Loading...
The URL can be used to link to this page
Your browser does not support the video tag.
Home
My WebLink
About
7047 CORINTIA ST; ; AS100070; Permit
3f7/24,1:46 PM ASI 00070 Permit Data City of Carlsbad Sprinkler Permit Job Address: 7047 CORINTIA ST Permit Type: SPRINK Parcel No: 2237921400 Lot #: 0 Reference No.: Permit No: AS100070 Status: ISSUED Applied 5/26/2010 Approved: 5/26/2010 Issued: 5/26/2010 PC #: Inspector: Project Title: ORDWAY RESIDENCE TWO RESIDENTIAL FIRE SPRINKLER INSPECTIONS @ $65/EA Applicant: INNOVATIVE FIRE PROTECTION SUITE 101 8779 COTTONWOOD AV SANTEE, CA (619) 593-8200 (619)593-9133 Owner: ORDWAY GRIFFIN&VASILIEVAYULIA REVOCABLE TRUST 0 2424 CAMINO OLEADA SAN CLEMENTE CA Fees ($) Add'l Fees ($) Total ($) Balance ($) 130 0 130 0 about:blank 1/1 .LJ SPRINKLER.SYSTEM HYDRAULIC ANALYSIS Page 1 DATE 5/18/2010 C:\HASS74\C4351.SDF JOB ITLE ORDWAY RESIDENCE TWO HEAD CALC-2nd FLOOR WATER SUPPLY DATA SOURCE NODE TAG 1 STATIC RESID. PRESS. PRESS. @ (PSI) (PSI) 49.0 45.0 FLOW AVAIL. TOTAL REQ'D PRESS. 0 DEMAND PRESS. (GPM) (PSI) (GPM) (PSI) 500.0 49.0 31.2 20.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 20.0 31.2 2 0.0 - - - - 13.9 - - - 2A 0.0 - - - - 9.9 - - - B 0.0 - - - - 9.1 - - - P 0.0 - - - - 35.3 - - - U.1 0.0 HOSE STREAM 33.6 5.0 3 0.5 - - - 33.1 - - - 4 3.5 - - - - 30.1 - - - 5 10.5 - - - - 20.5 - - - 6 21.5 - -. - - 14.3 - - - 7 21.5 - - - - 11.4 - - - 8 21.5 - - - - 9.7 - - - 8A 21.0 K= 4.30 9.5 13.2 9A 21.0 K= 4.30 9.1 13.0 10 21.5 - - - - 13.9 - - - 11 13.0 - - - - 18.0 - - - 12 11.0 - - - - 19.0 - - - 13 11.0 - - - - 19.0 - - - 13A 10.5 - - - - 19.2 - - - 14A 10.5 - - - - 19.2 - - - 15 11.0 - - - - 19.0 - - - APftQED AS SUBMTTED CRL$BADFFRE DEPAJMENT These plans have been reviewed for apparent compliance with the current applicable codes aiid-itandardsin force in the jurisdiction. The owner or contractor may utilize this il review in support of an application for a building perittil with the express understanding that this review in no way, relieves the owner or contractor or their professipnal engineer or ahhect for sole nsponsihility for lull compliance with said codes and standards. including the huilding;txxle oribr any sponsihilty foI deficiencies. ror.o,iiiioni-or negligence in these platis whether or not noted ii this review. Dutc577//O Rviéwer() 10 RE.64WENDAPPROVAl- 13, RECOMMENI) APPROVAL. AS NOTED SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 5/18/2010 : c:\HAss74\c4351.sDF JOB ftTLE: ORDWAY RESIDENCE TWO HEAD CALC-2nd FLOOR 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 31.2 0.995 PL 15.00 PF 6.1 1 0.0 SRCE 20.0 (N/A) 12.9 150 FTG TG. PE 0.0 2 0.0 0.0. 13.9 0.0 0.254 TL 24.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 13.9 0.0 4.0 psi, 31.2 gpm 2A 0.0 0.0 9.9 0.0. Pipe: 3 31.2 2.050 PL 90.00 PF 0.8 2A 0.0 0.0 9.9 0.0 3.0 150 FTG 5L PE 0.0 B 0.0 0.0 9.1 0.0 0.008 TL 105.00 PV Pipe: 4 FIRE PUMP Rating: 31.0 gpm @ 65.0 psi B 0.0 0.0 9.1 0.0 Avail.: 31.2 gpm @ 64.7 psi P 0.0 0.0 35.3 0.0 Req'd.: 31.2 gpm @ 26.2 psi Pipe: 5 31.2 2.050 PL 185.00 PF 1.7 P 0.0 0.0 35.3 0.0 3.0 150 FTG E9L PE 0.0 U.1 0.0 H.S. 33.6 5.0 0.008 TL 220.00 PV Pipe: 6 .26.2 1.985 PL 10.00 PF 0.3 U.l 0.0 R.S. 33.6 5.0 2.7 150 FTG T3LC PE -0.2 . 3 0.5 0.0 33.1 0.0 0.006 TL 51.00 PV Pipe: 7 26.2 1.049 PL 3.00 PF 17 3 0.5 0.0 33.1 0.0 9.7 120 FTG C PE -1.3 4 3.5 0.0 30.1 0.0 0.215 TL 8.00 PV Pipe: 8 26.2 1.101 PL 29.00 PF 6.5 4 3.5 0.0 30.1 0.0 8.8 150 FTG 2E3T PE -3.0 5 10.5 0.0 20.5 0.0 0.112 TL 58.00 PV Pipe: 9 19.0 1.101 PL 10.50 PF 1.5 5 10.5 0.0 20.5 0.0 6.4 150 FTG ET2R PE -4.8 6 21.5 0.0 14.3 0.0 . 0.062 TL 24.50 PV Pipe: LO 14.9 1.101 PL 47.00 PF 2.9 6 . 21.5 0.0 14.3 0.0 5.0 150 FTG 2ET7R PE 0.0 7 21.5 0.0 11.4 0.0 0.040 TL 73.00 PV Pipe: ii . 26.2 1.101 PL 9.00 PE' 1.7 7 21.5 0.0 11.4 0.0 8.8 150 FTG TR PE 0.0 8 21.5 0.0 9.7 0.0 0.112 TL 15.00 PV Pipe: 12 . 13.2 1.101 PL 1.50 PF 0.5 8 21.5 0.0 9.7 0.0 4.5 150 FTG ETR PE 0.2 8A 21.0 4.3 9.5 13.2 0.032 TL 14.50 PV HYDRAULIC ANALYSIS SPRINKLER SYSTEM Page 3 DATE: 5/18/2010 C:\HASS74\C4351.SDF JOB T'tTLE: ORDWAY RESIDENCE TWO HEAP CALC-2nd FLOOR 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 13.0 1.101 PL 10.00 PF 0.8 8 21.5 0.0 9.7 0.0 4.4 150 FTG 2ER PE 0.2 9A 21.0 4.3 9.1 13.0 0.031 TL 25.00 PV Pipe: 14 -11.3 1.101 PL 54.00 PF 2.5 7 21.5 0.0 11.4 0.0 3.8 150 FTG 6ET6R PE 0.0 10 21.5 0.0 13.9 0.0 0.024 TL 107.00 PV Pipe: 15 -4.0 1.101 PL 72.00 PF 0.4 10 21.5 0.0 13.9 0.0 1.4 150 FTG E3T9R PE 0.0 6 21.5 0.0 14.3 0.0 0.004 TL 103.00 PV Pipe: 16 -7.3 1.101 PL 19.50 PF 0.4 10 21.5 0.0 13.9 0.0 2.4 150 FTG 3E2R PE 3.7 11 13.0 0.0 18.0 0.0 0.010 TL 42.50 PV Pipe: 17 -1.3 1.101 PL 86.00 PF 0.1 11 13.0 0.0 18.0 0.0 0.4 150 FTG 7E4T PE 0.9 12 11.0 0.0 19.0 0.0 0.000 TL 155.00 PV Pipe: 18 . 0.0 1.101 PL 2.00 PF 0.0 12 11.0 0.0 19.0 0.0 0.0 150 FTG T PE 0.0 13 11.0 0.0 19.0 0.0 0.000 TL 7.00 PV Pipe: 19 0.0 1.101 PL 5.00 PF 0.0 13 11.0 0.0 19.0 0.0 0.0 150 FTG ETR PE 0.2 13A .10.5 0.0 19.2 0.0 0.000 TL 18.00 PV Pipe: 20 0.0 1.101 PL 11.00 PF 0.0 13 11.0 0.0 19.0 0.0 0.0 150 FTG 2ER PE 0.2 14A 10.5 0.0 19.2 0.0 0.000 TL 26.00 PV Pipe: 21 -1.3 1.101 PL 99.50 PF 0.1 12 11.0 0.0 19.0 0.0 0.4 150 FTG 9E5T PE 0.0 15 11.0 0.0 19.0 0.0 0.000 TL 187.50 PV Pipe: 22 . 6.0 1.101 PL 14.50 PF 0.1 15 11.0 0.0 19.0 0.0 2.0 L50 FTG TR PE -0.9 11 13.0 0.0 . 18.0 0.0 0.007 TL 20.50 PV Pipe: 23 -7.3 1.101 PL 68.00 PF 1.3 15 11.0 0.0 19.0 0.0 2.4 L50 FTG 5E4T PE 0.2 5 10.5 0.0 20.5 0.0 0.010 TL 123.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2010 S C:\HASS74\C4351.SDF JOB 'IITLE: ORDWAY RESIDENCE TWO HEAD CALC-2nd FLOOR NOTES (HASS): Calculations were performed by the HASS 8.0 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 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 0.002 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.9 ft/sec at pipe 1. The Minimum pump suction pressure under maximum calculated demand is 9.12 (psi) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCL-140 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 1.00 1.00 PAGE: 1-1 MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.985 8.00 15.00 3.00 17.00 2.00 2.00 0.00 0.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet in) E T L C B G A D Eli Tee 2.050 8.00 15.00 3.00 17.00 9.00 2.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 5/18/2010 C:\HASS74\C4351.SDF JOB TITLE: ORDWAY RESIDENCE TWO HEAD CALC-2nd FLOOR PAGE: K MATERIAL: CPPR-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee L 0.995 2.00 6.00 1.50 0.00 0.00 3.00 0.00 0.00 Static: 49.00 psi Resid: 45.00 psi Flow: 500.0 gpm 120.1 100 -14.7 LEGEND Pressure available at source 48.98 psi @ 31.2 gpm Pressure required at source 20.00 psi @ 31.2 .gpm 19 Pressure available from pump 64.73 psi @ 31.2 gpm Pressure required from pump 26.18 psi @ 31.2 gpm Total Pressure avail- able at pump dschg. 102.83 psi @ 31.2 gpm Total Pressure re- quired at pump dschg. 35.30 psi @ 31.2 gpm I A. Source Supply Curve B. Net Pump Supply Curve I I I C. Pump Discharge Curve 20C300 400 500 600 700. 800 900 100CD. System Demand Curve * FLOW (GPM) Available at Source Available at Pump Suction G A 80.0 U G E 3 p 60.0 R E 1 40.0 U R 6 E 4 2020 p S 1 0.0 SPRINKLER SYSTEM-HYDRAULIC ANALYSIS Page 1 DATE: 5/18/2010 C:\HASS74\C4351.SDF JOB ¶IITLE: ORDWAY RESIDENCE TWO HEAD CALC-STUDY - - 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 49.0 45.0 500.0 49.0 31.2 20.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 31.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE . 20.0 31.2 2 0.0 - - - - 13.9 - - - 2A 0.0 - - - - 9.9 - - - B 0.0 - - - - 9.1 - - - P 0.0 - - - - 34.2 - - - 0.1 0.0 HOSE STREAM 32.6 5.0 3 0.5 - - - - 32.0 - - - 4 3.5 - - - 29.0 - - - 5 10.5 - - - - 19.5 - - - 6 21.5 - - - - . 13.9 - - - 7 21.5 - - - - 13.4 - - - 8 21.5 - - - - 13.4 - - - 8A 21.0 - - - - 13.6 - - - 9A 21.0 - - - - 13.6 - - - 10 21.5 - - - - 12.7 - - - 11 13.0 - - - - 14.9 - - - 12 11.0 - - - - 10.5 - - - 13 11.0 - - - - 9.7 - - - 13A 10.5 K= 4.30 9.4 13.2 14A 10.5 . K= 4.30 9.1 13.0 15 11.0 - - - - 15.8 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE 5/18/2010 C:\HASS74\C435.1.SDF JOB -TITLE: ORDWAY RESIDENCE TWO HEAD CALC-STUDY : 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 31.2 0.995 PL 15.00 PF 6..1 1 0.0 SRCE 20.0 (N/A) 12.9 150 FTG TG PE 0.0 2 0.0 0.0 13.9 0.0 0.253 TL 24.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 13.9 0.0 4.0 psi, 31.2 gpm 2A 0.0 0.0 9.9 0.0: Pipe: 3 31.2 2.050 PL 90.00 PF 0.8 2A 0.0 0.0 9.9 0.0 3.0 150 FTG 5L PE 0.0 B 0.0 0.0 9.1 0.0. 0.007 TL 105.00 PV Pipe: 4 FIRE PUMP Rating: 31.0 gpm @ 65.0 psi B 0.0 0.0 9.1 0.0 Avail.: 31.2 gpm @ 64.7 psi P 0.0 0.0 34.2 0.0 Req'd. : 31.2 gpm @ 25.1 psi Pipe: 5 31.2 2.050 PL 185.00 PF 1.6 P 0.0 0.0 34.2 0.0 3.0 150 FTG E9L PE 0.0 U.1 0.0 H.S. 32.6 5.0 0.007 TL 220.00 PV Pipe: 6 26.2 1.985 PL . 10.00 PF 0.3 0.1 0.0 H.S. 32.6 5.0 2.7 150 FTG T3LC PE -0.2 3 0.5 0.0 32.0 0.0 0.006 TL 51.00 PV Pipe: 7 26.2 1.049 PL 3.00 PF 1.7 3 0.5 0.0 32.0 0.0 9.7 120 FTG C PE -1.3 4 3.5 0.0 29.0 0.0 0.214 TL 8.00 PV Pipe: 8 26.2 1.101 PL 29.00 PE' 6.5 4 3.5 0.0 29.0 0.0 8.8 150 FTG 2E3T PE -3.0 5 - 10.5 0.0 19.5 0.0 0.112 TL 58.00 PV Pipe: 9 13.7 1.101 PL 10.50 PE' 0.8 5 10.5 0.0 19.5 0.0 4.6 150 FTG ET2R PE -4.8 6 21.5 0.0 13.9 0.0 0.034 TL . 24.50 PV Pipe: 10 5.8 1.101 PL 47.00 PE' 0.5 6 V 21.5 0.0 L 3.9 0.0 2.0 150 FTG 2ET7R PE 0.0 7 21.5 0.0 13.4 0.0 0.007 TL 73.00 PV Pipe: 11 0.0 1.101 PL 9.00 PE' 0.0 7 21.5 0.0 13.4 0.0 0.0 150 FTG TR PE 0.0 8 21.5 0.0 13.4 0.0 0.000 TL 15.00 PV Pipe: 12 0.0 1.101 PL 1.50 PE' 0.0 8 21.5 0.0 13.4 0.0 0.0 150 FTG ETR PE 0.2 8A 21.0 0.0 13.6 0.0 0.000 TL 14.50 PV t." -- •- .' - .- -. -rt'----- -r '" -. --t'rr - -- SPRINKLER SYSTEM HYDRAULIC PNALYSIS Page 3 DATE 5/18/2010 - C:\HASS74\C435l.SDF JOB TITLE: 'ORDWA-Y RESIDENCE TWO HEAD: -STUDY - 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 ' 10.00 PF 0.0 8 21.5 0.0 13.4 0.0 0.0 150 FTG 2ER PE 0.2 9A 21.0 0.0 13.6 0.0 0.000 TL 25.00 PV Pipe: 14 5.8 1.101 PL 54.00 PF 0.7 7 21.5 0.0 13.4 0.0 2.0 150 FTG 6ET6R PE 0.0 10 21.5 0.0 12.7 0.0 - 0.007 TL 107.00 PV Pipe: 15 - -7.9 1.101 PL 72.00 FE' 1.2 10 21.5 0.0' 12.7 0.0, 2.6 150 FTG E3T9R FE 0.0 6 21.5 0.0 13.9 0.0 0.012 TL 103.00 PV Pipe: 16 13.7 1.101 FL 19.50 PF 1.4 10 21.5 0.0 12.7 0.0 4.6 150 FTG 3E2R PE 3.7 11 13.0 0.0 14.9 0.0 0.034 TL 42.50 PV Pipe: 17 13.8 1.101 FL 86.00 FE' 5.3 11 13.0 0.0 14.9 0.0 4.6 150 FTG 7E4T PE 0.9 12 11.0 0.0 10.5 0.0 0.034 TL 155.00 PV 'Pipe: 18 26.2 1.101 FL 2.00 PF 0.8 12 11.0 0.0 10.5 0.0 8.8 150 FTG T PE 0.0 13 11.0 0.0 9.7 .0.0 0.112 TL 7.00 PV Pipe: 19 13.2 1.101 PL .5.00 FE' 0.6 13 11.0 0.0 9.7 0.0 4.4 150 FTG ETR FE 0.2 13A 10.5 4.3 9.4 13.2 0.031 TL 18.00 PV Pipe: 20 13.0 1.101 FL 11.00 FE 0.8 13 11.0 0.0 9.7 0.0 4.4 150 FTG 2ER FE 0.2 14A 10.5 4.3 9.1 13.0 0.031 TL 26.00 PV Pipe: 21 -12.4 1.101 FL 99.50 FE' 5.3 12 11.0 0.0 10.5 0.0 4.2 150 FTG 9E5T PE 0.0 15 11.0 0.0 15.8 0.0 0.028 TL 187.50 PV Pipe: 22 . 0.1 1.101 PL 14.50 FE' 0.0 15 11.0 0.0 15.8 0.0 0.0 150 FTG TR FE -0.9 11 13.0 0.0 14.9 0.0 0.000 TL 20.50 PV Pipe: 23 -12.5 1.101 FL . 68.00 FE' 3.5 15 11.0 0.0 15.8 0.0 4.2 150 FTG 5E4T FE 0.2 5 10.5 0.0 19.5 0.0 0.028 TL 123.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 5/18/2010 . C:\HASS74\C4351.SDF JOB TITLE: ORDWAY RESIDENCE TWO HEAD CALC-STUDY NOTES (HASS): Calculations were performed by the HASS 8.0 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 The system has been calculated to provide an average imbalance at each node of 0.007 gpm and a maximum imbalance at anynode of 0.062 gpm. Total pressure at each node is. used in balancing the system. Maximum water velocity is 12.9 ft/sec at pipe 1. The Minimum pump suction pressure under maximum calculated demand is 9.14 (psi) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 1.00 1.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 PAGE: I MATERIAL: CPPR-L HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.985 8.00 15.00 3.00 17.00 2.00 2.00 0.00 0.00 PAGE: J MATERIAL: S40PVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A 0 Eli Tee 2.050 8.00 15.00 3.00 17.00 9.00 2.00 0.00 0.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS - Page 5 DATE 5/18/2010 C:\HASS74.\C-4351.:SDF JOB TITLE: ORDWAY RESIDENCE TWO HEAD CALC-STUDY PAGE: K MATERIAL: CPPR-K }IWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee L 0.995 2.00 6.00 1.50 0.00 0.00 3.00 0.00 0.00 Static: 49.00 psi Resid: 45.00 psi Flow: 500.0 gpm 120. LEGEND 100 Pressure available at source 48.98 psi @ 31.2 gpm -14.7 Pressure - required at source 20.00 psi @ 31.2 gpm Pressure available from pump 64.73.psi @ 31.2 gpm Pressure required from pump 25.07 psi @ 31.2 gpm Total Pressure avail- able at pump dschg. 102.85 psi @ 31.2 gpm Total Pressure re- quired at pump dschg. 34.21 psi @ 31.2 gpm Source SuppLy Curve Net Pump Supply Curve I I I I C. Pump Discharge Curve 20C300 400 500 600 700 800 900 100CD. System Demand Curve FLOW (GPM) Available at Source Available at Pump Suction G A 80.0 U G E 3 P 60.0 R E S 1 S 40.0 U R 6 E 4 2020 P S i 0.0 ---f - WATERUPPLY- DATA - . - -. SOURCE STATIC RESID. FLOW -NODE - ---PRESS.- -PRESS. @ TAG (PSI) (PSI) (GPM) 1 49.0 .45.0 500.0 - AVAIL TOTAL REQ'D PRESS. .-@ DEMAND PRESS. (PSI)......(.GPM) -. .(PSI) 49.0 31 -3 20.0 U AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1 31.3 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 5.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 26.3 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 0.0 SOURCE 20.0 . 31.3 2 0.0 - - - - 13.9 2A 0.0 - - - - . 9.9 - - - 0.0 - - - - 9.1 - - - P 0.0 - - - - 32.8 0.1 0.0 HOSE STREAM 31.1 5.0 3A 0.5 - - - - 30.6 - - - 4 - 3.5 - - - - 27.6 - - - 5 10.0 - - - - - 18.6 6 21.5 - - - - 10.6 7 21.5 - - - - 9.5 - - - 7A 21.0 K= 4.30 9.1 13.0 8 21.5 - - - - 9.5 - - - 8A 21.0 K= 4.30 9.5 13.2 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: 1 31.3 0.995 PL 15.00 PF 6.1 1 0.0 SRCE 20.0 (N/A) 12.9 150 FTG TG PE 0.0 2 0.0 0.0 13.9 0.0 0.254 TL 24.00 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE 2 0.0 0.0 13.9 0.0 4.0 psi,. 31.2 gpm 2A 0.0 0.0 9.9 0.0. Pipe: 3 31.3 2.050 PL 90.00 PF 0.8 2A 0.0 0.0 9.9 0.0 3.0 150 FTG 5L PE 0.0 B 0.0 0.0 9.1 0.0 0.008 TL 105.00 PV Pipe: 4 FIRE PUMP Rating: 31.0 gpm @ 65.0 psi B 0.0 0.0 9.1 0.0 Avail.: 31.3 gpm @ 64.6 psi P 0.0 0.0 32.8 0.0 Req'd.: 31.3 gpm @ 23.7 psi Pipe: 5 31.3 2.050 PL 185.00 PF 1.7 P 0.0 0.0 32.8 0.0 3.0 150 FTG E9L PE 0.0 U.1 0.0 H.S. 31.1 5.0 0.008 TL 220.00 PV Pipe: 6 26.3 1.985 PL 10.00 PF 0.3 U.1 0.0 H.S. 31.1 5.0 2.7 150 FTG T3LC PE -0.2 3A 0.5 0.0 30.6 0.0 0.006 TL 51.00 PV Pipe: 7 26.3 1.049 PL 3.00 PF 1.7 3A 0.5 0.0 30.6 0.0 9.7 120 FTG C PE -1.3 4 3.5 0.0 27.6 0.0 0.215 TL 8.00 PV Pipe: 8 26.3 1.101 PL 30.00 PE 6.2 4 3.5 0.0 27.6 0.0 8.8 150 FTG 3E4R PE -2.8 5 10.0 0.0 18.6 0.0 0.113 TL 55.00 PV Pipe: 9 26.3 1.101 PL 13.00 PF 3.0 5 10.0 0.0 18.6 0.0 8.8 150 FTG ET2R PE -5.0 6 21.5 0.0 10.6 0.0 0.113 TL 27.00 PV Pipe: 10 14.4 1.101 PL 14.50 PF 1.1 6 21.5 0.0 10.6 0.0 4.9 150 FTG ET2R PE 0.0 7 21.5 0.0 9.5 0.0 0.037 TL 28.50 PV Pipe: 11 13.0 1.101 PL 5.50 PF 0.6 7 21.5 0.0 9.5 0.0 4.4 150 FTG ETR PE 0.2 .7A 21.0 4.3 9.1 13.0 0.031 TL 18.50 PV Pipe: 12 1.4 1.101 PL 8.00 PF 0.0 7 21.5 0.0 9.5 0.0 0.5 150 FTG E PE 0.0 8 21.5 0.0 9.5 0.0 0.001 TL 15.00 PV _fa DAX Ti . . . - . . .. . •-• - ., PIPE TAG Q (GPM) DIA(IN) LENGTH -END - ELEV NOZ PT DISC VEL-(FPS)HW(C)--. (FT) - NODES (FT) (K) (PSI) (GPM) FL/FT - - Pipe 13 i:37.1'2- 101 PL 0.50 8 - .21.5 0.0 9.5 0.0 -4.5- 150 FTG, TR 8A 21.0 4.3 9.5 132-..........0.032 TL 6.50 1 C -GH PRESS. SUM. - (PSI) .... -- PF 0.2 PE 0.2 PV - - Pipe: 14. -11.8 1.101 PL 28.50 PF 1.1 8 21.5 0.0 9.5 0.0 4.0 150 FTG . E6R PE 0.0 6 21.5 0.0 10.6 0.0 0.026 TL 41.50 PV NOTES (HASS): Calculations were performed by the HASS 8'.0 computer program under license no. 16080621 granted by FIRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 The system has been calculated to provide an average imbalance at each node of 0.008 gpm and a maximum imbalance at any node of 0.049 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 12.9 ft/sec at pipe 1. The Minimum pump suction pressure under maximum calculated demand is 9.11 (psi) PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D Eli Tee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 1.00 1.00 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E . T R K C L B L Eli Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 Diaiaétér. Equivalent FittiiigLèngthsin Feet (in) E T L C B G A - -• Efl• Tee , • - 1.985 8.00 15.00 3.00 17.00. 2.00 2.00 '0.00 PAGE: J MATERIAL: S40PVC HWC:-150- Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Eli Tee 2.050 8.00 15.00 3.00 17.00. 9.00 2.00 0.00 PAGE: K MATERIAL: CPPR-K HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G Eli Tee L 0.995 2.00 6.00 1.50 0.00 0.00 3.00 0.00 D 0.00 D 0..00 Static 49 00 psi Res-id: -45.00. psi Flow 500.0 gpm 120.0 LEGEND 100 A Pressure available at source 48.98 psi @31.3gpm G A 80. Pressure required U at source G 20.00 psi @ 31.3 gpm E 3 Pressure available p 60. )L from pump R 64.64 psi @ 31.3 gpm E Pressure required S 40. )L from pump U 23.69 psi @ 31.3 gpm R E Total Pressure avail- able at pump dschg. 20 102.73 psi @ 31.3 gpm Total Pressure re- quired at pump dschg. 32.79 psi @ 31.3 gpm 0. Source Supply Curve Net Pump Supply Curve -14.7 II I I I I I 1 1 I I C P"m fl 4 r' h r rT 20C300 400 500 600 700 800 900 100CD. System Demand Curve FLOW (GPM) Available at Source Available at Pump Suction 55+ 50+ 0\\\\\ I \\\\\\ I \\\\\\ 45+ * <-45.0 psi @ 500 gpm I Flow Test Point P 40+ R I E I S I S35+ U I R I E I 30+ ( I P I S I I 25+ ) I 20X 15+ 10+ LEGEND I X = Required Water Supply 20.00 psi @ 31.3 gpm 5+ •lt I 0 = Available Water Supply 48.98 psi @ 31.3 gpm 0+------+----+-----+------+--------+--------+---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM)