL, RFC58, and RFC76 sprinklers are covered by U.S. Patent No. 9,248,327 and U.S. Patent io 7,275,60:3. Model RFC3, RFC:30LL, R7-C43 and RFC43LL sprinklers are additionally covered ay U.S. lPatent No. 3,776,9J3. Ordering Information Specify the following when orcering. Sprinkler Model (RFC30, 3FC30LL, RFC43, RFC43LL, RFC49, RFC49LL, RFC58, RFC76) Temperature Ra:ing Cover Plate Model RFC TemperatLre Raing Fnish (See Table H) Sprinkler Wrench Model FC FvodelW3 Bulletin 006 September 2018 Page 8of8 www.reliablesprinkler.com SERIES GL-RES RESIDENTIAL RECESSED PENDENT _ri !jtr FIRE SPRINKLER CORPORATION RESIDENTIAL A U TOMA TI C SPRINKLERS GL4II0 & GL4910 PENDENT RECESSED PENDENT DESCRIPTION AND OPERATION The Globe GL4I10 and GL4910 Residential Sprinklers have a low profile yet durable design which utilize a 3mm frangible glass ampule as the thermosensitive element. They feature economy, aesthetics and low flow. The combination of the 3mm frangible glass ampule and special- ly designed deflector make the GL4110 and GL4910 Residential Sprinklers the ultimate in life safety and fire control. These Globe Pendent and Recessed Pendent Residential Sprinklers have met the strict requirements of Underwriters Laboratories Inc. as de- scribed in the UL Standard for Residential Sprinklers for Fire Pro- tection Service, UL 1626, and should be used accordingly. These sprinklers should also be installed in accordance with the appropri- ate NFPA Standard 13, 13D or 13R and under the direction of the approving authorities having jurisdiction. The heart of Globe's GL4110 and GL4910 sprinklers proven ac- tuating assembly is a hermetically sealed frangible glass ampule that contains a precisely measured amount of fluid. When heat is absorbed, the liquid within the bulb expands increasing the inter- nal pressure. At the prescribed temperature the internal pressure within the ampule exceeds the strength of the glass causing the glass to shatter. This results in water discharge which is distributed in an approved pattern. The sprinkler and escutcheon are not factory assembled. Assembly is done in the field. TECHNICAL DATA See reverse side for Approvals and Specifications. Temperature Rating - 155°F (68°C), 175°F (79°C) Water Working Pressure Rating -175 psi (12 Bars) Factory tested hydrostatically to 500 psi (34 Bars) Maximum low temperature glass bulb rating is -67°F (-55°C) Frame - bronze Deflector - brass • Screw - brass Bulb seat - copper. Spring - nickel alloy• Seal - teflon Bulb - glass with alcohol based solution, 3mm size Escutcheon Assembly - steel SERIES GL-RES RESIDENTIAL PENDENT *SPRINKLER TEMPERATURE RATING/CLASSIFICATION and COLOR CODING AVAILABLE SPRINKLER N.F.P.A. MAXIMUM CEILING CLASSIFICATION TEMPERATURES BULB COLOR - TEMPERATURE ORDINARY 3°C RED 10flF INTERMEDIATE 1 9°C YELLOW 1.OF DEC 2017 GFS-310 (Formerly A-11) RESIDENTIAL A UTOMA TIC SPRINKLERS GL4II0 & GL4910 PENDENT • RECESSED PENDENT SPECIFICATIONS A ND APPROVALS SIN NOMINAL THREAD LENGTH FINISHES cLL.js NYC - DOB "K" FACTOR SIZE EL MEA 101-92-E GL4110 4.1 (58 metric) Factory Bronze 1/2"NPT 21/2" Chnme GL4910 4.9 (68 metric) (15mm) (6.4crr) White Polyester x Black PcIyester12 NOTE: METRIC CONVERSIONS ARE APPROXIMATE. 'FINISHES AVAILABLE ON SPECIAL ORDER. 'AVAILABLE AS cULus LISTED CORROSION RESISTANT WHEN SPECFIED ON ORDER. INSTALLATION DATA FOR FLAT AND SLOPED CEILINGS** TEMPERATURE MAX. AREA * MIN. DISTANCE SIN STYLE OF COVERAGE3 *MIN. PRESSURE MIN. FLOW BETWEEN 155°F 175°F (68°C) (79°C) VflDHxLENGTH Fee: (Meters) P.S. !. (bars G PM. (L/min.) SPRINKLERS Feet (Meters) X X 12 (3.7) x 12 (3.7): 7.2 (.50) 11(42) GL4110 PENDENT RECESSED PENDENT 8(2.4) x 14(4.3) x 14 (4.3)' 8.6 (.59) 12(45) X X 15(4.9) x 16(4.9) 11.7 (.81) 14 (53.) X X 1.2 37) x 12 (3.7) 7.0 (.48) 13(49) X X 14(43)> 14 (4.3) 8.2 (.57) (5.3) GL4910 PENDENT RECESSED PENDENT 8(2.4) X X 13(4.9)x16(4.9) 8.2(57) '.(53) X X 13(5.5)>. .8 (5.5) 2.0 (.83) 7 64) X X 20 (3.1) > 20(6.1) 13.7(l.15) 2076) NOTE: METRIC CONVERSIONS ARE APPROXIMATE. *WHEN THESE SPRINKLERS ARE USED IN NFPA 13 SYSTEMS, A 0.1 DESIGN DENSITY MINIMUM SHALL BE UTIL IZEE'. **REFER TO PAGE 2 OF GLOBE'S RESIDENTIAL SPRINKLER INSTALLATION G'JIDEBULLETIN RS.I.G.) FOR NFFA 13D AND 13R REQUIREMENTS. 'FOR COVERAGE AREA DIMENSIONS LESS THAN OR BETWEEN THOSE INDCAE:D, USE THE MINIMUM REQUED FLOW FOR THE NEXT HIGHEST COVERAGE AREA FOR WHICH HYDRAULIC DESIGN CRITERIAARE STATED. CROSS SECTION -2 15/16 NA. - 2" MIN. DIA. HOLE IN CEILING 129/32' DLA.- 1" x 1/2" REDUCER 1/8" MIN. 5/8" MAX. 1" MIN. 11/2" MAX. 1/2" ADJUSTMENT RECESSED PENDENT 0&6mm FIRE SPRINKLER CORPORATION ORDERING INFORMATION SPECIFY Quantity SIN Style 'Orifice Temperature• Finishes desired Quantity - Wrenches - P/N 325390 Quantity - Recessed Wrenches - P/N 325391 Quantity - Protective Caps - P/N 327109-CAP (Friction Fit Recessed) GLOBE® PRODUCT WARRANTY G,ote agrees to repair or replace any of its own manufactured products found to be defective in material or workmanship for a period cf one year from date of sipmeDt. For specific details of our warranty lease refer to Price List Te-ms and Conditions of Sale (Our Price List). 4077AIRPARK DRIVE, STANDISH, MICHIGAN 48658 989-846-4583 FAX 989-846-9231 1-800-248-0278 www.ctobesprinkIer.com PRINTED L.S.A. GFS-310 (Formerly A-I) DEC 2017 IF ~`~km W' 4077 Airpark Dr. Standish, Ml 48658 • 989-846-4583 . www.globesprinkler.com FIRE SPRINKLER CORPORATION Technical Support. 989-414-2600. techservice@globesprinkIer.com SPECIFIC APPLICATION MODEL "IC" INTERSTITIAL COMBUSTIBLE CONCEALED SPACE UPRIGHT SPRINKLER GL5608 GENERAL DESCRIPTION The Globe Series GL-SS/IC GL5608 Interstitial Combustible Space Sprinkler is a quick response, upright, specific appli- cation sprinkler designed to provide protection of light haz- ard combustible and non-combustible concealed spaces, inclusive of interstitial (between floors) or attic spaces (with slopes 2:12 or less). Each GL5608 sprinkler can be de- signed for up to 16ft x 16ft (4.9m x 4.9m) spacing, providing as much as 256 ft2 (23.8m2) of protection per sprinkler. The GL5608 sprinkler meets the requirements of Under- writers Laboratories UL 199H to comply with criteria for the protection of combustible concealed spaces as described in - NFPA 13. When heat is absorbed, liquid within the glass bulb ex- pands, increasing the internal pressure. At the prescribed temperature the internal pressure within the ampule ex- ceeds the strength of the glass causing the glass to shatter. This results in water discharge which is distributed in an ap- proved pattern. APPLICATION The GL-SS/IC GL5608 can be designed for installation in CPVC wet pipe sprinkler systems and steel wet pipe or dry pipe sprinkler systems. The GL5608 can be used in concealed spaces having roof pitch of 2 in 12 or less con- structed of wood truss, non-combustible bar joist, solid wood joists, or composite wood joists. The specific design requirements for each type of piping system, and construc- tion materials can be found in the following sections of this document. NFPA 13 REQUIREMENTS Sprinklers shall be Listed for use in combustible concealed spaces (with a slope not exceeding 2 in 12) with combus- tible wood truss, wood joist construction, or bar joist con- struction having a combustible upper surface and where the depth of the space is less than 36" (914.4mm) from deck to deck or with double wood joist and composite wood joist construction with a maximum of 36" (914.4mm) between the top of the bottom joist and the bottom of the upper joist. HYDRAULIC DESIGN AREA For all pipe and construction types the design area shall be 1000 ft2 (92.9m2) except for Steel Pipe Systems with insula- tion filled joists, the design area shall be in accordance with the Light Hazard Systems requirements of NFPA 13. SPRINKLER CO VERA GE AREA The coverage area of any single GL-SS/IC Sprinkler shall utilize the SxL rule for all sprinkler spacings (i.e. 16 x 10 = 160 sq. ft. XO.10= 16gpm). GL5608 SERIES GL-SS/IC UPRIGHT SPRINKLER: The Globe GL-SS/IC GL5608 Interstitial Combustible Up- right Sprinkler has been Listed to be used beyond the 36" (914.4mm) height to a height of 60" (1.5m) to provide more functionality in installation specifically in areas where the height of the concealed space is both above and below the height of 36" (914.4mm). TECHNICAL DATA cULus Listed for coverage areas up to 256 ft2 (23.8 m2) 16ft(4.9 m) maximum and 6 ft (1.8 m) minimum Sprinkler Spacing Maximum Open Space Height 60 in (1.5 m) Temperature Ratings - 175°F (79°C), 200°F (93°C) Finish - Factory Bronze Water Working Pressure Rating -175 psi (12 Bars) Maximum low temperature glass bulb rating -67°F (-55°C) Materials of Construction, Frame - bronze, Deflector - brass, Screw - brass, Bulb seat - copper, Spring - nickel alloy, Seal - teflon, Bulb - glass with alcohol based solution, 3mm size NOV 2018 GFS-600 (Formerly A-40) Page 1 of 6 TABLE A GENERAL INSTALLATION ALLOWANCES STEEL PIPING CPVC PIPING COVERAGE DISTANCE OPEN SPACE HEIGHT TOTAL OPEN SPACE HEIGHT TOTAL CONSTRUCTION TYPE :ALLOWED ALLOWED AREA BETWEEN SPRINKLERS MINIMUM MAXIMUM SPACE HEIGHT MINIMUM MAXIMUM SPACE HEIGHT'- Feet2 (Met9rs2.) Inches (mm) 'Inches (mm) Inches (mm Inches(nm, lnchesmm) :nches (mm) Unobstructed Wood Truss 6(152) 60(1524) 60(1524) 6(152) 60(1524) 60(1524) 6 (1.8) Non-Combustible Bar Joist 256 (78.0) MINIMUM Obstructed Wood Truss 6(152) 60(1524) 84(2134) N/A N/A N/A MAXIMUM 16(49) Solid Wood Joist 72 (1829) MAXIMUM Insulation Filled Joist 6(152) 60 (1524) 1 72 (1829)2 6 (152) 6-)(1524) NOTE: METRIC CONVERSIONS ARE APPROXIMATE. i WHEN TRUSS OR JOIST SPACE IS NONINSULATION FILLED, THE MAXIMUM ALLOWED TOP MEMBER DEPTH IS i2"(305 mm). 2 UP TO 12' (305mm) LOWER MEMBER SPACE. TABLE B SPRINKLER SPECIFICATION AND APPROVALS STYLE SIN MODEL NOMINAL "K" HAZARD' THREAD IZE SPRINKLER ruin FINISH TEMPERATURE RATING ' PRESSURE MAX. LOW TEMP. BULB cULus FACTOR 175F 200°F RATING RATING (79-C) (93-C) UPRIGHT GL5608 5.6 _F LH 1/2" NPT 21/4" Factory x x 175 psi -67°F x (80 metric) (15mm) (5.7cm) Bronze (12 Bars) (-55°C) NOTE: Y METRIC CONVERSIONS ARE APPROXIMATE. 2 SPRINKLERS SHALL BE LIMITED AS PER THE REQUIREMENTS OF NFPAI3 AND ANY OTHER RELATED DOCUMENTS. OBSTRUCTION CRITERIA For systems where the Globe "IC" Upright Sprinklers are positioned with 15' (4.6m) or less between sprinklers the Globe "IC" Upright Sprinkler must use the obstruction re- quirements for standard spray upright sprinklers. For systems where the Globe "IC" Upright Sprinklers are positioned with greater than 15' (4.6m) between sprinklers the Globe "IC' Upright Sprinkler must use the obs:ruction requirements for extended coverage upright sprinklers. NOTE: WEB MEMBERS AND GUSSETS SHALL NOT BE CCNSIDEED OB- STRUCTIONS PROVIDED THE MINIMUM 4-1/2 INCH LATERAL DISTANCE REQUIRED BY THE SPECIFIC APPLICATION LISTING/S MAINTAINED. CPVC DESIGN REQUIREMENTS SYSTEM TYPE PARTITION REQUIREMENTS The concealed space being protected must be broken up Wet pipe system. into areas no greater than 1000 square feet either by full height walls rr hv draft curtains ALLOWABLE CONSTRUCTIO TYPES Unobstructed wood truss construction' Unobstructed bar joist construction' Non-combustible insulation filled solid wood joist construction' Non-combustible insulation filled composite wood joist construction N ... DRAFT CURTAINS When draft curtains are used they must he 8" (203.2mm) in height or one third of the depti of the concealed space, whichever is greater. Draft curtains must be constructed of a material that will not allow for heat to escape through or above them. NOTE: i Upper joist/truss cannot be more than 4' (101.6mm) in height. 2 The joist space in non-combustible insulation filled joist coistruction must be completely filled with noncombustible insulation and secured in place by metal wire netting to hold the insulation in place in the event of a/ire. NOV 2018 GFS-600 (Formerly A-40) Page 2 of 6 DEFLECTOR POSITION 1 1/2 to 4 inches below the upper deck for wood truss and bar joist constructions. 1 1/2 to 4 inches below the joists for non-combustible insulation filled solid and composite wood joist constructions. 4 1/2 inches away from trusses. CONCEALED SPACE SIZE All spaces must have a minimum open space (from top of lower joist, cord, or truss to bottom of upper joist, cord, or truss) of 6" (152.4mm). (see Figures 1 and 2) Unobstructed wood truss and bar joist construction must not have a total bottom of floor to top of ceiling space height of more than 60" (1.5m). (see Figure 2) Joist construction with noncombustible insulation in the upper deck must not have an open space (from top of lower joist to bottom of upper joist) of greater than 60 inches in size. They must not have a total concealed space height of greater than 72" (1.8m). This allows for a maximum lower joist space of 12" (304.8mm). Solid wood joist and obstructed truss construction must not have an open space (from top of lower joist or truss to bottom of upper joist or truss) of greater than 60"(1.5m) in size. They must not have a total concealed space height of greater than 84"(2.1 m). The upper joist space must not be greater than 12(304.8mm) in depth (see Figure 2) CPVC PIPE INSTALLATION Horizontal runs of CPVC piping must be located with the bottom of the piping not more than 6" (152.4mm) above the ceiling below or above ceiling insulation (if present), or one third depth of the combustible concealed space as mea- sured between the top surface of the ceiling below to the bottom of the floor above or the bottom of the noncombus- tible insulation above. Whichever is smaller. When the lower joists are greater than 6(152.4mm) in height, CPVC piping is permitted to be attached directly to the top of the joist. The CPVC piping can be used to supply the Globe "IC" Upright Sprinklers as well as the sprinklers protecting the space below. When using 1" (DN25) or larger pipe, a hanger must be located at the truss nearest a sprig for purposes of re- straint. If using %" (DN19) piping, all sprigs over 12" (304.8mm) must be laterally braced using methods described in the NFPA standards. Where CPVC piping must be offset to go over an obstruction that will violate the hori- zontal positioning requirements the CPVC piping must be spaced not greater than 6 inches from that obstruction and an additional Globe IC Upright Sprinkler must be provided to protect the section of CPVC piping (see Figure 1 and 2). CPVC piping must be kept a minimum of 18" (457.2mm) lat- erally away from heat sources such as heat pumps, fan mo- tors, and heat lamps. l/2(114mm)MIN. 11 (38rmo) MIN. TO FACE OF WOOD TRUSS 4" (102mm) MAX. 7 OR TOP CHORD OF BAR JOIST 6" (152mm) MAX. FOR CFVC P1PE1 ,—UPPER DECK AE ARMS MUST BE ALLED IN-LINE I PIPE RUN "(125mm) MAX. 6FOR —GL5608 CPVC PIPE (MODEL IC 6" (152 m) MIN. 3C 3C 3C 3C —OBSTRUCTION 0 0 0 0 I l0)t°-I1°Jt° F PIPE/ rCE1L1NGB0TTOM0 TOP OF CORD CEILING TO BOTTOM OF PIPE CEILING INSULATION, OR 1/3 THE DEPTH OF CONCEALED SPACE (AS MEASURED FROM TOP SURFACE OF CEILING TO BOTTOM SURFACE OF DECK), OR WHICH EVER IS SMALLER. FIGURE 1: CPVC PIPE UNOBSTRUCTED WOOD TRUSS AND BAR JOIST CONSTRUCTION NOV 2018 GFS-600 (Formerly A-40) Page 3 of 6 12 60" INSULATION MUST BE HELD —+JCN-COMELJSTIBLE SCLID WOOD JO/ST IN RACE WIT METAL. / / COMPCSITE WOOD JOIST 12' 305mm) lAX. DEPTH WIRE NETTING / / 12" (3E5mm/ MAX. DEPTH N— DECK TCPCHORD 1 12 (305mm) MAX. £ EPTH /2" (38mm) MIN 4(102mri) MAX. GLEBOB H l-.---6"(152mr)MAX. (MODEL IC SPRI ' I FOR CPVC FRAM SARMS MUST cl-101---I-lf-\ —6" (152mm) MAX. BE INSTP&LED I -----t-'—r ____ FOR CPVC I 'IN-LINE WITH PIPE RU' I 7 . I I 6(1E2mmMIN. I I i ..p LJ_OBSTRUCTIJN Il829Sm) 3 C3 ± I1D *13 £3 ] ' CEILING 3C 3f MAX U WOOD TFLWS 0 WEE MEVEB-ER O 0 lF9P d 60" (1524mm) MA. BO TCIM OFF,IFE1J TOP OF CHOFD \'\\ WHEN OFFSETTING CPVC PIPE OVER AN -' DESTRUCTION, A 13L5608 MODEL "IC" SPRINKLER 6" (152mm) MAX. ASOVE CEILING OR NON-COMBUSTIBLE CEILING INSUTION, DR 113 THE DEPTH OF CONCEALED] MUST BE INSTALLED DIRECTLY ON THE PIPE OVER THE OBSTRUCTION. AREA (AS MEASURED FROLi TOP SURFACE OF CEILING TO TOF SURFACE OF JOIST INSL-LATIO' ABOVE), OR WHIOH E'ER S SMALLER WHEN THE LOWER JOIST IS GREATER THAN 8" (152mm) IN HEIGHT CPVC PIPING IS PERMITTED TO BE ATTACHED DIRECTL"' TO THE TOP OF THE JUST. FIGURE 2: CPVC PIPE NON-COMBUSTIBLE INSULATION FILLED UPPER DECK SOLID WOOD, COMPOSITE WOOD JOIST, OR WOOD TRUSS CONSTRUCTION STEEL PIPING DESIGN REQUIREMENTS SYSTEM TYPE DRAFT CURTAINS Wet pipe system and dry type systems. Draft Curta n for Unobstructed wood truss constction ard noncombustible bar ioist construction mLJ:2t be R" i202mm' ALLOWABLE CONS TRUCTIO TYPES 'N in height or one third of the depth of the concea'ed space: whichever is greater. Draft curtains mus: be corstructed of a material that will not allow for heat to escape through o, above the'r. Draft Curtain for Obstructed wood truss and solid wood joist construction must be 6" (1524mm:) in height or one third of the depth of the concealed space, whichever is greater. Draft curtains must be constructed cf a if aterial that will no: allow for heat to escape through or above them. Unobstructed wooc truss construction' Unobstructed bar joist construction' Solid wood joist corstruction2 Obstructed wood truss Construction2 Non-combustible insuatbn filled solid wooc joist construction' Non-combustible insulation filled com:Dsite wood joist construction3 NOTE: Upper joist/truss cannot La ,TOE thm' 4" (10; .6mm,' in heicht. 2 Upper joist/fross cannot La more tha'-" 12" (3114.änro) in ne'ghf. 3 The joist space in nor-ccmoustLote r-"sulatior fil/Ed bit construction most be completely filled with noncombustible insulation and secured in place by metal wire netting to hold the insulation in pace in the event of a ire, PARTITION REQUIREMENTS For unobstructed wood truss construct,on, unobstruc:ed bar joist construction, solid wood joist construction, and obstructed wood truss construction the concealed space being protected must be broken up into areas no greater than 1000 square feet either by full height wails or by draft curtains. Noncombustible insulation illed joist construction is notre- quired to be broken up into paritonec areas.. - DEFLECTOR POSITION 1 '/2 to 4 nches below the upper deck for unobstructed wood truss a-id bar joist constructions 1 /2 to niches below the joists for noncombustible insulation filled solid and composite v/cod joist ccnstruction. 1 1/2 to 2 nches below the jois: or truss or solid -wood joist or obstructed truss construction. 4 inches away from trusses BLOCKING For solid wcod foist and obstructed wood :russ constructioi blocking must be provided in each o the channels between the upper joists or trusses. The blocking must be locatedi where the draft curtains intersect the channels. The block- ing must be installed to the full depth of the jois:s and be -installed as :o not allow heat to escape through or above the blocking. The blocking must be installed using either the same materai as the joists or a roncomoustible material. NOV 2018 GFS-600 (Formerly A-40) - Page 4 of 6 CONCEALED SPACE SIZE All spaces must have a minimum open space (from top of lower joist, cord, or truss to bottom of upper joist, cord, or truss) of 6(152.4mm) (see Figures 3, 4, and 5). Unobstructed wood truss and bar joist construction must not have a total concealed space height of more than 60"(1.5m). (see Figure 3). Joist construction with noncombustible insulation in the upper deck must not have an open space (from top of lower joist to bottom of upper joist) of greater than 60"(1.5m) in size. They must not have a total concealed space height of greater than 72"(1.8m). This allows for a maximum lower joist space of 12(304.8mm) (see Figure 4). Solid wood joist and obstructed truss construction must not have an open space (from top of lower joist or truss to bottom of upper joist or truss) of greater than 60"(1.5m) in size. They must not have a total concealed space height of greater than 84"(2.1 m). The upper joist space must not be greater than 12(304.8mm) in depth(see Figure 4). 41/2(114mm) MIN. TO FACE OF WOOD TRUSS OR TOP CHORD OF BAR JOIST 4" (1 UPPER 1 1/2" (38mm) MIN. 4-(100 m) MAX. (1mm) (152mm) MIN. CEILING FRAME ARMS MUST BE INSTALLED IN-LINE WITH PIPE RUN (MODEL FIGURE 3: STEEL PIPE UNOBSTRUCTED WOOD TRUSS OR NON-COMBUSTIBLE BAR JOIST CONSTRUCTION 2x FLOOR SOLID WOOD JOISTS/OBSTRUCTED TRUSS UPPER DECK 16 (406mm) ON CENTER ________________ 1 1/2" (38mm) MIN. 12 (305mm) MAX. [ 2 (51 mm) MAX. 84" FRAME ARMS MUST (2134mm) BE INSTALLED GL5608 _______ 60" (1524mm) M. MAX. 6" (152mm) MIN. IN-LINE WITH PIPE RUN1' IC SPRINKLER) CEILING NG FRAMI FIGURE 4: STEEL PIPE OBSTRUCTED WOOD TRUSS OR SOLID WOOD JOIST CONSTRUCTION NOV 2018 GFS-600 (Formerly A-40) Page 5 of 6 UPPER DECK 1 NON-COMBUSTIBLE 2x FLOOR SOLID UINSULATIOCOMPOSITE WOOC JOST WC1(lfl .I(IT 11/2' (38rrm) MIN. IMaMF 4" (132mm) M INSULATION IN PLACE WITH METAL (MODEL IC SPRINKLER) WIRE NETTING 60 52 m) MAX. FRAME ARMS MUST BE INSTALLED 72" IN-LINE WITH PIPE RUN (1829mm) MAX. CEILING FRAMING FIGURE 5: STEEL PIPE NON-COMBUSTIBLE INSULATION FILLED UPPER DECK SOLID WOOD OR COMPOSITE WOOD JOIST CONSTRUCTION ORDERING INFORMATION GLOBE® PRODUCT Quantity ° SIN ° Style ° Orifice olhread Size WARRANTY Temperature ° Finishes ° Desired Quantity Globe agrees to reDir or replace any of its own manu- factured products fourd to be defective in material or work- manship for a period cf one year from date of shipment. For specific details ,of our warranty please refer to Price List Terms and Conditions of Sale (Our Price List). 4077 Airpark Dr. Technical Support Standish, Ml 48658 1-800-248-0278 www.globesprinkIer.com io_ Ph. 989-846-4583 techservice@globesprinkler.com NOV 2018 GFS-600 (Formerly A-40) Page 6 of 6 9-:~Wm ~~i i!~E 4077 Airpark Dr. Standish, Ml 48658• 989-846583• www.globesprinkler.com FIRE SPRINKLER CORPORATION Technical Support. 989-414-2600 techservice@globesprinkler.com SPECIFIC APPLICATION ATTIC SPRINKLERS GENERAL DESCRIPTION The Globe Specific Application Attic Protection Scheme has undergone full scale fire testing with Underwriters Laborato- ries and is Listed to be utilized per NFPA 13 in conformance with the New Technology and Equivalency Sections as well as the Special Sprinkler Section. The Globe Specific Application Attic Protection Scheme has been engineered to consider all construction conditions typically found in the attic built environment. The scheme utilizes a unique strategy with two distinct types of special sprinklers. The positioning and use of these sprinklers in conjunction with each other, and their complimentary ef- fects on fire control has been carefully considered for these specific Attic structure hazards. Consequently, the required number of sprinklers to calculate and system demand is drastically reduced from that seen with standard protec- tion schemes or even the more recent Special Application schemes. The Globe Specific Application Attic Protection Scheme uti- lizes two specially listed sprinklers, each with a fixed flow and pressure requirement. The "Area/Density" allowances of NFPA 13 do not apply and reductions in flow cannot be taken for reduced spacing. Moreover, as a fixed flow and pressure sprinkler which has been full scale fire tested in its intended installed environment, the slope ceiling penalty of "Area/Density" sprinklers per the prescriptive requirements of NFPA 13 does not apply. The Globe Specific Application scheme is based on full scale fire testing resulting in antici- pated Heat Affected Zones of Protection The Globe Attic Protection Scheme requires identifying any of four separate 'spaces" within an attic; "Ridgeline"; "Downslope"; "Lower Hip" and "Upper Hip". See Figure 1. FIGURE 1: ATTIC AREA OF PROTECTION IDENTIFICATION MODEL GL-SS/RE MODEL GL-SS/DS GL5620 GL5621 *Multiple Patents Pending SYSTEM CRITERIA SLOPE 3:12 up to and including 6:12 SPAN I Branchline up to 24 ft 3 Branchlines up to 72 ft TOTAL SYSTEM DEMAND See Hydraulic Calculation section for details AREA OF USE LIGHT HAZARD CONCEALED ATTIC SPACES: RIDGELINE Sprinkler Model: GL-SS/RE • K-Factor: 5.6 Temperature: 200° F DOWNSLOPE Sprinkler Model: GL-SS/DS • K-Factor: 5.6 Temperature: 200° F Sprinkler Model: GL-SS/RE • K-Factor: 5.6 Temperature: 200° F EAVE Sprinkler Model: GL-SS/RE • K-Factor: 5.6 Temperature: 200° F HIP Sprinkler Model: GL-SS/RE • K-Factor: 5.6 Temperature: 200° F NOTE: Users should refer to Globe's web site (www.globesprinkler.com) to assure that the most recent technical literature is being utilized. SEPT 2018 Page 1 of 22 GFS-650 2 1 FIGURE 5: MODEL GL-SS/DS GL5621 MATERIALS OF CONSTRUCTION ITEM NO. DESCRIPTION MATERIAL 1 DEFLECTOR Bronze 2 COMPRESSION SCREW Brass 3 BULB Glass 3mm diameter 4 FRAME Brass 5 BULB SEAT Brass 6 BULB SEAT GASKET Teflon FIGURE 3: MODEL GL-SS/DS GL5621 2%" 70mm I 2%0 70mm 1%" 44mm 1 21,/4 27mm FIGURE 2: MODEL GL-SS/RE GL5620 FIGURE 4: MODEL GL-SS/RE GL5620 MATERIALS OF CONSTRUCTION TECHNICAL DATA Approvals cULus Maximum Working Pressure 175 psi (l2bar) Factory tested to 500 psi (34 bar) Minimum Low Temperature -40'F (-40°C) Minimum Operating Pressure 12.8 psi (0.88 bar) Temperature Rating 200°F (93.3°C) Response Type Quick Response ITEM NO. DESCRIPTION MATERIAL 1 DEFLECTOR Bronze 2 FRAME Brass 3 COMPRESSION SCREW Brass 4 BULB Glass 3mm diameter 5 BULB SEAT Bronze 6 BULB SEAT GASKET Teflon 7 BELLEVILLE SPRING Steel SEPT 2018 Page 2 of 22 GFS-65.0 FIGURE 6B FIGURE 6: DIMENSION FROM EAVE 1001 GL-SS/DS SPRINKLER 20.0 j 44' - MAX. I MAX. - FIGURE 7: SPRINKLER FRAME ORIENTATION TO ROOF SLOPE 6 MIN. TRUSSES FIGURE 8: DIMENSION FROM TRUSS OPERATION Upon the application of sufficient heat, the fluid within the bulb expands, compressing the air bubble within the bulb. When the air bubble can no longer compress, the fluid ex- pansion results in breakage of the glass bulb, allowing the evacuation of the water seat assembly, and discharge of water from the sprinkler. INSTALLATION The Globe Specific Application Attic Sprinklers for Protect- ing Attics must be installed in accordance with this section. The Globe GL-SS/RE and GL-SS/DS Specific Application Attic Sprinklers comprise an overall protection scheme which takes into account strategic positioning for activation sensitivity while providing unique distribution characteris- tics specifically designed for attic construction. The protection methodology utilizing these sprinklers has been full scale fire tested in the built attic environment. As such, they must be installed in accordance with the guide- lines set forth within this data sheet. The NFPA 13 Den- sity/Area prescriptive spacing requirements do not apply as these sprinklers are not bound by the NFPA 13 "S x L Rules". The positioning and spacing requirements of this data sheet take precedence over any other prescriptive re- quirements that may exist in NFPA 13. NOTICE Do not install any bulb-type sprinkler if the bulb is cracked or there is loss of liquid from the bulb. A leak-tight 1/2 inch NPT sprinkler joint should be obtained by applying a torque of approximately 7 to 14 ft.-lb. (9,5 to 19,0 Nm). Higher levels of torque can distort the sprinkler inlet resulting in possible leakage. To install the Globe Specific Application Attic Sprinklers, the following steps shall be taken: Step 1. Sprinklers must be oriented correctly as follows: Series GL-SS/RE Sprinklers - At horizontal ridge (peak) - installed in the upright verti- cal position with deflector parallel to the ceiling below (i.e. sprinkler centerline perpendicular to the ridgeline). - Near eave or under hip type roofs - installed in the up- right position with deflector parallel to roof deck (i.e. sprin- kler centerline perpendicular to the roof slope). Series GL-SS/DS Sprinklers - These sprinklers are installed downslope from a ridge- line/peak (See Figure 11). Installed in the upright position with deflector parallel to roof deck (i.e. sprinkler centerline perpendicular to the roof slope). Step 2. With pipe thread sealant applied to the pipe threads, hand tighten the sprinkler into the sprinkler fitting. Note: Do not grasp the sprinkler by the deflector. Step 3. Wrench-tighten the sprinkler using only the ap- propriate wrench. Wrenches are only to be applied to the sprinkler wrench flats or wrench hex, as applicable. Note: Do not apply wrench to frame arms. SPRINKLER SPACING MEASURED HORIZONTALLY FROM THIS POINT BOTTOM CHORD FIGURE 6A SPRINKLER SPACING MEASURED HORIZONTALLY FROM THIS POINT - 2 MAX. GAP FOR EAVE VENTING\ , COMBUSTIBLE INSULATION SEPT 2018 Page 3 of 22 GFS-650 S ROOF SLOPE ;DOWN S ROOF: SLOPE DOWN II i EAVE RIDGELINE FIGURE 9A RIDGELINE UI U. 0 -Iz 0 0 Ic RIDGELINE SYSTEM DESIGN PROCEDURE GABLE STYLE ROOF OPTION 1: RIDGE SPRINKLERS ONLY When utilizing this option Model GL-SS/RE sprinklers are used to protect the entirety of the attic space. The span of the attic is measured along the floor (or ceiling of floor below) of the attic space from the peak to the intersection of the bottom of the top chord of the roof joist and the insulation or floor joist on the floor (or ceiling of floor below). The span is twice the longer of the two measured spans. (See Figure 6) The maximum span which can be protected by a single line of GL-SS/RE sprinklers at the peak is a total span of 24 ft or a maximum half span of 12 ft. OPTION 2: RIDGELINE SPRINKLERS/EAVE SPRIN- KLERS (GL-SS/RE) This approach utilizes the GL-SS/RE sprinklers at the Ridgeline and downslope covering to the eave. (See Figure 10 for dimensional limitations) 2% F -.-* FIGURE 9B OPTION 3: RIDGELINE SPRINKLERS WITH DOWNSLOPE SPRINKLERS The maximum span of this approach is 72 ft or a half span of 36 ft. as measured horizontally. (See Figures 10 and 11 for dimensional limitations) NOTE: Single sloped roofs have not been investigated at the time of printing. Design single slope roofs with shear walls in ac- cordance with NFPA 13. = MODEL GL-SS/RE = MODEL GL-SS/DS FIGURE 9C FIGURE 9: PROTECTION OPTIONS SEPT 2018 Page 4 of GFS:-650 SEE H (FIGURES RIDGELINE DESIGN CRITERIA SPRINKLER MODEL GL-SS/RE FLOW RATE 20gpm DISTANCE BETWEEN SPRINKLERS ALONG RIDGE Minimum 6 ft Maximum 8 ft MINIMUM DISTANCE TO DOWNSLOPE SPRINKLER 6 ft (measured horizontally) MAXIMUM DISTANCE TO DOWNSLOPE SPRINKLER 16 ft (measured horizontally) DEFLECTOR DISTANCE BELOW CEILING (AT RIDGELINE) Minimum 16 in Maximum 24 in DEFLECTOR DISTANCE BELOW CEILING (WHEN DOWNSLOPE OF RIDGELINE) Install with deflector below bottom of top chord to be a maximum of 2" (maximum top chord to be 6"). LATERAL MAXIMUM DISTANCE FROM RIDGELINE 12 in DISTANCE FROM HIP PEAK Minimum 1 ft Maximum 4 ft INSTALLATION When installed for Ridgeline protection, the GL-SS/ RE Sprinkler has a zone of protection of 24 ft. wide as measured horizontally across the ridgeline). The maximum zone of protection on either side of the ridgeline is 12 ft. (as measured horizontally). The zone of protection along the ridgeline is 8 ft. (4 ft. maximum to either side of the GL-SS/RE Sprinkler). When a GL-SS/RE sprinkler is installed under a horizontal Ridge, the deflector is to be positioned parallel with the floor/ceiling below. (Regardless of allowed offset from directly below ridge) Maximum span for GL-SS/RE sprinkler to cover is 24 ft wide attic. Sprinklers must be installed with the frame arms parallel to the ridge. Centerline of sprinkler must be a minimum of 6" laterally from face of any truss. (see Figure 8) For obstruction criteria, see Obstruction section within this data sheet. EAVE I SEE 6OVVN§L6P9 LAYöUt CITRIA I II I I I I I I I I I I II lI I I I 121 I I I T r I H1Il° IIIIHI liii LAY; LIT I 13)FR THIS AREA ' I , I I 4.MLJ ! 1 1IVIIN.:, 1 8 MAX I I I I I I I I I I I I I I I I I I I I I I I I I I I I I SEE DO'JVNLOP LA\YIbU+ CII1ERA II I I I I I I I 2 lu A. - 0 IZ -. 2 N I- - RIDGELINE 2 N 1 0 -. .Jz ILO 5 EAVE r MODEL GL-SS/RE MODEL GL-SS/DS FIGURE 10: RIDGELINE LAYOUT CRITERIA SEPT 2018 Page 50f22 GFS-650 DOWNSLOPE DESIGN CRITERIA SPRINKLER MODEL GL-SS/DS FLOW RATE 20gpm DISTANCE BETWEEN SPRINKLERS PERPENDICULAR TO SLOPE Minimum 4 ft Maximum 8 ft MAXIMUM SPRINKLER THROW (measured horizontally) Upslope-4ft Downslope - 20 ft MINIMUM DISTANCE BETWEEN SPRINKLERS DOWNSLOPE OF THE GL-SS/DS (throw direction) 15 ft DEFLECTOR DISTANCE BELOW CEILING Install with deflector below bottom of top chord to a maximum of 2" (maximum t:'p chord to be 6"). DISTANCE AWAY FROM HIP"LINE Minimum 1 ft Maximum 3 ft INSTALLATION The GL-SS/DS Sprinkler has a zone of protection of 20 ft. forward (measured on the horizontal); 4 ft. backwards (measured on the horizontal; and 8 ft. wide (4 ft. laterally to either side of the sprinkler). Ensure that the sprinkler deflector is installed with the deflector parallel to the sloped roof above. Centerline of sprinkler must be a minimum of 6" laterall from face of truss (See Figure 8). Must be offset at least :)ne channel laterally from any Ridgeline sprinkler. Sprinklers must be installed with the frame arms perpendicular to the roof slope. For obstruction criteria, see Obstruction section withir. this data sheet. EAVE GL S/DS SPPW KLEFS MUET BE \.1 DFFSETtATLEA.TONECHPNNEL 8MAX' FROM SPRINKLERS UPSLOPE 11 4M 'it / -- --I- \ U iII 1 ISEIDI3ELINjE I --I--- " 7 I - - I (FIqUFE O)l J FORTHISAREA GL-SS/RE SPRINKLER ( I DEFLECTOR DISTANCE BELOW BOTTOM OF TO _/ (FIGURES 1 & 13 FOR THIS AREA CHORD TO MAXIMUM OF 20 I I (MAX. TOP CHORD TOBE6°) ---.--. - I I I I I I I TTTT Y rT -r— T H - EAVE = MODEL GL-SS/RE = MODEL GL-SS/DS FIGURE 11: DOWNSLOPE LAYOUT CRITERIA SEPT 2018 Page 6of22 S • 0 19 2 N RIDGELINE w 0. 0 -jz 0 2 C N GFS-65C - HIP AREA SPRINKLER DESIGN CRITERIA HIP TRUSS/JACK TRUSS CONSTRUCTION MODEL GL-SS/RE FLOW RATE 20gpm DISTANCE BETWEEN SPRINKLERS FIRST ROW FROM EAVE (measured horizontally) Minimum 6 ft Maximum 8 ft DISTANCE BETWEEN SPRINKLERS ALL OTHER ROWS UPSLOPE (measured horizontally) Minimum 6 ft Maximum 12 ft DISTANCE FROM EAVE TO FIRST ROW (measured horizontally) Minimum 5 ft Maximum 12 ft DISTANCE BETWEEN ROWS (measured horizontally) Maximum 12 ft MINIMUM DISTANCE BETWEEN SPRINKLERS 6ft DEFLECTOR DISTANCE BELOW CEILING Install with deflector below bottom of top chord to a maximum of 2" (maximum top chord to be 6'). SPRINKLER AT APEX A GL-SS/RE Sprinkler must be installed between 1 ft. to 5 ft. down from the intersection of the ridgeline and hip lines (Apex) SPRINKLERS ADJACENT TO HIP LINE All GL-SS/RE Sprinklers directly adjacent to hip line shall be 1 ft. to 3 ft. from hip line (as measured perpendicular to hip line) INSTALLATION Ensure that the sprinkler is installed with the deflector parallel to the sloped roof above. Sprinklers must be installed with the frame arms perpendicular to the roof slope (see Figure 7). For obstruction criteria, see Obstruction section within this data sheet. --------------------- a MAX._ 8*MAX. _ -I I II ii I III III I I II I2MAX. 5MIN. ,"8-MAX. lill MIN. 12" DEEP DRAFT 6 MIN. STOP REQUIRED AT HIP REQUIRED SPACING FOR TRUSS ONLY IF 1ST ROW 1ST ROW FROM EAVE ONLY IS BELOW HIP TRUSS (REGARDLESS OF FRAMING DIRECTION) (BETWEEN EAVE & 1ST HIP TRUSS) FIGURE 12A: HIP LAYOUT CRITERIA WHEN FIRST ROW OF SPRINKLERS PLACED "WITHIN" JACK TRUSSES * = MODEL GL-SS/RE 5MAX. ;L7 10 MAX 16Jw:. IOMAX. (I I I I I II I I III I Al I\I- I2MAX. !JAdK!TILSSE 1' 5' MIN. BMAX. 6 MIN. REQUIRED SPACING FOR 1ST ROW FROM EAVE ONLY (REGARDLESS OF FRAMING DIRECTION) FIGURE 1213: HIP LAYOUT CRITERIA WHEN FIRST ROW OF SPRINKLERS PLACED "BEYOND JACK TRUSSES FIGURE 12: HIP LAYOUT CRITERIA - HIP TRUSS! JACK TRUSS CONSTRUCTION SEPT 2018 Page 7of22 GFS-650 HIP AREA SPRINKLER DESIGN CRITERIA FRAMING MEMBERS PARALLEL TO ROOF SLOPE MODEL GL-SS/RE FLOW RATE 20gpm DISTANCE FROM EAVE TO FIRST ROW (measured horizonlally) Minimum 5 ft Maximum 12 ft MAXIMUM DISTANCE BETWEEN SPRINKLERS See Figure 13 DEFLECTOR DISTANCE BELOW CEILING Install with deflector below bottom of top chord to a maximum of 2' (maximum top chord to be 6"). SPRINKLER AT APEX A GL-SS/RE Sprinkler must be installed between 1 ft. to 5 ft. down from the intersection of te ridgeline and hip lines (Apex) SPRINKLERS ADJACENT TO HIP LINE All GL-SS/RE Sprinklers directly adjacent to hip line shall be 1 ft. to 3 ft. from hip line (as measured perpendicular to hip line) INSTALLATION Ensure that the sprinkler is installed with the deflector parallel to the sloped roof above Sprinklers must be installed with the frame arms perpendicular to the roof slope. For obstruction criteria, see Obstruction section within this data sheet. I i I I I I I I -- I I I I I I I . 8- MAX. 6'MIN. TYPICAL BELOW ENTIRE HP ROOF WHEN FRAMING IS PARALLEL TO ROOF SLOPE = MODEL GL-SS/RE = MODEL GL-SS/DS FIGURE 13: HIP LAYOUT CRITERIA FRAMING MEMBERS PARALLEL TO ROOF SLOPE SEPT 2018 Page 8of22 GFS-650 DORMER PROTECTION CRITERIA The protection scheme for dormer roofs shall be in accordance with the following guidelines: Dormers Built Entirely Over (on top) of Main Roof Sheathing - 4 Sprinklers or Less - Any Slope RE/DS Sprinklers allowed (CPVC allowance applies for wet systems only) Standard Spray Sprinklers allowed Dormers Built Entirely Over (on top) of Main Roof Sheathing - More than 4 Sprinklers RE/DS Sprinklers allowed where the pitch is between 3:12 and 6:12. Protection scheme utilized shall be in accordance with this document Standard Spray Sprinklers allowed for any slope Dormers Open to Attic Space Below -4 Sprinklers or Less - Any Slope RE/DS Sprinklers allowed (CPVC allowance applies for wet systems only) Standard Spray Sprinklers allowed. Dormers Open to Attic Space Below - More than 4 Sprinklers RE/DS Sprinklers allowed where the pitch is between 3:12 and 6:12. Protection scheme utilized shall be in accordance with this document Standard Spray Sprinklers allowed for any slope. (Required to calculate Attic in accordance with NFPA 13 (i.e. 2535 sq. ft. for Dry Systems) DORMER OPEN TO ATTIC AREA NON-CONTINUOUS SHEATHING DORMER OPEN TO ATTIC SPACE DORMER ENTIRELY OVER MAIN ROOF SHEATHING FIGURE 14: DORMERS SECTION VIEW SEPT 2018 Page 9 of 22 GFS-650 HYDRAULIC DESIGN The Globe Specific Application Attic protection scheme shall be hydraulically calculated in accordance with the following guidelines. These calculation guidelines are applicable only to the special Globe Attic Protection scheme utilizing Globe GL-SS/RE and GL-SS/DS sprinklers. These requirements are based on special full scale fire testing and in no way should be utilized when designing other than these specially listed and tested sprinklers for use in sloped combustible attic struc- tures. As with Hydraulic Calculations performed in accordance with NFPA 13, multiple areas of piping may need to be investigated and multiple calculations performed should it not be readily obvious of the hydraulically most demanding area due to non-typical pipe layout. Hose allowances must be included in the hydraulic calculations in accordance with NFPA 13. GABLE ROOF CALCULATION PROCEDURE 3 BRANCHLINE DESIGN - WET SYSTEM Perform the following 2 calculations: Calculation #1: Calculate :he 5 most hydraulically demanding sprinklers consisting of 5 GL-SS/RE (Ridgeline) sprinklers. Minimum sprinkler flow is 20 gpm per sprinkler. See Figure 15A. Calculation #2: Calculate the 5 most hydraulically demanding sprinklers consisting of 2 GL-SS/DS (Downslope) sprinklers and 3 GL-SS/RE (Ridgeline) sprinklers. Minimum sprinkler flow is 20 gpm per sprinkler. See Figure 15B. Note: If additional sprinklers are required beyond an obstruction, calculate up to 2 additional sprinklers beyond the obstruc- tion. (See Figure 15B) 4] o 0 Iii — S — • - z w -W S I w > Ui 0 0 55 0 I O LZU -I w 0 0 -• — — a — 0 0 - 0 FIGURE 15A FIGURE 15B FIGURE 15: HYDRAULIC CALCULATION REQUIRED FOR WET 3 BRANCHLINE SYSTEM SEPT 2018 Page 10of 22 GFS-650. HYDRAULIC DESIGN 3 BRANCHLINE DESIGN - DRY SYSTEM Perform the following 2 calculations: Calculation #1: Calculate the 6 most hydraulically demanding sprinklers consisting of 6 GL-SS/RE (Ridgeline) sprinklers. Minimum sprinkler flow is 20 gpm per sprinkler. See Figure 16A. Calculation #2: Calculate the 6 most hydraulically demanding sprinklers consisting of 2 GL-SS/DS (Downslope) sprinklers and 4 GL-SS/RE (Ridgeline) sprinklers. Minimum sprinkler flow is 20 gpm per sprinkler. See Figure 16B. Note: If additional sprinklers are required beyond an obstruction, calculate up to 2 additional sprinklers beyond the obstruc- tion. See Figure 16B. 1 I • • • • • • lii - U -. S I UU UI Z iii LLI MI I Z • 12 • • U I • • • FIGURE 16A FIGURE 16B FIGURE 16: HYDRAULIC CALCULATIONS REQUIRED FOR DRY 3 BRANCHLINE SYSTEM SEPT 2018 Page 11 of 22 GFS-650 HYDRA ULIC DESIGN HIP ROOF CALCULATION PROCEDURE C .1 When a Hip is included in the design of the attic, there are three calculations reqiired. One calculation for the "Ridge/Hip Transition" area. The second and third calculations determine the pipe sizirg for the Hip area itself. For the purposes of these hydraulic calculations the Hip is broken into two areas; the Lower Hip" area; anci the "Upper Hip" area. See above figure. HIP CALCULATION (HIP TRUSS/JACK TRUSS CONSTRUCTION) -WET SYSTEM Calculation #1. - Ridge/Hip Transitions Calculate the most demanding 7 cor:guous spriiklers with. a maximum of ,5 sDirkIers along the ridge plus the 2 most demanding sprinklers within the hip area. See. Fiue 17A. Minimum sprinkler flow is 20 gpm per sprinkler. Calculation #2 - Lower Hip Area Calculate up to the 7 most demandin contguous sprinklers along tie eave. This may include sprinklers on both sides of the hip line as shown. See Figure 17B. Minimum sprinkler flow is 20 gpm per sprinkler. Calculation #3 - Upper Hip Area If there a-e 4 sprinklers or less in the shaded area (Figure 17B): Calculate up to the 7 most demandin contgeous sprinklers in the "Upper ftp' area. This may include sprinklers on both sdes of the hip line as shown. Minimum sprinkler flow is 20 gpm per sprinkler. If there ae more than 4 sprinklers in the shaded area (Figure "170d): Calculate the hydraulically most demanding 7.E% o'tie total numbe- :f spffink!Ers ocated within the "Upper Hip" area, rourding up to the nearest sprinkler. Minirrurn number of sprinklers to be calculated is 7) Minimum sprinkler flow is 20 gpm per sprinkler. - Example shown in Figure 17C results in 9 sprinklers to be calculated. (12 x 0 75 = 9) I--------,/1I '-'..- / 5, • ". -i I• V - FIGURE 17A FIGURE 17C - FIGURE 17 HYDRAULIC CALCULATIONS REQUIRE) FOR HIP -WET SYSTEW (HIP TRUSS/JACK TRUSS CONSTRUC11ON) - SEPT 2018 Page 12of 22 - GFS-650 HIP CALCULATION (HIP TRUSS/JACK TRUSS CONSTRUCTION - DRY SYSTEM Calculation #1 - Ridge/Hip Transitions Calculate the most demanding 8 contiguous sprinklers with a maximum of 6 sprinklers along the ridge plus the 2 most demanding sprinklers within the hip area. See Figure 18A. Minimum sprinkler flow is 20 gpm per sprinkler. Calculation #2 - Lower Hip Area Calculate the 8 most demanding contiguous sprinklers along the eave. This may include sprinklers on both sides of the hip line as shown. See Figure 18B. Minimum sprinkler flow is 20 gpm per sprinkler. Calculation #3 - Upper Hip Area If there are 4 sprinklers or less in the shaded area (Figure 1813): Calculate up to the 8 most demanding contiguous sprinklers in the 'Upper Hip area. This may include sprinklers on both sides of the hip line as shown. See Figure 18B. Minimum sprinkler flow is 20 gpm per sprinkler. If there are more than 4 sprinklers in the shaded area (Figure 18C): Calculate all sprinklers in the "Upper Hip' area. Minimum sprinkler flow is 20 gpm per sprinkler. FIGURE 18C FIGURE 18: HYDRAULIC CALCULATIONS REQUIRED FOR HIP - DRY SYSTEM (HIP TRUSS/JACK TRUSS CONSTRUCTION) (Examples shown in these figures are for reference only. Actual sprinklers selected based on piping configuration which results in the most demanding hydraulic demand.) SEPT 2018 Page 13of22 GFS-650 HYDRAULIC DESIGN Q HIP CALCULATION (FRAMING MEMBERS PARALLEL TO ROOF SLOPE) - WET SYSTEM Calculation #1 - Ridge/Hip Transitions Calculate the most demanding 7 contigLous sprnklers with a maximum of 5 sprinklers along the ridge plus the 2 most demanding sprinklers within the hp area. See Figure 17A. Minimum sprinkler flow is 20 gpm per sprinkler. Calculation #2 - Hip Area Calculate all sprinklers within the hip area snown shaded. See Figure 19. Minimum sprinkler flow is 20 gpm per sprinkler. HIP CALCULATION (FRAMING MEMBERS PARALLEL TO ROOF SLOPE) - DRY SYSTEM Calculation #1 - Ridge/Hip Transitions Calculate the most demanding 8 cont:guous sprinklers with a maximum of 6 sprinKlers along the ridge plus the 2 most d9manding sprinklers within The hip area. See Figure 18A. Minimum sprinkler flow is 20 gpm pr sprinkler. Calculation #2 - Hip Area Calculate all sprinklers within the hip area shown shaded. See Figure 19. Minimum sprinkler flow is 20 gpm pr sprinkler FIGURE 19: HYDRAULIC CALCULATIONS REQUIRED FOR HP (FRAMING MEMBERS PARALLEL TO SLOPE) SEPT 2018 Page 14cU2 GFS-650 FIGURE 20B OBSTRUCTIONS The following guidelines outline criteria to minimize critical obstructions to spray pattern development and to maximize effectiveness in achieving control. General Structural trusses and web members are not considered "obstructions" provided a minimum 6" lateral distance from sprinklers to side of truss/web member is maintained. GL-SS/RE and GL-SS/DS sprinklers may be installed directly on maximum nominal 21/2U (DN65) pipe without the need for a "Sprig-up'. For pipe larger than 21/2 nominal, see NPFA 13 for Sprig requirements. Sprinklers shall be positioned away from obstructions a minimum distance of Four (4) times the maximum dimension of the obstruction (e.g. Ducts, pipe). This 4X requirement does not apply to truss web members provided the web members do not exceed 6" and the minimum lateral distance of 6" from sprinkler to side of member is maintained. Obstruction criteria is otherwise grouped into three catego- ries (See Figures 20. 21 and 24 Vertical Obstructions Those obstructions which run vertically through the attic. These may consist of fireplace flues, walls, vents, stacks, etc. These obstructions will typically run up to or penetrate the roof deck. Suspended Horizontal Obstructions Those obstructions which are typically "suspended" within the attic space itself and run horizontally. These obstructions will have clearance over and under the obstruction to allow discharge of water around the obstruction. These obstructions may consist of ductwork; walkways; etc. Horizontal obstructions located within 1'-0" vertically of the bottom chords or ceiling joists are not considered Suspended" Horizontal Obstructions. Obstructions at Upper Deck Those obstructions which are either attached directly to the roof deck or to the top chords/joists of the roof framing in a manner that little to no discharge of water can pass/clear the top of the obstruction. These obstructions can have an impact on the upper portion of the spray pattern from sprinklers. PLAN VIEW :5 48' Width • GL-SS/RE/GL-SS/DS c=4Aor4B 1 1131 (Use (Use dimension A or B whichever is greater) Should the sprinkler not be able to be located a distance of 4X away from obstruction, an additional sprinkler must be installed on the opposite side of the obstruction within 1-0 from the opposite side of the obstruction. FIGURE 21: VERTICAL OBSTRUCTIONS GL-SS/RE/GL-SS/DS SPRINKLERS co V c=4Aor4B I B I (Use dimension A or B whichever is greater) No additional sprinkler required below, if equal to or less than 48" suspended obstruction. FIGURE 20A U M U Al >48" Additional sprinkler required below, if greater than 48" suspended obstruction. FIGURE 20C FIGURE 20: SUSPENDED HORIZONTAL OBSTRUCTIONS GL-SS/RE/GL-SS/DS SPRINKLERS SEPT 2018 Page 15of22 GFS-650 OBSTRUCTIONS T 00 - GL-SS/RE SPRINKLER DISTANCE FROM MAXIMUM ALLOWABLE DISTANCE OF SPRKR. TO SIDE OF DEFLECTOR ABOVE OBSTRUCTION BOTTOM OF OBSIRUCTICN (C) inhes (metric) (A) inches (mm) Less than itt. 6 in. NOT ALLOWED 457mm) 1 ft. 6 in (457mm) to less 1 in '25 than 3 ft. 0 in. (914mm) 3 ft. 0 in (914mm) to less 3 in (76) than 4 ft. 0 in. (1.2m) 4 ft. 0 in. (1.2m) to less 5 in (127 than 4 ft. 6 in. (1.4m) 4 ft. 6 in. (1.4m) to less 49 7 in (178 than 6 ft. 0 in. (1.8m) . - 6 ft. 0 in. (1.8m) to less 9 in (229 than 6ft. 6 in. (2m) 6 ft. 6 in. (2m) to less than 11 27) 7ftO in. (2.lm) 7 ft. 0 ii. (2.1 m) to less 14 in 35 than f ft. 0 in. (2.4m) 8 ft. Oh. (2.4m) to less 15 in 381 than E, ft. 6 in. (2.6m) 8 ft. 6 in. (2.6m) to less 17 in 43 than ft. 0 in. (2.7m) *Minimum 31/2" clear space needed for unimpeded hot gas flow FIGURE 22: OBSTRUCTIONS AT LiPPER DECK GL-SSIRE SPRINKLER -.1 SEPT 2018 1 Page 16 of 22 GFS-650 DISTANCE FROM MAXIMUM ALLOWABLE DISTANCE OF SPRKR. TO SIDE OF DEFLECTOR ABOVE BOTTOM OF OBSTRUCTION OBSTRUCTION (A) inches (mm) (C) feet (m) Less than 8 ft. NOT ALLOWED (2.4) 8 ft. (2.4) to less than in (25) 10 ft. (3) 10 ft. (3.0) to less than 2 in (51) 11 ft. (3.3) 11 ft. (3.3) to less than 3 in (76) 12 ft. (3.7) 12 ft. (3.7) to less than 4 in. (102) 13 ft. (4) 13 ft. (4) to less than 6 in (152) 14 ft. (4.3) 14 ft. (4.3) to less than 7 in (178) 15 ft. (4.6) 15 ft. (4.6) to less than 9 in (229) 16 ft. (4.9) 16 ft. (4.9) to less than 11 in. (279) 17 ft. (5.2) 17 ft. (5.2) or greater 14 in. (356) , GL-SS/DS SPRINKLER co FIGURE 23: OBSTRUCTIONS AT UPPER DECK GL-SS/DS SPRINKLER OBSTRUCTIONS SEPT 2018 Page 17of22 GFS-650 OBSTRUCTIONS PIGGYBACK TRUSSES When trusses are stacked (Piggyback") at the peak, con- sideration to obstructions to the spray pattern of the Globe RE sprinklers must be made. These "Piggyback" configura- tions will typically include 2X "Stiffeners' running perpen- dicular to the trusses. Additionally, these "stiffeners" will be sandwiched between the uppermost and lowermost hori- zontal chords of the two stacked trusses.. In the event that all members are above the level of the GL-SS/RE deflector, no obstruction exists to the GL-SS/RE spray pattern. See Figures 24 and 25. STIFFEN __RS 24 MAX. 16" MIN.J DEFLECTOR GL-SS/PE SPRINKLER yy FIGURE 24: DEFLECTOR COMPLETELY BELOW STIFFENERS AND HORIZONTAL WEB MEMBERS (NO OBSTRUCTION) In the event that the GL-SS/RE Deflector is located com- pletely above the stiffeners and horizontal web members, the parameters of Figure 25 must be met for the spray pat- tern to be considered unobstructed. 70% MINUMUM STIFFENERS OPEN AREA GLESPRINKLER U i 7'/' j,t,12 MAX.11 MIN. FIGURE 25: DEFLECTOR ABOVE STIFFENERS AND HORIZONTAL WEB MEMBERS (NO OBSTRUCTION) SEPT 2018 Page 18 of 22 GFS-E5C' CPVC GUIDELINES USE OF UL LISTED CPVC PIPING WITH GLOBE SPECIFIC APPLICATION ATTIC SPRINKLERS (Wet Systems Only) UL Listed CPVC piping may be used in a combustible con- cealed attic space requiring sprinklers when installed in accordance with the following guidelines. For clarity, the following guidlines reference both "Ridgeline/Downslope" areas as well as "Hip" areas. Refer to Figure 1 on page 1 for explanation of these areas. Notice: Where the use of non-combustible insulation is specified, verify with the insulation manufacturer as to the non-combustibility of the insulation. The non-combustible insulation (fiberglass) may be faced or unfaced. Where faced, the facing need not be non- combustible. The insulation is to have a flame spread index of not more than 25. Verify chemical compatibility of the insulation with the UL Listed CPVC by consulting the CPVC Manufacturer's literature. CPVC AT BOTTOM CHORDS TO FEED CEILING SPRINKLERS BELOW UL Listed CPVC may be used to feed the wet system ceiling sprinklers on the floor below when adhering to the following guidelines: (See Figure 26) There must be 6 in. (152.4 mm) of non-combustible insulation covering the horizontal or vertical pipe extending 12 in. (304.8 mm) on each side away from the centerline of the pipe. Refer to Figure 26A. The area above the pipe must be protected with Globe GL-SS/RE and GL-SS/DS Special Application Attic Sprinklers. If the pipe is located inside the ceiling joist, the joist channel must be covered or filled with 6 in. (152.4 mm) of non-combustible insulation on top of the pipe and the area above must be protected by Globe GL-SS/RE and/or GL-SS/DS Sprinklers. Refer to Figure 2613. Insulation is for fire protection purposes. It is not freeze protection. CPVC must be installed in accordance with the CPVC Manufacturer's installation guide instructions. , 12 12" , MIN. -r MIN. I ATTIC SPRINKLER NON COMBUSTIBLE PROTECTED SPACE INSULATION _\ I CPVC JOISJ 1 PIPE & FITTINGS cEILING PENDENT SPRINKLER FIGURE 26A ATTIC SPRINKLER NON COMBUSTIBLE PROTECTED SPACE INSULATION JOIST CPVC CEILING PIPE & FITTINGS PENDENT SPRINKLER FIGURE 26B FIGURE 26: NON-COMBUSTIBLE INSULATION FOR THE PROTECTION OF CPVC PIPE SEPT 2018 Page 19of 22 GFS-650 USE OF UL LISTED CPVC PIPING WITH GLOBE SPECIFIC APPLICATION ATTIC SPRINKLERS (CONTINUED) (Wet systems only) CPVC AT RIDGELINE/DOWNSLOPE AREAS ONLY UL Listed CPVC Pipe and Fittings may be used to feed the GL-SS/RE and GL-SS/DS sprinklers protecting the attic space when adhering to the following guidelines,: (See Figure 27) Wet Systems only Risers are vertical and protected by GL-SS/RE or GL-SS/DS Sprinklers located at a maximum lateral distance of 12 in. (304.8 mm) from the riser centerline. GL-SS/RE or GL-SS/DS Sprinklers are directly mounted on the branchline. GL-SS/RE or GL-SS/DS Sprinklers are on arm-overs and located at a maximum lateral distance of 6 in. (152.4 mm) from the branchline centerline. GL-SS/RE or GL-SS/DS Sprinklers are on verticali sprigs attached to the branchline. I, 1'-O" 1-0" I I (3m) (.3 m) : I I MAX. I 6' (150mm) I 'f'MAX. GL-SS/RE or GL-SS/DS I I I SPRINKLER SPRINKLER GL-SS/RE or DIRECTLY MOUNTED fl GL-SS/DS cvc A cvc fl>. SPRINKLER I CP PVC. CPVC VERTICAL a, H 5 -CPV€ RISER Il< i VERT:tAL RISER - S FIGURE 27C FIGURE 27A DIRECT MOUNT VERTICAL RISER FIGURE 2:7B ARM-OVER DIRECT MOUNT VERTICAL RISER SPRIG UP 6' 150mm) 6'(150mm) , f.(15Omm MAX. MAX. I GL-SS/RE or I GL-SS/DS I - SPRINKLER GL-SS/RE or GL-SS/RE or I I SPRINKLER H SPRINKLER 'I Uj CPVC FIGURE 27D FIGURE 27E FIGURE 27F ANGLED SPRIG ARM OVER SPRIG VERTICAL SPRIG WITH SWING JOINT FIGURE 27: CPVC ALLOWANCE GUIDELINES WET SYSTEMS ONLY (DIRECTLY FEEDING GL-SS/RE I GL-SS/DS SPRINKLERS) SEPT 2018 . Page 20of22 GFS-650 S/RE or GL-SS/DS SPRINKLER SS/REor GL-SS/DS SPRINKLER II I I-I ALLOWED EXPOSED o CPVC CPVC SPRIG W PIPE & FITTINGS NON COMBUSTIBLE Z INSULATION (NOT INTENDED FOR FREEZE PROTECTION) , )?( NON COMBUSTIBLE INSULATION (NOT INTENDED FOR FREEZE PROTECTION) ALLOWED EXPOSED \\ CPVC PIPE CPVC SPRIG & FITTINGS CPVC GUIDELINES CPVC AT HIP AREAS Listed CPVC may be used to feed the GL-SS/RE and GL-SS/DS sprinklers protecting the Hip areas when adher- ing to the following guidelines: Wet systems only When the horizontal branchline piping feeding sprinklers within the hip roof areas is run over the bottom chords of the trusses, it shall be covered with a minimum of 6 in. (152.4 mm) in depth of non-combustible insulation (See Figure 28). This insulation must extend nominally 12 in. (304.8 mm) on each side away from the centerline of the CPVC branchline. Insulation is for fire protection purposes. It is not freeze protection. When the horizontal CPVC branchline piping feeding the sprinklers within the hip roof areas is located within the ceiling joist, the joist channel must be covered or filled with a minimum of 6 in (152.4 mm) depth of noncombustible insulation on top of the branchline feeding the sprigs (See Figure 29). Insulation is for fire protection purposes. It is not freeze protection. A minimum lateral distance of 18 in (450 mm) is maintained between the CPVC pipe and a heat producing device such as heat pumps, fan motors, and heat lamps. The sprinklers (RE or DS) may be fed by exposed vertical sprigs directly to a sprinkler or exposed angled sprigs directly to a sprinkler provided: —Vertical sprigs have no maximum exposed length, the RE or DS Sprinkler is located at a maximum lateral distance of 12 in (3304.8 mm) from the sprig centerline. —Angled sprigs with a maximum exposed length of 3 ft. (0.9 m). LSS/DS or SPRINKLER I ALLOWED EXPOSED EXPOSED CPVC CPVC SPRIG W PIPE & FITTINGS >- NON COMBUSTIBLE INSULATION (NOT INTENDED FOR FREEZE PROTECTION) JOIST U CEILING FIGURE 29A VERTICAL SPRIG :SS/REor SPRINKLER ALLOWED EXPOSED CPVC CPVC SPRIG PIPE & FITTINGS NON COMBUSTIBLE INSULATION (NOT INTENDED FOR FREEZE PROTECTION) D-0 JOIST CEILING FIGURE 29B ANGLED SPRIG FIGURE 29: EXPOSED CPVC AT HIP ROOF AREAS (HORIZONTAL BRANCHLINE WITHIN JOISTS) WET SYSTEMS ONLY CEI FIGURE 28A FIGURE 28B VERTICAL SPRIG ANGLED SPRIG FIGURE 28: EXPOSED CPVC AT HIP ROOF AREAS (HORIZONTAL BRANCHLINE OVER JOISTS) WET SYSTEMS ONLY SEPT 2018 Page 21 of 22 GFS-650 ORDERING INFORMATION SPECIFY Quaitity' Model • SIN • Part Number GL-SS/RE.... GL5620. 562020001 GL-SS/DS.... GL5621 . . 562120001 Quantity - Wrenches - P/N 325390 4 GLOBE® PRODUCT WARRANTY Globe agrees to repair or replace any of its manufactured products found to be cefective in material or workmanship for a period of one year from date of shipment. For specific details of our warranty please refer to Pri':e List Terms and Conditions of Sale (Our Price List). 4)77 Airpark Dr. Standish, Ml 48658 • 989-846-4583 www.gIobesprinkler.com Technical Suppot• 98E -414-2600 techservice©gtobesprinkIe-.com SEPT 2018 Page 22 of 22 GFS-650 ( i ) FIRE SPRINKLER CORPORATION QUICK RESPONSE A U TOMA TI C SPRINKLERS GL SERIES UPRIGHT e PENDENT VERTICAL SIDEWALL HORIZONTAL SIDEWALL CONVENTIONAL (OLD STYLE) DESCRIPTION AND OPERATION The Globe Quick Response Series GL-QR Sprinklers are a low profile yet durable design which utilizes a 3mm frangible glass ampule as the thermosensitive element. This provides sprinkler operation approximately six times faster than ordinary sprinklers. While the Quick Response Sprinkler provides an aesthetically pleasing appearance, it can be installed wherever standard spray sprinklers are specified when allowed by the ap- plicable standards. It offers the additional feature of greatly in- creased safety to life and is available in various styles, orifices, temperature ratings and finishes to meet many varying design requirements. Quick Response Sprinklers should be used ad- visedly and under the direction of approving authorities having jurisdiction. The heart of Globe's Series GL-QR sprinkler proven ac- tuating assembly is a hermetically sealed frangible glass ampule that contains a precisely measured amount of fluid. When heat is absorbed, the liquid within the bulb expands increasing the inter- nal pressure. At the prescribed temperature the internal pressure within the ampule exceeds the strength of the glass causing the glass to shatter. This results in water discharge which is distrib- uted in an approved pattern depending upon the deflector style used. QUICK RESPONSE SERIES GL-QR SERIES GL-QRICNV UPRIGHT CONVENTIONAL ((5 L;. QUICK RESPONSE SERIES GL-QR SERIES GL-QR/SW PENDENT VERTICAL SIDEWALL TECHNICAL DATA See reverse side for Approvals and Specifications. Temperature Ratings - 135°F (57°C), 155°F (68°C), L &tJ 175°F (79°C), 200°F (93°C), 286°F (141°C) Water Working Pressure Rating -175 psi (12 Bars) QUICK RESPONSE Factory tested hydrostatically to 500 psi (34 Bars) HORIZONTAL LPCB/CE Maximum low temperature glass bulb rating is -67°F (-55°C) SIDEWALL HORIZONTAL Frame - bronze • Deflector - brass • Screw - brass SERIES GL-QRISW SIDEWALL Lodgement Wire - stainless steel • Bulb seat - copper SERIES GL-QR/SW Spring - nickel alloy • Seal - teflon Bulb - glass with alcohol based solution, 3mm size SPRINKLER TEMPERATURE RATING/CLASSIFICATION and COLOR CODING CLASSIFICATION AVAILABLE SPRINKLER BULB COLOR N.F.P.A. MAXIMUM TEMPERATURES CEILING TEMPERATURE ORDINARY 135 F/15 - C,/68 'C ORANGE/RED r r C INTERMEDIATE 175'F/200'F C:/93C YELLOW/GREEN I I p (11 HIGH 286CF 141CC BLUE [ iz C MAR 2018 GFS-100a (Formerly A-20) QUICK RESPONSE A UTOMA TIC SPRINKLERS UPRIGHT PENDENT VERTICAL SIDEWALL HORIZONTAL SIDEWALL CONVENTIONAL (OLD STYLE) SPECIFICATIONS NOMINAL "K" FACTOR THREAD SIZE LENGTH' FINISHES 2.8 (40 metric) 1/2"NP7 (15mm) 21/4" (5.7cm) 4.2 (60 metric) 1/2"NP7 (15mm) 2 1/4" (5.7cm) Factory Bronze 5.6 (80 metric) 1/2"NP (15mm) 2 1/4" (5.7cm) White PolyesteO 8.0 (115 metric) 1/2"NP 11 (15nm) 2 1/4" (5.7cm) Black FoIyester2'3 8.0 (115 metric) I 3/4"NFT (20nm) 2 7/16" (6.2cm) NW L: E: ME I FO UON VERSIONS ARE APFROXIMATE. 'HORIZONTAL SIDEWALL Is 2 9/16". 2FINISHES AVAILABLE ON SPECIAL ORDE R. 3AVAILABLE AS cULus LISTED CORROSION RESISTANT WHEN SPECFIED ON ORDER. LISTINGS/APPROVALS TEMPERATURE 4YC-DOB STYLE SIN FACTOR HAZARD cULLs FM LpCB: CE MEA 135°F 155°F I 175°F 200°F 286°F (7°C) (68°C) (79°C) 93°C) (141°C) 101-92-E GL2815 2.8 LH . X X )( X X X --- X GL4215 4.2 LH X X X X X X X UPRIGHT GL5615 5.6 LH/OH X X X X X X X X X X GL8115* 8.0* (W' NPT) LH/OH X X X X X X X GL8118 8.0 LH/OH X , X X. X X X X X X X GL2801 2.8 LH X X X X X X X GL4201 4.2 LH ,X X X X X X -- X PENDENT GL5601 5.6 LH/OH X X X X X X i X X X X GL8101* 8.0- (1/2" NPT) LH/OH X X X X X X --- --- X GL8106 8.0 LH/OH X X X X X X X X X X VERTICAL GL5632 5.6 LH X X X X X X X - --- -- SIDEWALLt GL8133 8.0 LH X X X X X X --- GL2826 2.8 LH X X X X X X --- -- --- X HORIZONTAL GL4226 4.2 LH X X X X X X --- --- --- SIDEWALL GL5626 5.6 LH/OH )( X X X X X X -- -- X GL5627u 5.6 LH/OH )( X X - X X --- -- X X GL8127 8.0 LH/OH X X X X X X --- --- CONVENTIONAL GL5624 5.6 LH/OH X X X' X X --- --- X X (OLD STYLE) GL81258.0 LH/OH, X X X X X --- --- X -- 'SPRINKLERS SHALL BE LIMITED AS PER THE REQUIREMENTS OF NFPA1 3 AND ANY OTHER RELATED DOCUMENTS. §HORIZONTAL SIDEWALL cULus LISTED FOR DEFLECTOR 4" TO 12" BELOW THE CEILING, FM APPROVED 4" TO 6" BELOW THE CEILING. INSTALL IN ACCORDANCE TO 6S5306 AND ANY OTHER RELATED DOCUMENTS. tPENDENT VERTICAL SIDEWALL cULus LISTED FOR 6' MIN. SPACING. tUPRIGHT VERTICAL SIDEWALL cULus LISTED FOR 9' MIN. SPACING. OH: ORDINARY HAZARD LH: LIGHT HAZARD 1/2" NPT, FOR RETROFIT ONLY 2 LPCB REF. NO. 147c/05 ORDERING INFORMATION GLOBE® PRODUCT WARRANTY SPECIFY Globe agrees to repair or replace any of its own manufactur€- Qua itity • SIN • Style • Orifice products fcund to be defective in material or workmanship fcra Thread Size • Temperature . Finishes desired period of oie year from date of shipment. Quantity - Wrenches - PIN 325390 (1121; For spec fic details of our warranty please refer to Price List P/N 312366 (L 0) Terms and Conditions of Sale (Our Price List). (3ga6m M FIRE SPRINKLER CORPORATION MAR 2018 4077 AIRPARK DRIVE, STANDISH, MICHIGAN 4E658 989-846-4583 FAX 969-E46-G231 1-800-248-0278 ww°gIobesprhkIer.xm PRINTED U S A GFS 100a (Thrmerlyft 0)