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HomeMy WebLinkAbout3390 HARDING ST; ; FPR2017-0097; PermitPERMIT REPORT (41 City of C arlsbad Print Date: 10/14/2021 Permit No: FPR2017-0097 Job Address: 3390 HARDING ST, CARLSBAD, CA 92008 Status: Closed - Finaled Permit Type: FIRE-Construction Residential Work Class: Parcel #: 2041101200 Track #: Valuation: $559,108.00 Lot #: Occupancy Group: Project #: #of Dwelling Units: Plan #: Bedrooms: Construction Type: Bathrooms: Orig. Plan Check #: Plan Check #: Single Family Fire Sprinkli Applied: 03/29/2017 Issued: DEV15085 Finaled Close Out: 08/12/2021 Inspector: Final Inspection: Project Title: HARDING CHESTNUT 4 PLEX Description: APT HARDING SQUARE: INSTALLATION OF (4) NEW SPRINKLER SYSTEMS FOR 4-PLEX UNITS FEE AMOUNT FIRE NFPA 13D Single Family System (lnsp/Bldg) $121.00 FIRE NFPA 13D Single Family System (Plan Review) $132.00 FIRE NFPA 13D Single Family System (Plan Review) $132.00 FIRE NFPA 13D Single Family System (Plan Review) $132.00 FIRE NFPA 130 Single Family System (Plan Review) $239.00 Total Fees: $756.00 Total Payments To Date: $756.00 Balance Due: $0.00 Fire Department Page 1 of 1 1635 Faraday Avenue, Carlsbad CA 92008-7314 1 760-602-4665 1 760-602-8561 f I www.carlsbadca.gov McMahon Fire Protection _j ôo- P0 Box 27116 San Diego Ca. 92198 HYDRAULIC CALCULATIONS FOR Harding Square: Unit 1 3390 Harding St Carlsbad Ca. 92008 FILE NUMBER: 2017 DATE: March 26, 2017 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R3 DENSITY: .05 gpm/sq. ft. AREA OF APPLICATION: 2 sprinklers COVERAGE PER SPRINKLER: 196 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers: Bedroom 2 TOTAL SPRINKLER WATER FLOW REQUIRED: 20.1 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR): 25.1 gpm @ 36.2 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: McMahon fire Protection DESIGN/LAYOUT BY: T. McMahon AUTHORITY HAVING JURISDICTION: City Of Carlsbad CONTRACTOR CERTIFICATION NUMBER: 884732 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE.SDF JOB TITLE: harding square unit 1 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 74.5 20.0 1100.0 74.4 25.1 65.7 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 65.0 SOURCE 65.7 25.1 2 68.0 - - - - 57.7 - - - 3 68.0 - - - - 53.7 - - - 4 68.0 - - - - 53.6 - - - 5 68.0 - - - - 41.6 - - - 6 78.0 HOSE STREAM 33.4 5.0 7 68.0 - - - - 36.2 - - - 8 74.0 - - - - 30.9 - - - 9 78.0 - - - - 28.9 - - - 10 78.0 - - - - 25.6 - - - 11 88.0 - - - - 20.1 - - - 12 88.0 - - - - 17.5 - - - 13 98.0 - - - - 12.0 - - - 14 98.0 - - - - 11.5 - - - Si 98.0 K= 3.00 11.4 10.1 S2 98.0 K= 3.00 11.1 10.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DARE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE.SDF JOB TITLE: harding square unit 1 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 25.1 0.995 PL 30.00 PF 6.6 1 65.0 SRCE 65.7 (N/A) 10.4 150 FTG ETG PE -1.3 2 68.0 0.0 57.7 0.0 0.170 TL 39.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 68.0 0.0 57.7 0.0 4.0 psi, 25.1 gpm 3 68.0 0.0 53.7 0.0 Pipe: 3 25.1 1.025 PL 1.00 PF 0.1 3 68.0 0.0 53.7 0.0 9.8 150 FTG ---- PE 0.0 4 68.0 0.0 53.6 0.0 0.147 TL 1.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 4 68.0 0.0 53.6 0.0 12.0 psi, 25.1 gpm 5 68.0 0.0 41.6 0.0 Pipe: 5 25.1 1.380 PL 92.00 PF 3.8 5 68.0 0.0 41.6 0.0 5.4 150 FTG 4E PE -4.3 6 78.0 H.S. 33.4 5.0 0.035 TL 110.13 PV Pipe: 6 20.1 1.049 PL 15.00 PF 1.6 6 78.0 H.S. 33.4 5.0 7.5 150 FTG E PE 4.3 7 68.0 0.0 36.2 0.0 0.087 TL 18.02 PV Pipe: 7 20.1 1.025 PL 6.00 PF 2.7 7 68.0 0.0 36.2 0.0 7.8 150 FTG 22.0 PE -2.6 8 74.0 0.0 30.9 0.0 0.098 TL 28.00 PV Pipe: 8 20.1 1.101 PL 4.00 PF 0.3 8 74.0 0.0 30.9 0.0 6.8 150 FTG ---- PE -1.7 9 78.0 0.0 28.9 0.0 0.069 TL 4.00 PV Pipe: 9 20.1 1.101 PL 18.00 PF 3.2 9 78.0 0.0 28.9 0.0 6.8 150 FTG 29.0 PE 0.0 10 78.0 0.0 25.6 0.0 0.069 TL 47.00 PV Pipe: 10 20.1 1.101 PL 10.00 PF 1.2 10 78.0 0.0 25.6 0.0 6.8 150 FTG 7.0 PE -4.3 11 88.0 0.0 20.1 0.0 0.069 TL 17.00 PV Pipe: 11 20.1 1.101 PL 22.00 PF 2.6 11 88.0 0.0 20.1 0.0 6.8 150 FTG 16.0 PE 0.0 12 88.0 0.0 17.5 0.0 0.069 TL 38.00 PV Pipe: 12 20.1 1.101 PL 10.00 PF 1.2 12 88.0 0.0 17.5 0.0 6.8 150 FTG 7.0 PE -4.3 13 98.0 0.0 12.0 0.0 0.069 TL 17.00 PV Pipe: 13 6.0 1.101 PL 42.00 PF 0.6 13 98.0 0.0 12.0 0.0 2.0 150 FTG 34.0 PE 0.0 Si 98.0 3.0 11.4 10.1 0.007 TL 76.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE.SDF JOB TITLE: harding square unit 1 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 -4.1 1.101 PL 1.00 PF 0.0 51 98.0 3.0 11.4 10.1 1.4 150 FTG 7.0 PE 0.0 14 98.0 0.0 11.5 0.0 0.004 TL 8.00 PV Pipe: 15 -14.1 1.101 PL 8.00 PF 0.5 14 98.0 0.0 11.5 0.0 4.8 150 FTG 7.0 PE 0.0 13 98.0 0.0 12.0 0.0 0.036 TL 15.00 PV Pipe: 16 10.0 1.101 PL 8.00 PF 0.3 14 98.0 0.0 11.5 0.0 3.4 150 FTG 10.0 PE 0.0 S2 98.0 3.0 11.1 10.0 0.019 TL 18.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 27091255 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 0.017 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.4 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 1 under full flow conditions is 74.44 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE.SDF JOB TITLE: harding square unit 1 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEli ChkViv BfyViv GatVlv AimChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G F45 El Tee RunT Kpig ChkViv Gate 1.101 1.40 2.50 6.00 1.70 1.00 8.00 0.40 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Eli Tee 45-Eli TeeRun Kouplg ChkVlv GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Eli Tee 45-Eli TeeRun Koupig ChkViv GatVlv NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3127/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE.SDF JOB TITLE: harding square unit 1 a) E 0. 0. w0 0 U H -I V U) C O)Lt) U) Lt) WC'J (OC'J a C-i (1) a) Q.c2) 0. O W-H H . HCI) VU) -. .00. 0)0. 14.4-) I-" (. (Cl HLC) HW U) In -H W U) i:1 (0• >, 0)14) 0N co 104 CQ 0. /-- / / / / / / / _I I Io r1 (N 0• Q 0 N N 0 0 0 0 0 0 0 0 0 0 0 0 0 0 L0 (1) (N rI a4 124 Ir(1)C1) ~D 124 Ir) 0.(O-r-1-- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DAT: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE. SDF JOB TITLE: harding square unit 1 WATER SUPPLY CURVE 84+ 77+ 0 \ 70+ \ x\ \ 63+ \ I \ I \ I \ P 56+ \ R I \ E I \ S I \ S 49+ \ U I \ R I \ E 42+ \ \ P I \ S I \ I 35+ \ \ \ \ 28+ \ \ I \ \ 21+ \ I * <-20.0 psi @ 1100 gpm Flow Test Point 14+ LEGEND of II I X = Required Water Supply I 65.66 psi @ 25.1 gpm 7+ I 0 = Available Water Supply U I 74.45 psi @ 25.1 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) McMahon Fire Protection P0 Box 27116 San Diego Ca. 92198 HYDRAULIC CALCULATIONS FOR Harding Square: Unit 2 3390 Harding St Carlsbad Ca. 92008 FILE NUMBER: 2017 DATE: March. 26, 2017 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R3 DENSITY: .05 gpm/sq. ft. AREA OF APPLICATION: 2 sprinklers COVERAGE PER SPRINKLER: 196 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 20.1 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR): 25.1 gpm @ 35.6 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: McMahon fire Protection DESIGN/LAYOUT BY: T. McMahon AUTHORITY HAVING JURISDICTION: City Of Carlsbad CONTRACTOR CERTIFICATION NUMBER: 884732 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: '3/28/2017 C:\PROGRAIyI FILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 74.5 20.0 1100.0 74.4 25.2 65.6 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 25.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 65.0 SOURCE 65.6 25.2 2 68.0 - - - - 57.7 - - - 3 68.0 - - - - 53.7 - - - 4 68.0 - - - - 53.5 - - - 5 68.0 - - - - 41.5 - - - 6 78.0 HOSE STREAM 33.4 5.0 7 68.0 - - - - 35.6 - - - 8 74.0 - - - - 30.3 - - - 9 78.0 - - - - 28.1 - - - 10 78.0 - - - - 25.7 - - - 11 88.0 - - - - 20.2 - - - 12 88.0 - - - - 17.6 - - - 13 98.0 - - - - 12.1 - - - 14 98.0 - - - - 11.5 - - - Si 98.0 K= 3.00 11.5 10.2 S2 98.0 K= 3.00 11.1 10.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: :3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 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 25.2 0.995 PL 30.00 PF 6.6 1 65.0 SRCE 65.6 (N/A) 10.4 150 FTG ETG PE -1.3 2 68.0 0.0 57.7 0.0 0.170 TL 39.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 68.0 0.0 57.7 0.0 4.0 psi, 25.2 gpm 3 68.0 0.0 53.7 0.0 Pipe: 3 25.2 1.025 PL 1.00 PF 0.1 3 68.0 0.0 53.7 0.0 9.8 150 FTG ---- PE 0.0 4 68.0 0.0 53.5 0.0 0.148 TL 1.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 4 68.0 0.0 53.5 0.0 12.0 psi, 25.2 gpm 5 68.0 0.0 41.5 0.0 Pipe: 5 25.2 1.380 PL 92.00 PF 3.8 5 68.0 0.0 41.5 0.0 5.4 150 FTG 4E PE -4.3 6 78.0 H.S. 33.4 5.0 0.035 TL 110.13 PV Pipe: 6 20.2 1.049 PL 15.00 PF 2.1 6 78.0 H.S. 33.4 5.0 7.5 150 FTG 3E PE 4.3 7 68.0 0.0 35.6 0.0 0.088 TL 24.07 PV Pipe: 7 20.2 1.025 PL 6.00 PF 2.7 7 68.0 0.0 35.6 0.0 7.8 150 FTG 22.0 PE -2.6 8 74.0 0.0 30.3 0.0 0.098 TL 28.00 PV Pipe: 8 20.2 1.025 PL 4.00 PF 0.4 8 74.0 0.0 30.3 0.0 7.8 150 FTG ---- PE -1.7 9 78.0 0.0 28.1 0.0 0.098 TL 4.00 PV Pipe: 9 20.2 1.101 PL 7.00 PF 2.4 9 78.0 0.0 28.1 0.0 6.8 150 FTG 28.0 PE 0.0 10 78.0 0.0 25.7 0.0 0.069 TL 35.00 PV Pipe: 10 20.2 1.101 PL 10.00 PF 1.2 10 78.0 0.0 25.7 0.0 6.8 150 FTG 7.0 PE -4.3 11 88.0 0.0 20.2 0.0 0.069 TL 17.00 PV Pipe: 11 20.2 1.101 PL 22.00 PF 2.6 11 88.0 0.0 20.2 0.0 6.8 150 FTG 16.0 PE 0.0 12 88.0 0.0 17.6 0.0 0.069 TL 38.00 PV Pipe: 12 20.2 1.101 PL 10.00 PF 1.2 12 88.0 0.0 17.6 0.0 6.8 150 FTG 7.0 PE -4.3 13 98.0 0.0 12.1 0.0 0.069 TL 17.00 PV Pipe: 13 6.0 1.101 PL 42.00 PF 0.6 13 98.0 0.0 12.1 0.0 2.0 150 FTG 34.0 PE 0.0 Si 98.0 3.0 11.5 10.2 0.007 TL 76.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE:3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 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 -4.1 1.101 PL 1.00 PF 0.0 Si 98.0 3.0 11.5 10.2 1.4 150 FTG 7.0 PE 0.0 14 98.0 0.0 11.5 0.0 0.004 TL 8.00 PV Pipe: 15 -14.1 1.101 PL 8.00 PF 0.5 14 98.0 0.0 11.5 0.0 4.8 150 FTG 7.0 PE 0.0 13 98.0 0.0 12.1 0.0 0.036 TL 15.00 PV Pipe: 16 10.0 1.101 PL 8.00 PF 0.4 14 98.0 0.0 11.5 0.0 3.4 150 FTG 14.0 PE 0.0 S2 98.0 3.0 11.1 10.0 0.019 TL 22.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 27091255 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 0.017 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.4 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 1 under full flow conditions is 74.44 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LrigEll ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G F45 El Tee RunT Kplg ChkVlv Gate 1.101 1.40 2.50 6.00 1.70 1.00 8.00 0.40 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Eli TeeRun Kouplg ChkVlv GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Ell TeeRun Kouplg ChkVlv GatVlv NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 a) E E I). 04 0 a) c'J '-'(N U). . a U)Lt) CQL() a) Q)C'.J Cfl(Ij E a) w Q) 04 C --1 .-1 WE -- HU) 0u >a) .Q 04 WQ (a Hifl -H'-1 U) r) H (I) :i a)• Y. >, UJifl r- 04 / / / / / - I 0 C C c co r- 0 C 0 0 0 C 0 • • • • • 0 0 0 0 • 0 0 0 in lzal () C'I H la, U)-'-1--- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 3/28/2017 C:\PROGRAM F'ILES\HASSDATA\HARDING SQUARE UNIT 2.SDF JOB TITLE: harding square unit 2 WATER SUPPLY CURVE 84+ 77+ 0 \ 70+ \ I \ x \ 63+ \ I \ I \ I \ P 56+ R I \ E I \ S I \ S 49+ \ U I \ R I \ E I \ 42+ \ I \ P \ S I \ I 35+ \ I \ \ 28+ \ I \ \ I \ 21+ \ I * <-20.0 psi @ 1100 gpm I Flow Test Point 14+ LEGEND I X = Required Water Supply U I 65.61 psi @ 25.2 gpm 7+ It I 0 = Available Water Supply U I 74.45 psi @ 25.2 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) McMahon Fire Protection P0 Box 27116 San Diego Ca. 92198 HYDRAULIC CALCULATIONS FOR Harding Square: Unit 3 3390 Harding St Carlsbad, Ca. 92008 FILE NUMBER: 2017 DATE: March 27, 2017 -DESIGN DATA- OCCUPANCY CLASSIFICATION: R3 DENSITY: .05 gpm/sq. ft. AREA OF APPLICATION: 2 sprinklers COVERAGE PER SPRINKLER: 196 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 2 sprinklers: Bedroom 2 TOTAL SPRINKLER WATER FLOW REQUIRED: 20.1 gpm TOTAL WATER REQUIRED (including hose): 25.1 gpm FLOW AND PRESSURE (@ BOR) : 25.1 gpm @ 35.4 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: McMahon fire Protection DESIGN/LAYOUT BY: T. McMahon AUTHORITY HAVING JURISDICTION: City of Carlsbad CONTRACTOR CERTIFICATION NUMBER: 884732 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: /28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TITLE: harding square unit 3 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 74.5 20.0 1100.0 74.5 25.1 65.8 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 25.1 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.1 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 65.0 SOURCE 65.8 25.1 2 68.0 - - - - 57.9 - - - 3 68.0 - - - - 53.9 - - - 4 68.0 - - - - 53.8 - - - 5 68.0 - - - - 41.8 - - - 6 78.0 HOSE STREAM 32.7 5.0 7 68.0 - - - - 35.4 - - - 8 74.0 - - - - 30.1 - - - 9 78.0 - - - - 28.1 - - - 10 78.0 - - - - 25.5 - - - 11 88.0 - - - - 20.0 - - - 12 88.0 - - - - 17.7 - - - 13 98.0 - - - - 12.2 - - - 14 98.0 - - - - 11.3 - - - Si 98.0 K= 3.00 11.3 10.1 S2 98.0 K= 3.00 11.1 10.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: /28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TITLE: harding square unit 3 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 25.1 0.995 PL 30.00 PF 6.6 1 65.0 SRCE 65.8 (N/A) 10.3 150 FTG ETG PE -1.3 2 68.0 0.0 57.9 0.0 0.169 TL 39.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 68.0 0.0 57.9 0.0 4.0 psi, 25.1 gpm 3 68.0 0.0 53.9 0.0 Pipe: 3 25.1 1.025 PL 1.00 PF 0.1 3 68.0 0.0 53.9 0.0 9.8 150 FTG ---- PE 0.0 4 68.0 0.0 53.8 0.0 0.147 TL 1.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 4 68.0 0.0 53.8 0.0 12.0 psi, 25.1 gpm 5 68.0 0.0 41.8 0.0 Pipe: 5 25.1 1.380 PL 120.00 PF 4.8 5 68.0 0.0 41.8 0.0 5.4 150 FTG 4E PE -4.3 6 78.0 H.S. 32.7 5.0 0.034 TL 138.13 PV Pipe: 6 20.1 1.049 PL 15.00 PF 1.6 6 78.0 H.S. 32.7 5.0 7.5 150 FTG B PE 4.3 7 68.0 0.0 35.4 0.0 0.087 TL 18.02 PV Pipe: 7 20.1 1.025 PL 6.00 PF 2.7 7 68.0 0.0 35.4 0.0 7.8 150 FTG 22.0 PE -2.6 8 74.0 0.0 30.1 0.0 0.097 TL 28.00 PV Pipe: 8 20.1 1.101 PL 4.00 PF 0.3 8 74.0 0.0 30.1 0.0 6.8 150 FTG ---- PE -1.7 9 78.0 0.0 28.1 0.0 0.069 TL 4.00 PV Pipe: 9 20.1 1.101 PL 10.00 PF 2.6 9 78.0 0.0 28.1 0.0 6.8 150 FTG 28.0 PE 0.0 10 78.0 0.0 25.5 0.0 0.069 TL 38.00 PV Pipe: 10 20.1 1.101 PL 10.00 PF 1.2 10 78.0 0.0 25.5 0.0 6.8 150 FTG 7.0 PE -4.3 11 88.0 0.0 20.0 0.0 0.069 TL 17.00 PV Pipe: 11 20.1 1.101 PL 11.00 PF 2.3 11 88.0 0.0 20.0 0.0 6.8 150 FTG 22.0 PE 0.0 12 88.0 0.0 17.7 0.0 0.069 TL 33.00 PV Pipe: 12 20.1 1.101 PL 10.00 PF 1.2 12 88.0 0.0 17.7 0.0 6.8 150 FTG 7.0 PE -4.3 13 98.0 0.0 12.2 0.0 0.069 TL 17.00 PV Pipe: 13 11.5 1.101 PL 22.00 PF 1.0 13 98.0 0.0 12.2 0.0 3.9 150 FTG 17.0 PE 0.0 Si 98.0 3.0 11.3 10.1 0.025 TL 39.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TITLE: harding square unit 3 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 1.4 1.101 PL 8.00 PF 0.0 Si 98.0 3.0 11.3 10.1 0.5 150 FTG 7.0 PE 0.0 14 98.0 0.0 11.3 0.0 0.001 TL 15.00 PV Pipe: 15 -8.6 1.101 PL 37.00 PF 1.0 14 98.0 0.0 11.3 0.0 2.9 150 FTG 31.0 PE 0.0 13 98.0 0.0 12.2 0.0 0.014 TL 68.00 PV Pipe: 16 10.0 1.101 PL 2.00 PF 0.2 14 98.0 0.0 11.3 0.0 3.4 150 FTG 7.0 PE 0.0 S2 98.0 3.0 11.1 10.0 0.019 TL 9.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 27091255 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 0.015 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 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 1 under full flow conditions is 74.44 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TITLE: harding square unit 3 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkViv BfyVlv GatVlv AlmChk DPVlv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G F45 El Tee RunT Kplg ChkViv Gate 1.101 1.40 2.50 6.00 1.70 1.00 8.00 0.40 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Eli TeeRun Kouplg ChkVlv GatVlv NPTee 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Eli Tee 45-Eli TeeRun Koupig ChkViv GatVlv NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TI1TLE: harding square unit 3 W 04 0. C-) a) 0). u)Lc) U)L() (0 a) e') (1) (11 E U) U) Q.U)) 0. -- Z 00) >(1) .00. 0)0. 44.1-) C!) (0 HLf) 4-1 -,-1,--1 0) ) H' Cl) (1 (0 • 0'. >, >-.p (U(S) r- D ft 7-- / / / / / / C-.-' 0 0 c co 0 0 0 0 0 0 c 0 C) C 0 0 if) IV (y) (N 0(!)E)) 01r)U)U) D 124 C.) QU) -H - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE; 3/28/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT3.SDF JOB TITLE: harding square unit 3 WATER SUPPLY CURVE 84+ 77+ 0 \ 70+ \ x\ I \ 63+ \ I \ I \ I \ P 56+ \ R I \ E I S \ S 49+ \ U \ R I \ E \ 42+ \ \ P \ S \ I 35+ \ I \ \ \ 28+ \ \ I \ \ 21+ \ I * <-20.0 Psi @ 1100 gpm Flow Test Point 14+ LEGEND U II I X = Required Water Supply U I 65.81 psi @ 25.1 gpm 7+ I 0 = Available Water Supply I 74.45 psi @ 25.1 gpm 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) McMahon Fire Protection P0 Box 27116 San Diego Ca. 92198 HYDRAULIC CALCULATIONS FOR Harding square: Unit 4 3390 Harding St Carlsbad Ca. 92008 FILE NUMBER: 2017 DATE: march 27, 2017 -DESIGN DATA- OCCUPANCY CLASSIFICATION: DENSITY: AREA OF APPLICATION: COVERAGE PER SPRINKLER: NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: R3 05 gpm/sq. ft. 2 sprinklers 196 sq. ft. 2 sprinklers: Bedroom 2 20.0 gpm TOTAL WATER REQUIRED (including hose): 25.0 gpm FLOW AND PRESSURE (@ BOR) : 25.0 gpm @ 36.1 psi SPRINKLER ORIFICE SIZE: 7/16 inch NAME OF CONTRACTOR: McMahon fire Protection DESIGN/LAYOUT BY: T. McMahon AUTHORITY HAVING JURISDICTION: City Of Carlsbad CONTRACTOR CERTIFICATION NUMBER: 884732 C-16 CALCULATIONS BY HASS COMPUTER PROGRAM HRS SYSTEMS, INC. SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 3727/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) 1 74.5 20.0 1100.0 74.5 25.0 66.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 25.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 20.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 65.0 SOURCE 66.5 25.0 2 68.0 - - - - 58.6 - - - 3 68.0 - - - - 54.6 - - - 4 68.0 - - - - 54.4 - - - 5 68.0 - - - - 42.4 - - - 6 78.0 HOSE STREAM 33.4 5.0 7 68.0 - - - - 36.1 - - - 8 74.0 - - - - 30.8 - - - 9 78.0 - - - - 28.8 - - - 10 78.0 - - - - 25.9 - - - 11 88.0 - - - - 20.4 - - - 12 88.0 - - - - 17.9 - - - 13 98.0 - - - - 12.4 - - - 14 98.0 - - - - 11.4 - - - 51 98.0 K= 3.00 11.1 10.0 S2 98.0 K= 3.00 11.2 10.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 3>'27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 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 25.0 0.995 PL 30.00 PF 6.6 1 65.0 SRCE 66.5 (N/A) 10.3 150 FTG ETG PE -1.3 2 68.0 0.0 58.6 0.0 0.169 TL 39.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 68.0 0.0 58.6 0.0 4.0 psi, 25.0 gpm 3 68.0 0.0 54.6 0.0 Pipe: 3 25.0 1.025 PL 1.00 PF 0.1 3 68.0 0.0 54.6 0.0 9.7 150 FTG ---- PE 0.0 4 68.0 0.0 54.4 0.0 0.146 TL 1.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE 4 68.0 0.0 54.4 0.0 12.0 psi, 25.0 gpm 5 68.0 0.0 42.4 0.0 Pipe: 5 25.0 1.380 PL 120.00 PF 4.7 5 68.0 0.0 42.4 0.0 5.4 150 FTG 4E PE -4.3 6 78.0 H.S. 33.4 5.0 0.034 TL 138.13 PV Pipe: 6 20.0 1.049 PL 15.00 PF 1.6 6 78.0 H.S. 33.4 5.0 7.4 150 FTG E PE 4.3 7 68.0 0.0 36.1 0.0 0.086 TL 18.02 PV Pipe: 7 20.0 1.025 PL 6.00 PF 2.7 7 68.0 0.0 36.1 0.0 7.8 150 FTO 22.0 PE -2.6 8 74.0 0.0 30.8 0.0 0.097 TL 28.00 PV Pipe: 8 20.0 1.101 PL 4.00 PF 0.3 8 74.0 0.0 30.8 0.0 6.7 150 FTG ---- PE -1.7 9 78.0 0.0 28.8 0.0 0.068 TL 4.00 PV Pipe: 9 20.0 1.101 PL 15.00 PF 2.9 9 78.0 0.0 28.8 0.0 6.7 150 FTG 28.0 PE 0.0 10 78.0 0.0 25.9 0.0 0.068 TL 43.00 PV Pipe: 10 20.0 1.101 PL 10.00 PF 1.2 10 78.0 0.0 25.9 0.0 6.7 150 FTG 7.0 PE -4.3 11 88.0 0.0 20.4 0.0 0.068 TL 17.00 PV Pipe: 11 20.0 1.101 PL 15.00 PF 2.5 11 88.0 0.0 20.4 0.0 6.7 150 FTG 22.0 PE 0.0 12 88.0 0.0 17.9 0.0 0.068 TL 37.00 PV Pipe: 12 20.0 1.101 PL 10.00 PF 1.2 12 88.0 0.0 17.9 0.0 6.7 150 FTG 7.0 PE -4.3 13 98.0 0.0 12.4 0.0 0.068 TL 17.00 PV Pipe: 13 11.1 1.101 PL 28.00 PF 1.0 13 98.0 0.0 12.4 0.0 3.7 150 FTG 17.0 PE 0.0 14 98.0 0.0 11.4 0.0 0.023 TL 45.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 3127/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 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 -8.9 1.101 PL 42.00 PF 1.0 14 98.0 0.0 11.4 0.0 3.0 150 FTG 25.0 PE 0.0 13 98.0 0.0 12.4 0.0 0.015 TL 67.00 PV Pipe: 15 10.0 1.101 PL 6.00 PF 0.2 14 98.0 0.0 11.4 0.0 3.4 150 FTG 7.0 PE 0.0 51 98.0 3.0 11.1 10.0 0.019 TL 13.00 PV Pipe: 16 10.0 1.101 PL 4.00 PF 0.2 14 98.0 0.0 11.4 0.0 3.4 150 FTG 7.0 PE 0.0 S2 98.0 3.0 11.2 10.0 0.019 TL 11.00 PV NOTES (HASS) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 27091255 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 0.005 gpm and a maximum imbalance at any node of 0.074 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 10.3 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 1 under full flow conditions is 74.44 psi compared to the minimum required pressure of 20.00 psi. PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEil ChkVlv BfyVlv GatVlv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 2.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 PAGE: F MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) F E T R K C G F45 El Tee RunT Kplg ChkVlv Gate 1.101 1.40 2.50 6.00 1.70 1.00 8.00 0.40 PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Eli Tee 45-Eli TeeRun Koupig ChkVlv GatViv NPTee 0.995 2.00 6.00 1.00 2.00 0.00 6.00 0.00 6.00 PAGE: L MATERIAL: CT-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R K C G N Ell Tee 45-Eli TeeRun Koupig ChkVlv GatViv NPTee 1.025 3.00 7.00 1.00 2.00 0.00 7.00 0.00 7.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 ci) 14 Q. 0. 0 I-i ci) C) o Ci) • 0 CuLt) CuLt) fo Q)N U) C14 E c-c II) ci) 0., l-ct2) 0. o 0)-H -H Z HO) 10u .00. '1)(2. 1-14-) U) (0 HLO I-c HLt) U) Ir) -HCu U) :1 (0• lJ•.. 0)00 '-4. FCC N W 0.01 0. / / / / / /- - I U, ('4 C C C C C C C C C r-1 C C 0 C 0 C C C C C N ¼I LI) () (N 11 U)0x) flU)U,0x) O.U)4— SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 3/27/2017 C:\PROGRAM FILES\HASSDATA\HARDING SQUARE UNIT 4.SDF JOB TITLE: harding square unit 4 WATER SUPPLY CURVE 84+ 77+ 0 \ 70+ \ \ 63+ \ I \ I \ \ P 56+ \ R I \ E I \ S I \ S 49+ \ U I \ R I \ E I \ 42+ \ I \ P I \ S I \ I 35+ \ I \ I \ 28+ I \ I \ \ 21+ I * <-20.0 psi 8 1100 gpm I Flow Test Point 14+ LEGEND I, I X = Required Water Supply 66.45 psi 8 25.0 gpm 7+ I 0 = Available Water Supply 11 I 74.45 psi 8 25.0 gpm it + ------+ --------+ --------+ ---------+ -----------+ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)