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2433 JEFFERSON ST; ; AS140080; Permit
9/14/22, 11 :05 AM AS 140080 Permit Data City of Carlsbad Sprinkler Permit Job Address: 2433 JEFFERSON ST Permit Type: SPRINK Parcel No: 1551404100 Lot#: 0 Reference No.: Permit No: AS140080 Status: ISSUED Applied 3/12/2014 Approved: 3/29/2014 Issued: 3/29/2014 PC #: Inspector: Project Title: DE ANDA RESIDENCE NEW 13D RESIDENTIAL FIRE SPRINKLER SYSTEM FOR 4052# TWO STORY SINGLE FAMILY RESIDENCE Applicant: INNOVATIVE FIRE PROTECTION INC STE 101 8779 COTTONWOOD AV SANTEE CA (619) 593-8200 (619)593-9133 Fees($) Add'I Fees ($) 605 0 about:blank Owner: ANDA VERONICA D 1409 TURQUOISE DR CARLSBAD CA Total($) 605 Balance($) 0 1 /1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA lHD.SDF JOB TITLE: C5301 DE ANDA 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 68.4 63.9 500.0 68.4 26.0 57.2 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 26.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 21. 0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 57.2 26.0 2 0.0 ----48.7 2A 0.0 44.7 D 0.0 43.4 C 0.0 37.4 3A 0.0 ----36.6 3B 1. 5 HOSE STREAM 34.8 5.0 3 3.5 ----32.5 4 6.5 30.1 5 9.0 ----25.3 6 9.0 ----25.3 7 9.0 ----25.1 8 9.0 ----25.1 9 19.0 ----19.9 10 19.0 ----19.3 l0A 18.0 K= 4.90 18.4 21. 0 11 19.0 ----19.3 llA 18.0 ----19.7 12 19.0 ----19.5 12A 18.0 ----19.9 13 19.0 20.4 AS140080 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA lHD.SDF JOB TITLE: C5301 DE ANDA 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 26.0 0.995 PL 40.00 PF 8.5 1 0.0 SRCE 57.2 (N/A) 10.7 150 FTG TG PE 0.0 2 0.0 0.0 48.7 0.0 0.181 TL 47.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 48.7 0.0 4.0 psi, 26.0 gprn 2A 0.0 0.0 44.7 0.0 Pipe: 3 26.0 0.995 PL 3.00 PF 1. 3 2A 0.0 0.0 44.7 0.0 10.7 150 FTG 2E PE 0.0 D 0.0 0.0 43.4 0.0 0.181 TL 7.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE D 0.0 0.0 43.4 0.0 6.0 psi, 26.0 gprn C 0.0 0.0 37.4 0.0 Pipe: 5 26.0 1.610 PL 30.00 PF 0.8 C 0.0 0.0 37.4 0.0 4 .1 150 FTG 2L2E PE 0.0 3A 0.0 0.0 36.6 0.0 0.017 TL 48.00 PV Pipe: 6 26.0 1. 265 PL 10.00 PF 1.1 3A 0.0 0.0 36.6 0.0 6. 6 150 FTG ET PE -0.6 3B 1. 5 H.S. 34.8 5.0 0.056 TL 19.00 PV Pipe: 7 21. 0 1.055 PL 10.00 PF 1. 5 3B 1. 5 H.S. 34.8 5.0 7.7 150 FTG 2E PE -0.9 3 3.5 0.0 32.5 0.0 0.092 TL 16.00 PV Pipe: 8 21. 0 1.049 PL 3.00 PF 1.1 3 3.5 0.0 32.5 0.0 7.8 120 FTG C PE -1. 3 4 6.5 0.0 30.1 0.0 0.142 TL 8.00 PV Pipe: 9 21. 0 1.101 PL 33.00 PF 3.6 4 6.5 0.0 30.1 0.0 7.1 150 FTG EB4R PE -1.1 5 9.0 0.0 25.3 0.0 0.074 TL 49.00 PV Pipe: 10 6.0 1.101 PL 4.00 PF 0.1 5 9.0 0.0 25.3 0.0 2.0 150 FTG B PE 0.0 6 9.0 0.0 25.3 0.0 0.007 TL 9.00 PV Pipe: 11 2.7 1.101 PL 49.00 PF 0.1 6 9.0 0.0 25.3 0.0 0.9 150 FTG 2EB5R PE 0.0 7 9.0 0.0 25.1 0.0 0.002 TL 73.00 PV Pipe: 12 2.7 1.101 PL 26.00 PF 0.1 7 9.0 0.0 25.1 0.0 0.9 150 FTG E2R PE 0.0 8 9.0 0.0 25.1 0.0 0.002 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA lHD.SDF JOB TITLE: C5301 DE ANDA 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 -3.3 1.101 PL 42.00 PF 0.2 8 9.0 0.0 25.1 0.0 1.1 150 FTG 34.0 PE 0.0 6 9.0 0.0 25.3 0. 0 0.002 TL 76.00 PV Pipe: 14 6.0 1.101 PL 72. 00 PF 0.9 8 9.0 0.0 25.1 0.0 2.0 150 FTG 6E7R PE -4.3 9 19.0 0.0 19.9 0.0 0.007 TL 121.00 PV Pipe: 15 12.8 1.101 PL 14.00 PF 0.6 9 19.0 0.0 19.9 0.0 4.3 150 FTG BR PE 0.0 10 19.0 0.0 19.3 0.0 0.030 TL 20.00 PV Pipe: 16 21. 0 1.101 PL 5.00 PF 1. 3 10 19.0 0.0 19.3 0.0 7.1 150 FTG EBR PE 0.4 l0A 18.0 4.9 18.4 21. 0 0.074 TL 18.00 PV Pipe: 17 -8.2 1.101 PL 3.00 PF 0.0 10 19.0 0.0 19.3 0. 0 2.8 150 FTG PE 0.0 11 19.0 0.0 19.3 0.0 0.013 TL 3.00 PV Pipe: 18 0.0 1.101 PL 8.00 PF 0.0 11 19.0 0.0 19.3 0.0 0.0 150 FTG EBR PE 0.4 llA 18.0 0.0 19.7 0.0 0.000 TL 21. 00 PV Pipe: 19 -8.2 1.101 PL 12.00 PF 0.2 11 19.0 0.0 19.3 0.0 2.8 150 FTG R PE 0.0 12 19.0 0.0 19.5 0.0 0.013 TL 13.00 PV Pipe: 20 0.0 1.101 PL 9.00 PF 0.0 12 19.0 0.0 19.5 0.0 0.0 150 FTG EBR PE 0.4 12A 18.0 0.0 19.9 0.0 0.000 TL 22.00 PV Pipe: 21 -8.2 1.101 PL 49.00 PF 0.9 12 19.0 0.0 19.5 0.0 2.8 150 FTG EB9R PE 0.0 13 19.0 0.0 20.4 0.0 0.013 TL 70.00 PV Pipe: 22 -15.0 1.101 PL 10.00 PF 0.6 13 19.0 0.0 20.4 0.0 5.1 150 FTG B PE 4.3 5 9.0 0.0 25.3 0.0 0.040 TL 15.00 PV Pipe: 23 6.8 1.101 PL 42.00 PF 0.5 13 19.0 0.0 20.4 0.0 2.3 150 FTG EB4R PE 0.0 9 19.0 0.0 19.9 0.0 0.009 TL 58.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA lHD.SDF JOB TITLE: C5301 DE ANDA NOTES (HASS) : (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (2) The system has been calculated to provide an average imbalance at each node of 0.007 gpm and a maximum imbalance at any node of 0.138 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 10.7 ft/sec at pipe 1. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (5) Available pressure at source node 1 under full flow conditions is 68.38 psi compared to the minimum required pressure of 20.00 psi. (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A Diameter (in) 1.049 PAGE: E Diameter (in) 1.610 PAGE: F Diameter (in) 1.101 MATERIAL: S40 HWC: 120 Equivalent Fitting Lengths in T L C B Feet G A E Ell 2.00 Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 5.00 2.00 5.00 6.00 1.00 10.00 MATERIAL: PVC150 HWC: 150 E Ell 6.00 Equivalent Fitting Lengths in Feet T L C B G Tee LngEll ChkVlv BfyVlv GatVlv 8.00 3.00 14.00 7.00 3.00 MATERIAL: CPVC HWC: 150 L 45 1.00 Equivalent Fitting Lengths in E B R C El BrT RunT Cplg 7.00 5.00 1.00 1.00 Feet s SwCk 8.00 N NPTee 11. 00 G Gate 2.00 D DPVlv 10.00 N NPTee 5.00 J SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 , DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA lHD.SDF JOB TITLE: C5301 DE ANDA PAGE: K MATERIAL: CT-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C s G N Ell Tee 45-Ell TeeRun Couplg SwgChk 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 C s G N Ell Tee 45-Ell TeeRun Couplg SwgChk GatVlv NPTee 1. 265 3.00 6.00 1.00 2.00 0.50 7.00 0.00 6.00 PAGE: M MATERIAL: CT-M HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T F R C s G N Ell Tee 45-Ell TeeRun Couplg SwgChk GatVlv NPTee 1.055 3.00 8.00 2.00 3.00 0.00 8.00 0.00 8.00 G A u G E p R E s s u R E p s i 80.0 70. 0 1 60.0 50.0 40.0 30.0 20.0 10.0 0. 0 -14.7 5 CJO WATER SUPPLY ANALYSIS Static: 68.40 psi Resid: 63.90 psi Flow: 500.0 gprn --------------------- 6 CJO 7 CJO 8 CJO 1 ~~E~liP1able pressure II 68.38 psi@ 26.0 gprn 21 ----- Required pressure 57.18 psi@ 26.0 gprn A. Source Supply Curve B. System Demand Curve . --------- 9CJO I( y t:J 0 >' tJj 1-3 t:x:l 1-3 •• H 1-3 N t-i ........... t:x:l u, .. ........... N () 0 u, f--1 w ~ 0 f--1 t:J t:x:l >' (/) z tu t:J ~ >' H z ~ t-i t:x:l ~ (/) f-<: (/) 1-3 t:x:l 3:: ::r: f-<: t:J ~ C: () t-i .. H /() ::r: >' >' (/) z (/) >' 00 t-i w f-<: / (/) () H u, U) w 0 f--1 t:J t:x:l >' z 0 >' f--1 ::r: tu 0 PJ \.Q (/) (D 0 h:J m 1000 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 f DATE : 2 / 5 / 2 014 JOB TITLE: C5301 DE ANDA WATER SUPPLY CURVE 72+ I 0\\\\\ I \\\\\\ 66+ \\\\\\ C:\HASS83\C5301 DE ANDA lHD.SDF I * <-63.9 psi@ 500 gpm I Flow Test Point I 60+ I X I 54+ I I I P 48+ R I E I s I S 42+ u I R I E I 36+ I P I s I I 30+ ) I I I 24+ I I I 18+ I I I============================== 12+ I I X I 6+ LEGEND Required Water Supply 57.18 psi@ 26.0 gpm I O = Available Water Supply I 68.38 psi@ 26.0 gpm I " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 \. DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA 2HD.SDF JOB TITLE: C5301 DE ANDA 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 68.4 63.9 500.0 68.4 31. 0 53.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31. 0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 53.5 31. 0 2 0.0 41. 7 2A 0.0 ----37.7 D 0.0 ----36.0 C 0.0 30.0 3A 0.0 ----28.8 3B 1. 5 HOSE STREAM 26.7 5.0 3 3.5 23.6 4 6.5 ----20.6 5 9.0 ----14.1 6 9.0 14.0 7 9.0 ----13.9 8 9.0 13. 8 9 19.0 ----8.2 10 19.0 ----7.4 l0A 18 .0 ----7.8 11 19.0 7.3 llA 18.0 K= 4.90 7.1 13.0 12 19.0 ----7.3 12A 18.0 K= 4.90 7.0 13.0 13 19.0 ----8.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA 2HD.SDF JOB TITLE: C5301 DE ANDA 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 31. 0 0.995 PL 40.00 PF 11. 8 1 0.0 SRCE 53.5 (N/A) 12.8 150 FTG TG PE 0.0 2 0.0 0.0 41. 7 0.0 0.251 TL 47.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 41. 7 0.0 4.0 psi, 31. 0 gpm 2A 0.0 0.0 37.7 0.0 Pipe: 3 31. 0 0.995 PL 3.00 PF 1. 8 2A 0.0 0.0 37.7 0. 0 12.8 150 FTG 2E PE 0.0 D 0.0 0.0 36.0 0.0 0.251 TL 7.00 PV Pipe: 4 FIXED PRESSURE LOSS DEVICE D 0.0 0.0 36.0 0.0 6.0 psi, 31. 0 gpm C 0.0 0.0 30.0 0.0 Pipe: 5 31. 0 1.610 PL 30.00 PF 1. 2 C 0.0 0.0 30.0 0.0 4.9 150 FTG 2L2E PE 0.0 3A 0.0 0.0 28.8 0.0 0.024 TL 48.00 PV Pipe: 6 31. 0 1. 265 PL 10.00 PF 1. 5 3A 0.0 0.0 28.8 0.0 7.9 150 FTG ET PE -0.6 3B 1.5 H.S. 26.7 5.0 0.078 TL 19.00 PV Pipe: 7 26.0 1.055 PL 10.00 PF 2.2 3B 1. 5 H.S. 26.7 5.0 9.6 150 FTG 2E PE -0.9 3 3.5 0.0 23.6 0.0 0 .136 TL 16.00 PV Pipe: 8 26.0 1.049 PL 3.00 PF 1. 7 3 3.5 0.0 23.6 0.0 9.7 120 FTG C PE -1. 3 4 6.5 0.0 20.6 0.0 0.212 TL 8.00 PV Pipe: 9 26.0 1.101 PL 33.00 PF 5.4 4 6.5 0. 0 20.6 0.0 8.8 150 FTG EB4R PE -1.1 5 9.0 0.0 14.1 0.0 0 .111 TL 49.00 PV Pipe: 10 7.2 1.101 PL 4.00 PF 0.1 5 9.0 0.0 14.1 0.0 2.4 150 FTG B PE 0.0 6 9.0 0.0 14.0 0.0 0.010 TL 9.00 PV Pipe: 11 3.3 1.101 PL 49.00 PF 0.2 6 9.0 0.0 14.0 0.0 1.1 150 FTG 2EB5R PE 0.0 7 9.0 0.0 13.9 0.0 0.002 TL 73.00 PV Pipe: 12 3.3 1.101 PL 26.00 PF 0.1 7 9.0 0.0 13. 9 0.0 1.1 150 FTG E2R PE 0.0 8 9.0 0.0 13. 8 0.0 0.002 TL 35.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 \. DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA 2HD.SDF JOB TITLE: C5301 DE ANDA 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 -3.9 1.101 PL 42.00 PF 0.3 8 9.0 0.0 13.8 0.0 1. 3 150 FTG 34.0 PE 0.0 6 9.0 0.0 14.0 0.0 0.003 TL 76.00 PV Pipe: 14 7.2 1.101 PL 72. 00 PF 1. 2 8 9.0 0.0 13.8 0.0 2.4 150 FTG 6E7R PE -4.3 9 19.0 0.0 8.2 0.0 0.010 TL 121.00 PV Pipe: 15 14.9 1.101 PL 14.00 PF 0.8 9 19.0 0.0 8.2 0.0 5.0 150 FTG BR PE 0.0 10 19.0 0.0 7.4 0.0 0.040 TL 20.00 PV Pipe: 16 0.0 1.101 PL 5.00 PF 0.0 10 19.0 0.0 7.4 0.0 0.0 150 FTG EBR PE 0.4 l0A 18.0 0.0 7.8 0.0 0.000 TL 18.00 PV Pipe: 17 14.9 1.101 PL 3.00 PF 0.1 10 19.0 0.0 7.4 0.0 5.0 150 FTG PE 0.0 11 19.0 0.0 7.3 0.0 0.040 TL 3.00 PV Pipe: 18 13. 0 1.101 PL 8.00 PF 0.6 11 19.0 0.0 7.3 0. 0 4.4 150 FTG EBR PE 0.4 llA 18.0 4.9 7.1 13.0 0.031 TL 21.00 PV Pipe: 19 1. 9 1.101 PL 12.00 PF 0.0 11 19.0 0.0 7.3 0.0 0.6 150 FTG R PE 0.0 12 19.0 0.0 7.3 0.0 0.001 TL 13.00 PV Pipe: 20 13. 0 1.101 PL 9.00 PF 0.7 12 19.0 0.0 7.3 0.0 4. 4 150 FTG EBR PE 0.4 12A 18.0 4.9 7.0 13.0 0.031 TL 22.00 PV Pipe: 21 -11.1 1.101 PL 49.00 PF 1. 6 12 19.0 0.0 7.3 0. 0 3.7 150 FTG EB9R PE 0.0 13 19.0 0.0 8. 9 0. 0 0.023 TL 70.00 PV Pipe: 22 -18.8 1.101 PL 10.00 PF 0.9 13 19.0 0.0 8.9 0.0 6.3 150 FTG B PE 4.3 5 9.0 0.0 14.1 0.0 0.061 TL 15.00 PV Pipe: 23 7.7 1.101 PL 42.00 PF 0.7 13 19.0 0.0 8.9 0.0 2.6 150 FTG EB4R PE 0.0 9 19.0 0.0 8.2 0.0 0.012 TL 58.00 PV ., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 i DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA 2HD.SDF JOB TITLE: C5301 DE ANDA NOTES (HASS): (1) Calculations were performed by the HASS 8.4 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 (2) 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 0.023 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 12.8 ft/sec at pipe 1. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (5) Available pressure at source node 1 under full flow conditions is 68.36 psi compared to the minimum required pressure of 20.00 psi. (6) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: A Diameter (in) 1.049 PAGE: E Diameter (in) 1.610 PAGE: F Diameter (in) 1.101 MATERIAL: S40 HWC: 120 E Ell 2.00 Equivalent Fitting Lengths in Feet T L C B G A Tee LngEll ChkVlv BfyVlv GatVlv AlmChk 5.00 2.00 5.00 6.00 1.00 10.00 MATERIAL: PVC150 HWC: 150 E Ell 6.00 Equivalent Fitting Lengths in T L C B Feet G Tee LngEll ChkVlv BfyVlv GatVlv 8.00 3.00 14.00 7.00 3.00 MATERIAL: CPVC HWC: 150 Equivalent Fitting Lengths in Feet L E B R C s 45 El BrT RunT Cplg SwCk 1. 00' 7.00 5.00 1.00 1.00 8.00 N NPTee 11. 00 G Gate 2.00 D DPVlv 10.00 N NPTee 5.00 ., SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 2/5/2014 C:\HASS83\C5301 DE ANDA 2HD.SDF JOB TITLE: C5301 DE ANDA PAGE: K Diameter (in) 0.995 PAGE: L Diameter (in) 1. 265 PAGE: M Diameter (in) 1.055 MATERIAL: CT-K HWC: 150 E Ell 2.00 Equivalent Fitting Lengths in T F R C Feet s G Tee 45-Ell TeeRun Couplg SwgChk GatVlv 6.00 1.00 2.00 0.00 6.00 0.00 MATERIAL: CT-L HWC: 150 E Ell 3.00 Equivalent Fitting Lengths in Feet T F R C S G Tee 45-Ell TeeRun Couplg SwgChk GatVlv 6.00 1.00 2.00 0.50 7.00 0.00 MATERIAL: CT-M HWC: 150 E Ell 3.00 Equivalent Fitting Lengths in Feet T F R C S G Tee 45-Ell TeeRun Couplg SwgChk GatVlv 8.00 2.00 3.00 0.00 8.00 0.00 N NPTee 6.00 N NPTee 6.00 N NPTee 8.00 G A u G E p R E s s u R E p s i 80.0 70. 0 1 60.0 2 50.0 40.0 30.0 20 .0 10 .0 0 .0 -14.7 2 ero 3 ero 4 ero WATER SUPPLY ANALYSIS Static: 68.40 psi Resid: 63.90 psi Flow: 500.0 gpm --------------------- 5 era 6 era 7 ero s era 1 ~~E~,tiP1able pressure 1' 68.37 psi@ 31.0 gpm 21 ----- Required pressure 53.53 psi@ 31.0 gpm A. Source Supply Curve B. System Demand Curve . --------- 9 ero "'- y t:l 0 >' lJ:J 1-3 l:rj 1-3 •• H 1-3 N t-4-........ l:rj u, .. -........ N () 0 u, f-' w~ 0 f-' t:l l:rj >' z t:l >' 1000 C/) hj ~ H z ~ t-4 l:rj ~ C/) i-< C/) 1-3 l:rj 8:: ::i:: i-< t:l ~ >' C: () t-4 •• H / () ::i:: >' >' C/) z C/) >' CX) t-4 w i-< / C/) () H u, C/) w 0 f-' t:l l:rj >' z t:l >' N ::i:: hj t:l OJ • I.Q C/) (1) t:l rrj<J'I J, SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 2/5/2014 JOB TITLE: C5301 DE ANDA WATER SUPPLY CURVE 72+ I 0\\\\\ I \\\\\\ 66+ \\\\\\ C:\HASS83\C5301 DE ANDA 2HD.SDF I * <-63.9 psi@ 500 gpm I Flow Test Point I 60+ I I I 54X I I I P 48+ R I E I s I S 42+ u I R I E I 36+ I P I s I I 30+ ) I I I 24+ I I I 18+ I I I============================== 12+ I I X I 6+ LEGEND Required Water Supply 53.53 psi@ 31.0 gpm I O = Available Water Supply I 68.37 psi@ 31.0 gpm I II " 0++-+---+----+-----+------+--------+--------+---------+-----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM)