Loading...
The URL can be used to link to this page
Your browser does not support the video tag.
Home
My WebLink
About
4980 AVENIDA ENCINAS; ; AS040088; Permit
City of Carlsbad Sprinkler Permit Permit No: AS040088 4980 AVEN IDA Job Address: Status: ISSUED ENCINAS Permit Type: SPRINK Applied 6/15/2004 Parcel No: 2100110200 Approved: 7/6/2004 Lot #: 0 Reference No.: Issued: 7/6/2004 PC #: Inspector: Project Title: CANNON COURT RESTAURANT FIRE SPRINKLER PLAN CHECK & INSPECTIONS Applicant: Owner: WESTERN STATES FIRE PROTECTION SUITE 201 9550 CHESAPEAKE DR. SAN DIEGO, CA 858-769-4900 Fees ($) Add'I Fees ($) Total ($) Balance ($) 46925 0 46925 0 Western States Fire Protection Co. 9550 Chesapeake Drive, Suite 201 San Diego, California 92123 iiA Phone (858) 769-4900 • Fax (858) 769-4920 www.wsfn.com _n 3 -~7 -56 9 Fire Protection Systems Design Fabrication • Installation Commercial • Residential • Industrial • Institutional Special Hazards High Tech • Defense. Hangars Retrofit • Service• Inspection • Maintenance 1 Lic. No. C16-488359 = 1-tyd4a&i&' C&c,&tvW C aviyoi't' C 0wt 9 etcttunt CITY OF CARLSBAD FIRE DEPARTMENT APPROVED Subject to field inspection and requfc1 tests, notations hereon, conditions In correspondence and conformance tIi applicable regulations. The stamping of these plane shelf not bo h1d to or aPpco)the violation of cay t By Dats1/i tHu ASo400go Albuquerque, NM • Anaheim. CA • Austin, TX • Colorado Springs, CO Da as, ecaiu . e Cr, • Port Worth, TX • Hossion, TX • Kansas City, KS Las Vegas, NV • Phoenix, AZ . Portland, OR - Rapid City, SD • San Antonio, TX • San Diego. CA • Seattle, WA • Spokane, WA • St. Louis, MO Locations Across Canada (Vipond Fire Protection Inc.) Western States Fire Protection Co. 9550 Chesapeake Drive SUite 201 San Diego CA 92123 HYDRAULIC CALCULATIONS FOR Cannon Court Restaurant Kitchen Area FILE NUMBER: DATE: JUN 2, 2004 -DESIGN DATA- OCCUPANCY CLASSIFICATION: Kitchen - Ordinary Group 1 DENSITY: .15 gpm/sq. ft. AREA OF APPLICATION: Kitchen Area COVERAGE PER SPRINKLER: 96 sq. ft. NUMBER OF SPRINKLERS CALCULATED: TOTAL SPRINKLER WATER FLOW REQUIRED: TOTAL WATER REQUIRED (including hose) FLOW AND PRESSURE (@ BOR) SPRINKLER ORIFICE SIZE: 13 sprinklers 236.5 gpm 486.5 gpm 236.5 gpm @ 29.1 psi 1/2 inch AUTHORITY HAVING JURISDICTION: Carlsbad Fire Department CONTRACTOR CERTIFICATION NUMBER: CA Lisc. C16-488359 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 5004004430) HRS SYSTEMS, INC. TUCKER, GA 30084 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/2/2004 C:\HASS75\CANNONKITCHF.SDF JOB TITLE: Cannon Kitchen WATER SUPPLY DATA ,0SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 97.0 80.0 693.0 88.2 486.5 33.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 486.5 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 236.5 GPM NODE ANALYSIS DATA NODE TAG ELEVATION (FT). 1 11.0 2 11.0 3 11.0 4 11.0 5 11.0 11.0 7 11.0 8 14.0 9 11.0 10 11.0 11 11.0 12 11.0 13 11.0 14 11.0 15 11.0 16 11.0 17 11.0 18 14.0 19 14.0 20 1.0 21 2.0 22 2.0 SOURCE 0.0 NODE TYPE PRESSURE DISCHARGE (PSI) (GPM) K= 5.60 7.0 14.8 K= 5.60 7.6 15.4 K= 5.60 8.2 16.0 K= 5.60 9.5 17.2 K= 5.60 11.8 19.2 K= 5.60 13.6 20.6 - - - - 18.0 - - - - - - - 22.0 - - - K= 5.60 16.6 22.8 K= 5.60 9.6 17.3 K= 5.60 10.4 18.0 K= 5.60 11.2 18.7 K= 5.60 12.9 20.1 - - - - 13.3 - - - K= 5.60 9.8 17.5 K= 5.60 11.0 18.6 - - - - 19.4 - - - - - - - 22.2 - - - - - - - 22.9 - - - - - - - 29.1 - - - - - - - 29.0 - - - - - - - 32.0 - - - SOURCE 33.1 236.5 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/2/2004 C:\HASS75\CANNONKITCHF.SDF JOB TITLE: Cannon Kitchen 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 -36.1 1.380 PL 13.50 PF 2.3 16 11.0 5.6 11.0 18.6 7.7 120 FTG ET PE 0.0 14 11.0 0.0 13.3 0.0 0.102 TL 22.50 PV Pipe 15 -110.2 1.610 PL 12.00 PF 6.1 14 11;0 0.0 13.3 0.0 17.4 120 FTG E PE 0.0 17 11.0 0.0 19.4 0.0 0.380 TL 16.00 PV Pipe: 16 -110.2 1.610 PL 3.00 PF 4.2 17 11.0 0.0 19.4 0.0 17.4 120 FTG T PE -1.3 18 14.0 0.0 22.2 0.0 0.380 TL 11.00 PV Pipe: 17 -126.2 3.260 PL 12.00 PF 0.2 8 14.0 0.0 22.0 0.0 4.9 120 FTG ---- PE 0.0 18 14.0 0.0 22.2 0.0 0.016 TL 12.00 PV Pipe: 18 -236.5 3.260 PL 4.50 PF 0.7 18 14.0 0.0 22.2 0.0 9.1 120 FTG E PE 0.0 19 14.0 0.0 22.9 0.0 0.050 TL 13.91 PV Pipe:. 19 -236.5 4.260 PL 13.00 PF 0.6 19 14.0 0.0 22.9 0.0 5.3 120 FTG C PE 5.6 LI'7 1.0 0.0 29.1 0.0 0.014 TL 41.97 PV .JQ\ Pipe: 20 -236.5 6.065 PL 70.00 PF 0.3 1.0 0.0 29.1 0.0 2.6 150 FTG 4ET PE -0.4 2.0 0.0 29.0 0.0 0.002 TL 199.95 PV Pipe: 21 FIXED PRESSURE LOSS DEVICE 2.0 0.0 32.0 0.0 3.0 psi, 236.5 gpm 2.0 0.0 29.0 0.0 Pipe: 22 -236.5 6.065 PL 60.00 PF 0.2 2.0 0.0 32.0 0.0 2.6 150 FTG ETG PE 0.9 SOURCE 0.0 SRCE 33.1 (N/A) 0.002 TL 131.02 PV NOTES: Calculations were performed by the HASS 7.5 computer program under license no. 5004004430 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 The system has been calculated to provide an average imbalance at each node of 0.006 gpm and a maximum imbalance at any node of 0.134 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 19.9 ft/sec at pipe 8. VA SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/2/2004 C:\HASS75\CANNONKITCHF.SDF JOB TITLE: Cannon Kitchen 10 (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * 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 GatViv AlmChk DPViv NPTee 3.260 9.41 20.16 6.72 21.50 13.44 1.34 17.47 17.47 20.16 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 26.33 26.33 PAGE: A MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyVlv GatViv AlmChk DPViv NPTee 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 10.00 5.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 10.00 6.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 10.00 8.00 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 P-j 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/2/2004 C:\HASS75\CANNONKITCHFSDF JOB TITLE: Cannon Kitchen CD CD I (N N . C C C C C C C C C C C C C C (N C U) WU)( P R E S S U R E SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/2/2004 C:\HASS75\CANNONKITCHFSDF JOB TITLE: Cannon Kitchen WATER SUPPLY CURVE (S 108+ 99+ *\\\\ I \\\\\ \\\\\ 90+ \\\\ I 0 \\\\\ I \\\\\ I \\\\ 81+ * <-80.0 psi 8 693 gpm Flow Test Point 72+ 63+ 54+ 45+ 36+ I x 27+ 18+ LEGEND I 'I I X = Required Water Supply I 33.11 psi @ 486.5 gpm 9+ I 0 = Available Water Supply I 88.17 psi 8 486.5 gpm 'I 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/2/2004 C:\HASS75\CANNONKITCHF.SDF JOB TITLE: Cannon Kitchen PIPE DATA SPIPE 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 -14.8 1.049 PL 8.00 PF 0.6 1 11.0 5.6 7.0 14.8 5.5 120 FTG ---- PE 0.0 2 11.0 5.6 7.6 15.4 0.075 TL 8.00 PV Pipe: 2 -30.3 1.380 PL 8.00 PF 0.6 2 11.0 5.6 7.6 15.4 6.5 120 FTG ---- PE 0.0 3 11.0 5.6 8.2 16.0 0.074 TL 8.00 PV Pipe: 3 -46.3 1.380 PL 8.00 PF 1.3 3 11.0 5.6 8.2 16.0 9.9 120 FTG ---- PE 0.0 4 11.0 5.6 9.5 17.2 0.162 TL 8.00 PV Pipe: 4 -63.5 1.380 PL 8.00 PF 2.3 4 11.0 5.6 9.5 17.2 13.6 120 FTG ---- PE 0.0 5 11.0 5.6 11.8 19.2 0.290 TL 8.00 PV Pipe: 5 -82.8 1.610 PL 8.00 PF 1.8 5 11.0 5.6 11.8 19.2 13.0 120 FTG ---- PE 0.0 6 11.0 5.6 13.6 20.6 0.223 TL 8.00 PV Pipe: 6 -103.4 1.610 PL 5.00 PF 4.4 11.0 5.6 13.6 20.6 16.3 120 FTG T PE 0.0 7 11.0 0.0 18.0 0.0 0.337 TL 13.00 PV Pipe: 7 -22.8 1.049 PL 3.00 PF 1.3 9 11.0 5.6 16.6 22.8 8.5 120 FTG T PE 0.0 7 11.0 0.0 18.0 0.0 0.166 TL 8.00 PV Pipe: 8 -126.2 1.610 PL 3.00 PF 5.4 7 11.0 0.0 18.0 0.0 19.9 120 FTG T PE -1.3 8 14.0 0.0 22.0 0.0 0.488 TL 11.00 PV Pipe: 9 -17.3 1.049 PL 8.00 PF 0.8 10 11.0 5.6 9.6 17.3 6.4 120 FTG ---- PE 0.0 11 11.0 5.6 10.4 18.0 0.100 TL 8.00 PV Pipe: 10 -35.4 1.380 PL 8.00 PF 0.8 11 11.0 5.6 10.4 18.0 7.6 120 FTG ---- PE 0.0 12 11.0 5.6 11.2 18.7 0.098 TL 8.00 PV Pipe: 11 -54.1 1.380 PL 8.00 PF 1.7 12 11.0 5.6 11.2 18.7 11.6 120 FTG ---- PE 0.0 13 11.0 5.6 12.9 20.1 0.216 TL 8.00 PV Pipe: 12 -74.2 1.380 PL 1.00 PF 0.4 13 11.0 5.6 12.9 20.1 15.9 120 FTG ---- PE 0.0 . 4 11.0 0.0 13.3 0.0 0.387 TL 1.00 PV Pipe: 13 -17.5 1.049 PL 12.00 PF 1.2 15 11.0 5.6 9.8 17.5 6.5 120 FTG ---- PE 0.0 16 11.0 5.6 11.0 18.6 0.102 TL 12.00 PV Western States Fire Protection Co. 9550 Chesapeake Drive San Diego CA 92123 HYDRAULIC CALCULATIONS S FOR Cannon Court Restaurant Dining Room Area FILE NUMBER: DATE: JUN 1, 2004 -DESIGN DATA- OCCUPANCY CLASSIFICATION: Light Hazard DENSITY: -' .10 gpm/sq. ft. AREA OF APPLICATION: 1,950 sq. ft. COVERAGE PER SPRINKLER: 64 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 31 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 600.2 gpm TOTAL WATER REQUIRED (including hose) : 700.2 gpm FLOW AND PRESSURE (@ BOR) : 600.2 gpm @ 63.7 psi SPRINKLER ORIFICE SIZE: 1/2 inch Light Hazard Dining Room Area. .10 GPM over 1,500 plus 30 percent remote area increase to 1,950 for slope ceiling. Calculated with minimum 7 PSI end sprinkler pressure per NFPA 13. AUTHORITY HAVING JURISDICTION: CONTRACTOR CERTIFICATION NUMBER: CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 5004004430) HRS SYSTEMS, INC. TUCKER, GA 30084 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant WATER SUPPLY DATA *SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SOURCE 97.0 80.0 693.0 AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 79.7 700.2 70.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 700.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 600.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 15.5 K= 5.60 9.8 17.5 2 15.5 K= 5.60 10.6 18.2 3 15.5 K= 5.60 11.4 18.9 4 15.5 K= 5.60 13.1 20.3 5 15.5 K= 5.60 14.6 21.4 15.5 K= 5.60 17.0 23.1 7 15.5 K= 5.60 20.5 25.4 8 14.0 - - - - 31.5 - - - 9 20.5 K= 5.60 8.2 16.0 10 20.5 K= 5.60 8.9 16.7 11 20.5 K= 5.60 9.6 17.3 12 20.5 K= 5.60 11.1 18.6 13 20.5 K= 5.60 12.3 19.7 14 20.5 K= 5.60 14.3 21.2 15 20.5 K= 5.60 17.3 23.3 16 14.0 - - - - 31.7 - - - 17 25.5 K= 5.60 7.0 14.8 18 25.5 K= 5.60 7.6 15.4 19 25.5 K= 5.60 8.2 16.0 20 25.5 K= 5.60 9.5 17.2 21 25.5 K= 5.60 10.6 18.2 22 25.5 K= 5.60 12.3 19.7 23 25.5 K= 5.60 14.9 21.6 24 14.0 - - - - 32.2 - - - 25 25.5 K= 5.60 7.3 15.1 26 25.5 K= 5.60 7.9 15.8 27 25.5 K= 5.60 8.5 16.4 28 25.5 K= 5.60 9.9 17.6 29 25.5 K= 5.60 11.0 18.6 30 25.5 K= 5.60 12.8 20.0 25.5 K= 5.60 15.5 22.1 .1 2 14.0 - - - - 33.3 - - - 33 20.5 K= 5.60 18.0 23.8 34 20.5 K= 5.60 19.5 24.7 35 20.5 K= 5.60 20.9 25.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant NODE ANALYSIS DATA SNODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 20.5 - - - - 24.0 - - - 37 20.5 - - - - 25.4 - - - 38 20.5 - - - - 26.9 - - - 39 20.5 - - - - 28.3 - - - 40 14.0 - - - - 35.1 - - - 41 14.0 - - - - 54.8 - - - 42 1.0 - - - - 63.7 - - - 43 2.0 - - - - 65.0 - - - 44 2.0 - - - - 68.0 - - - SOURCE 0.0 SOURCE 70.1 600.2 S 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant PIPE DATA *PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 1 -17.5 1.049 PL 8.00 PF 0.8 1 15.5 5.6 9.8 17.5 6.5 120 FTG ---- PE 0.0 2 15.5 5.6 10.6 18.2 0.102 TL 8.00 PV Pipe: 2 -35.7 1.380 PL 8.00 PF 0.8 2 15.5 5.6 10.6 18.2 7.7 120 FTG ---- PE 0.0 3 15.5 5.6 11.4 18.9 0.100 TL 8.00 PV Pipe: 3 -54.6 1.380 PL 8.00 PF 1.8 3 15.5 5.6 11.4 18.9 11.7 120 FTG ---- PE 0.0 4 15.5 5.6 13.1 20.3 0.219 TL 8.00 PV Pipe: 4 -74.9 1.610 PL 8.00 PF 1.5 4' 15.5 5.6 13.1 20.3 11.8 120 FTG ---- PE 0.0 5 15.5 5.6 14.6 21.4 0.186 TL 8.00 PV Pipe: 5 -96.3 1.610 PL 8.00 PF 2.4 5 15.5 5.6 14.6 21.4 15.2 120 FTG ---- PE 0.0 6 15.5 5.6 17.0 23.1 0.296 TL 8.00 PV Pipe: 6 -119.4 1.610 PL 8.00 PF 3.5 15.5 5.6 17.0 23.1 18.8 120 FTG ---- PE 0.0 7 15.5 5.6 20.5 25.4 0.440 TL 8.00 PV Pipe: 7 -144.8 1.610 PL 4.50 PF 10.4 7 15.5 5.6 20.5 25.4 22.8 120 FTG ET PE 0.6 8 14.0 0.0 31.5 0.0 0.629 TL 16.50 PV Pipe: 8 -16.0 1.049 PL 8.00 PF 0.7 9 20.5 5.6 8.2 16.0 6.0 120 FTG ---- PE 0.0 10 20.5 5.6 8.9 16.7 0.086 TL 8.00 PV Pipe: 9 -32.7 1.380 PL 8.00 PF 0.7 10 20.5 5.6 8.9 16.7 7.0 120 FTG ---- PE 0.0 11 20.5 5.6 9.6 17.3 0.085 TL 8.00 PV Pipe: 10. -50.0 1.380 PL 8.00 PF 1.5 11 20.5 5.6 9.6 17.3 10.7 120 FTG ---- PE 0.0 12 20.5 5.6 11.1 18.6 0.187 TL 8.00 PV Pipe: 11 -68.7 1.610 PL 8.00 PF 1.3 12 20.5 5.6 11.1 18.6 10.8 120 FTG ---- PE 0.0 13 20.5 5.6 12.3 19.7 0.158 TL 8.00 PV Pipe: 12 -88.3 1.610 PL 8.00 PF 2.0 13 20.5 5.6 12.3 19.7 13.9 120 FTG ---- PE 0.0 is 4 20.5 5.6 14.3 21.2 0.252 TL 8.00 PV Pipe: 13 -109.5 1.610 PL 8.00 PF 3.0 14 20.5 5.6 14.3 21.2 17.3 120 FTG ---- PE 0.0 15 20.5 5.6 17.3 23.3 0.375 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. S END ELEV. NOZ. PT DISC. VEL(FPS) H(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 14 -132.9 1.610 PL 9.50 PF 11.5 15 20.5 5.6 17.3 23.3 20.9 120 FTG ET PE 2.8 16 14.0 0.0 31.7 0.0 0.537 TL 21.50 PV Pipe: 15 -14.8 1.049 PL 8.00 PF 0.6 17 25.5 5.6 7.0 14.8 5.5 120 FTG ---- PE 0.0 18 25.5 5.6 7.6 15.4 0.075 TL 8.00 PV Pipe: 16 -30.3 1.380 PL 8.00 PF 0.6 18 25.5 5.6 7.6 15.4 6.5 120 FTG ---- PE 0.0 19 25.5 5.6 8.2 16.0 0.074 TL 8.00 PV Pipe: 17 -46.3 1.380 PL 8.00 PF 1.3 19 25.5 5.6 8.2 16.0 9.9 120 FTG ---- PE 0.0 20 25.5 5.6 9.5 17.2 0.162 TL 8.00 PV Pipe: 18 -63.5 1.610 PL 8.00 PF 1.1 20 25.5 5.6 9.5 17.2 10.0 120 FTG ---- PE 0.0 21 25.5 5.6 10.6 18.2 0.137 TL 8.00 PV Pipe: 19 -81.7 1.610 PL 8.00 PF 1.7 21 25.5 5.6 10.6 18.2 12.9 120 FTG ---- PE 0.0 22 25.5 5.6 12.3 19.7 0.218 TL 8.00 PV Pipe: 20 -101.4 1.610 PL 8.00 PF 2.6 22 25.5 5.6 12.3 19.7 16.0 120 FTG ---- PE 0.0 23 25.5 5.6 14.9 21.6 0.325 TL 8.00 PV Pipe: 21 -123.0 1.610 PL 14.50 PF 12.3 23 25.5 5.6 14.9 21.6 19.4 120 FTG ET PE 5.0 24 14.0 0.0 32.2 0.0 0.465 TL 26.50 PV Pipe: 22 -15.1 1.049 PL 8.00 PF 0.6 25 25.5 5.6 7.3 15.1 5.6 120 FTG ---- PE 0.0 26 25.5 5.6 7.9 15.8 0.078 TL 8.00 PV Pipe: 23 -30.9 1.380 PL 8.00 PF 0.6 26 25.5 5.6 7.9 15.8 6.6 120 FTG ---- PE 0.0 27 25.5 5.6 8.5 16.4 0.076 TL 8.00 PV Pipe: 24 -47.2 1.380 PL 8.00 PF 1.3 27 25.5 5.6 8.5 16.4 10.1 120 FTG ---- PE 0.0 28 25.5 5.6 9.9 17.6 0.168 TL 8.00 PV Pipe: 25 -64.8 1.610 PL 8.00 PF 1.1 28 25.5 5.6 9.9 17.6 10.2 120 FTG ---- PE 0.0 29 25.5 5.6 11.0 18.6 0.142 TL 8.00 PV Pipe: 26 -83.4 1.610 PL 8.00 PF 1.8 09 25.5 5.6 11.0 18.6 13.1 120 FTG ---- PE 0.0 30 25.5 5.6 12.8 20.0 0.227 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. ELEV. NOZ. PT DISC. VEL(FPS) HW(C) (FT) SUM. S END NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 27 -103.4 1.610 FL 8.00 PF 2.7 30 25.5 5.6 12.8 20.0 16.3 120 FTG ---- FE 0.0 31 25.5 5.6 15.5 22.1 0.338 TL 8.00 PV Pipe: 28 -125.5 1.610 FL 14.50 PF 12.8 31 25.5 5.6 15.5 22.1 19.8 120 FTG ET FE 5.0 32 14.0 0.0 33.3 0.0 0.483 TL 26.50 PV Pipe: 29 -23.8 1.049 PL 8.00 PF 1.4 33 20.5 5.6 18.0 23.8 8.8 120 FTG ---- FE 0.0 34 20.5 5.6 19.5 24.7 0.179 TL 8.00 PV Pipe: 30 -48.5 1.380 FL 8.00 PF 1.4 34 20.5 5.6 19.5 24.7 10.4 120 FTG ---- FE 0.0 35 20.5 5.6 20.9 25.6 0.176 TL 8.00 PV Pipe: 31 -74.1 1.380 FL 8.00 PF 3.1 35 20.5 5.6 20.9 25.6 15.9 120 FTG ---- PE 0.0 36 20.5 0.0 24.0 0.0 0.386 TL 8.00 PV Pipe: 32 -74.1 1.610 FL 8.00 PF 1.5 36 20.5 0.0 24.0 0.0 11.7 120 FTG ---- FE 0.0 37 20.5 0.0 25.4 0.0 0.182 TL 8.00 PV Pipe: 33 -74.1 1.610 PL 8.00 PF 1.5 37 20.5 0.0 25.4 0.0 11.7 120 FTG ---- FE 0.0 38 20.5 0.0 26.9 0.0 0.182 TL 8.00 PV Pipe: 34 -74.1 1.610 FL 8.00 PF 1.5 38 20.5 0.0 26.9 0.0 11.7 120 FTG ---- PE 0.0 39 20.5 0.0 28.3 0.0 0.182 TL 8.00 PV Pipe: 35 -74.1 1.610 PL 9.50 PF 3.9 39 20.5 0.0 28.3 0.0 11.7 120 FTG ET PE 2.8 40 14.0 0.0 35.1 0.0 0.182 TL 21.50 PV Pipe: 36 -144.8 3.260 FL 8.00 PF 0.2 8 14.0 0.0 31.5 0.0 5.6 120 FTG ---- FE 0.0 16 14.0 0.0 31.7 0.0 0.020 TL 8.00 PV Pipe: 37 -277.6 3.260 FL 8.00 PF 0.5 16 14.0 0.0 31.7 0.0 10.7 120 FTG ---- FE 0.0 24 14.0 0.0 32.2 0.0 0.068 TL 8.00 PV Pipe: 38 -400.6 3.260 PL 8.00 PF 1.1 24 14.0 0.0 32.2 0.0 15.4 120 FTG ---- FE 0.0 32 14.0 0.0 33.3 0.0 0.133 TL 8.00 PV Pipe: 39 -526.1 3.260 FL 8.00 PF 1.8 02 14.0 0.0 33.3 0.0 20.2 120 FTG ---- FE 0.0 40 14.0 0.0 35.1 0.0 0.220 TL 8.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant 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 -600.2 3.260 PL 42.00 PF 19.7 40 14.0 0.0 35.1 0.0 23.1 120 FTG 3E FE 0.0 41 14.0 0.0 54.8 0.0 0.281 TL 70.22 PV Pipe: 41 -600.2 4.260 FL 13.00 PF 3.2 41 14.0 0.0 54.8 0.0 13.5 120 FTG C FE 5.6 42 1.0 0.0 63.7 0.0 0.076 TL 41.97 PV Pipe: 42 -600.2 6.065 FL 70.00 PF 1.8 42 1.0 0.0 63.7 0.0 6.7 150 FTG 4ET FE -0.4 43 2.0 0.0 65.0 0.0 0.009 TL 199.95 PV Pipe: 43 FIXED PRESSURE LOSS DEVICE 44 2.0 0.0 68.0 0.0 3.0 psi, 600.2 gpm 43 2.0 0.0 65.0 0.0 Pipe: 44 -600.2 6.065 FL 60.00 PF 1.2 44 2.0 0.0 68.0 0.0 6.7 150 FTG ETG PE 0.9 SOURCE 0.0 SRCE 70.1 (N/A) 0.009 TL 131.02 PV NOTES: Calculations were performed by the HASS 7.5 computer program under license no. 5004004430 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 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 0.131 gpm.. Total pressure at each node is used in balancing the system. Maximum water velocity is 23.1 ft/sec at pipe 40. (4) PIPE FITTINGS TABLE Pipe Table 'Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEll ChkVlv BfyViv GatViv AlmChk DPV1v NPTee 3.260 9.41 20.16 6.72 21.50 13.44 1.34 17.47 17.47 20.16 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 26.33 26.33 S SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant PAGE: A MATERIAL: S40 HWC: 120 .Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A Eli Tee LngEfl ChkVlv BfyViv GatViv AimChk 1.049 2.00 5.00 2.00 5.00 6.00 1.00 10.00 1.380 3.00 6.00 2.00 7.00 6.00 1.00 10.00 1.610 4.00 8.00 2.00 9.00 6.00 1.00 10.00 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 D N DPViv NPTee 10.00 5.00 10.00 6.00 10.00 8.00 28.00 30.00 0 C/) (I) z H 01 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant 0 0 0 X.1 KI N 0 0 0 0 0 0 0 0 o CD CD CD CD CD (N 0 0 oH a.01rc')cn01r0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/1/2004 C:\HASS75\CANNONREST.SDF JOB TITLE: Cannon Court Restaurant WATER SUPPLY CURVE 108± 99+ *\\\\ \\\\\ \\\\\ 90+ \\\\ \\\\\ I \\\\\ \\\\ 81+ * <-80.0 psi 8 693 gpm 0 Flow TestPoint P 72+ X E 5 63+ .1.: ; I 45+ ) I • 36+ 27+ 18+ LEGEND I 'I I X = Required Water Supply I 70.08. psi @ 700.2 gpm 9+ I 0 = Available Water Supply I 79.67 psi @ 700.2 gpm H 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 FLOW (GPM) Western States Fire Protection Co. 9550 Chesapeake Drive San Diego CA 92123 HYDRAULIC CALCULATIONS S FOR Cannon Court Restaurant Lobby and Entrance FILE NUMBER: DATE: JUN 1, 2004 -DESIGN DATA- OCCUPANCY CLASSIFICATION: Light Hazard DENSITY: .10 gpm/sq. ft. AREA OF APPLICATION: Porch, lobby and restrooms COVERAGE PER SPRINKLER: varies sq. ft. NUMBER OF SPRINKLERS CALCULATED: 19 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 397.4 gpm TOTAL WATER REQUIRED (including hose) 497.4 gpm FLOW AND PRESSURE (@ BOR) 397.4 gpm @ 63.5 psi SPRINKLER ORIFICE SIZE: 1/2 inch AUTHORITY HAVING JURISDICTION: Carlsbad Fire Department CONTRACTOR CERTIFICATION NUMBER: Lisc C-16 488359 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 5004004430) HRS SYSTEMS, INC. TUCKER, GA 30084 SPRINKLER SYSTEM 14YDRAULIC ANALYSIS Page 1 DATE: 6/1/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby WATER SUPPLY DATA *SOURCE STATIC RESID. FLOW NODE PRESS. PRESS. @ TAG (PSI) (PSI) (GPM) SOURCE 97.0 80.0 693.0 AVAIL. TOTAL REQ'D PRESS. @ DEMAND PRESS. (PSI) (GPM) (PSI) 87.8 497.4 68.4 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 497.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 397.4 GEM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 1 15.5 K= 5.60 20.2 25.2 2 15.5 K= 5.60 21.8 26.1 3 14.0 - - - - 25.1 - - - 4 19.5 K= 5.60 10.3 18.0 .5 6 19.0 19.5 - - K= - - 5.60 10.9 11.3 - - - 18.8 7 19.0 - - - - 12.2 - - - 8 19.5 K= 5.60 12.2 19.5 9 19.0 - - - - 13.1 - - - 10 19.5 K= 5.60 13.9 20.9 11 19.0 - - - - 15.0 - - - 12 19.5 K= 5.60 15.4 22.0 13 19.0 - - - - 16.6 - - - 14 14.0 - - - - 25.1 - - - 15 20.0 K= 5.60 9.0 16.8 16 25.0 K= 5.60 8.1 15.9 17 25.0 - - - - 8.6 - - - 18 29.0 K= 5.60 7.0 14.8 19 25.0 - - - - 10.1 - - - 20 25.0 K= 5.60 12.5 19.8 21 25.0 - - - - 13.3 - - - 22 25.0 K= 5.60 13.7 20.7 23 25.0 - - - - 14.5 - - - 24 14.0 - - - - 25.8 - - - 25 19.5 K= 5.60 11.3 18.8 26 19.0 - - - - 11.8 - - - 27 19.5 K= 5.60 12.3 19.6 28 19.0 - - - - 13.2 - - - 29 19.5 K= 5.60 13.2 20.4 30 19.0 - - - - 14.3 - - - W 1 19.5 K= 5.60 15.1 21.8 2 19.0 - - - - 16.3 - - - 33 19.5 K= 5.60 16.8 22.9 34 19.0 - - - - 18.0 - - - 35 14.0 - - - - 27.1 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/1/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby NODE ANALYSIS DATA NODE TAG ELEVATION 0N NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 36 15.5 K= 5.60 23.5 27.2 37 15.5 K= 5.60 25.3 28.2 38 14.0 - - - - 29.0 - - - 39 14.0 - - - - 42.6 - - - 40 14.0 - - - - 56.4 - - - 41 1.0 - - - - 63.5 - - - 42 2.0 - - - - 63.9 - - - 43 2.0 - - - - 66.9 - - - SOURCE 0.0 SOURCE 68.4 397.4 0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/1/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby 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 1.049 FL 8.00 PF 1.6 1 15.5 5.6 20.2 25.2 9.3 120 FTG ---- PE 0.0 2 15.5 5.6 21.8 26.1 0.199 TL 8.00 PV Pipe: 2 -51.3 1.380 FL 4.50 PF 2.6 2 15.5 5.6 21.8 26.1 11.0 120 FTG ET FE 0.6 3 14.0 0.0 25.1 0.0 0.195 TL 13.50 PV Pipe: 3 -18.0 1.049 PL 1.00 PF 0.3 4 19.5 5.6 10.3 18.0 6.7 120 FTG E PE 0.2 5 19.0 0.0 10.9 0.0 0.107 TL 3.00 PV Pipe: 4 -18.0 1.049 PL 12.00 PF 1.3 5 19.0 0.0 10.9 0.0 6.7 120 FTG ---- PE 0.0 7 19.0 0.0 12.2 0.0 0.107 TL 12.00 PV Pipe: 5 -18.8 1.049 FL 1.00 PF 0.7 6 19.5 5.6 11.3 18.8 7.0 120 FTG T FE 0.2 7 19.0 0.0 12.2 0.0 0.116 TL 6.00 PV Pipe: 6 19.0 0.0 12.2 0.0 -36.8 7.9 1.380 120 FL FTG 9.00 ---- PF FE 1.0 0.0 9 19.0 0.0 13.1 0.0 0.106 TL 9.00 PV Pipe: 7 -19.5 1.049 FL 1.00 PF 0.7 8 19.5 5.6 12.2 19.5 7.3 120 FTG T FE 0.2 9 19.0 0.0 13.1 0.0 0.125 TL 6.00 PV Pipe: 8 -56.3 1.380 PL 8.00 PF 1.9 9 19.0 0.0 13.1 0.0 12.1 120 FTG ---- FE 0.0 11 19.0 0.0 15.0 0.0 0.232 TL 8.00 PV Pipe: 9 -20.9 1.049 PL 1.00 PF 0.8 10 19.5 5.6 13.9 20.9 7.8 120 FTG T FE 0.2 11 19.0 0.0 15.0 0.0 0.141 TL 6.00 PV Pipe: 10 -77.2 1.610 FL 8.00 PF 1.6 11 19.0 0.0 15.0 0.0 12.2 120 FTG ---- FE 0.0 13 19.0 0.0 16.6 0.0 0.197 TL 8.00 PV Pipe: 11 -22.0 1.049 FL 1.00 PF 0.9 12 19.5 5.6 15.4 22.0 8.2 120 FTG T FE 0.2 13 19.0 0.0 16.6 0.0 0.155 TL 6.00 PV Pipe: 12 -99.2 1.610 FL 8.50 PF 6.4 13 19.0 0.0 16.6 0.0 15.6 120 FTG ET FE 2.2 . 4 14.0 0.0 25.1 0.0 0.313 TL 20.50 PV Pipe: 13 -16.8 1.049 FL 15.00 PF 1.8 15 20.0 5.6 9.0 16.8 6.2 120 FTG 2E FE -2.2 17 25.0 0.0 8.6 0.0 0.094 TL 19.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/1/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby 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 -15.9 1.049 PL 1.00 PF 0.5 16 25.0 5.6 8.1 15.9 5.9 120 FTG T PH 0.0 17 25.0 0.0 8.6 0.0 0.085 TL 6.00 PV Pipe: 15 -32.7 1.380 PL 12.50 PF 1.6 17 25.0 0.0 8.6 0.0 7.0 120 FTG 2E PE 0.0 19 25.0 0.0 10.1 0.0 0.085 TL 18.50 PV Pipe: 16 -14.8 1.049 PL 10.00 PF 1.4 18 29.0 5.6 7.0 14.8 5.5 120 FTG 2ET PE 1.7 19 25.0 0.0 10.1 0.0 0.075 TL 19.00 PV Pipe: 17 -47.5 1.380 PL 12.50 PF 3.1 19 25.0 0.0 10.1 0.0 10.2 120 FTG 2E PE 0.0 21 25.0 0.0 13.3 0.0 0.169 TL 18.50 PV Pipe: 18 -19.8 1.049 PL 1.00 PF 0.8 20 25.0 5.6 12.5 19.8 7.4 120 FTG T PE 0.0 21 25.0 0.0 13.3 0.0 0.128 TL 6.00 PV Pipe: 19 -67.3 1.610 PL 8.00 PF 1.2 21 25.0 0.0 13.3 0.0 10.6 120 FTG ---- PE 0.0 23 25.0 0.0 14.5 0.0 0.152 TL 8.00 PV 0 Pipe: 20 -20.7 1.049 PL 1.00 PF 0.8 22 25.0 5.6 13.7 20.7 7.7 120 FTG T PH 0.0 23 25.0 0.0 14.5 0.0 0.139 TL 6.00 PV Pipe: 21 -88.0 1.610 PL 14.00 PF 6.5 23 25.0 0.0 14.5 0.0 13.9 120 FTG ET PE 4.8 24 14.0 0.0 25.8 0.0 0.250 TL 26.00 PV Pipe: 22 -18.8 1.049 PL 1.00 PF 0.3 25 19.5 5.6 11.3 18.8 7.0 120 FTG E PE 0.2 26 19.0 0.0 11.8 0.0 0.116 TL 3.00 PV Pipe: 23 -18.8 1.049 PL 12.00 PF 1.4 26 19.0 0.0 11.8 0.0 7.0 120 FTG ---- PE 0.0 28 19.0 0.0 13.2 0.0 0.116 TL 12.00 PV Pipe: 24 -19.6 1.049 PL 1.00 PF 0.8 27 19.5 5.6 12.3 19.6 7.3 120 FTG T PE 0.2 28 19.0 0.0 13.2 0.0 0.125 TL 6.00 PV Pipe: 25 -38.4 1.380 PL 9.00 PF 1.0 28 19.0 0.0 13.2 0.0 8.2 120 FTG ---- PE 0.0 30 19.0 0.0 14.3 0.0 0.114 TL 9.00 PV Pipe: 26 -20.4 1.049 PL 1.00 PF 0.8 9 19.5 5.6 13.2 20.4 7.6 120 FTG T PE 0.2 30 19.0 0.0 14.3 0.0 0.135 TL 6.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/1/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby 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: 27 -58.8 1.380 PL 8.00 PF 2.0 30 19.0 0.0 14.3 0.0 12.6 120 FTG ---- PE 0.0 32 19.0 0.0 16.3 0.0 0.252 TL 8.00 PV Pipe: 28 -21.8 1.049 PL 1.00 PF 0.9 31 19.5 5.6 15.1 21.8 8.1 120 FTG T PE 0.2 32 19.0 0.0 16.3 0.0 0.152 TL 6.00 PV Pipe: 29 -80.6 1.610 PL 8.00 PF 1.7 32 19.0 0.0 16.3 0.0 12.7 120 FTG ---- PE 0.0 34 19.0 0.0 18.0 0.0 0.213 TL 8.00 PV Pipe: 30 -22.9 1.049 FL 1.00 PF 1.0 33 19.5 5.6 16.8 22.9 8.5 120 FTG T PE 0.2 34 19.0 0.0 18.0 0.0 0.167 TL 6.00 PV Pipe: 31 -103.5 1.610 FL 8.50 PF 6.9 34 19.0 0.0 18.0 0.0 16.3 120 FTG ET PE 2.2 35 14.0 0.0 27.1 0.0 0.338 TL 20.50 PV Pipe: 32 -27.2 1.049 PL 8.00 PF 1.8 36 15.5 5.6 23.5 27.2 10.1 120 FTG ---- FE 0.0 37 0 15.5 5.6 25.3 28.2 0.229 TL 8.00 PV Pipe: 33 -55.3 1.380 PL 4.50 PF 3.0 37 15.5 5.6 25.3 28.2 11.9 120 FTG ET PE 0.6 38 14.0 0.0 29.0 0.0 0.225 TL 13.50 PV Pipe: 34 -51.3 2.635 PL 8.00 PF 0.1 3 14.0 0.0 25.1 0.0 3.0 120 FTG ---- PE 0.0 14 14.0 0.0 25.1 0.0 0.008 TL 8.00 PV Pipe: 35 -150.5 2.635 FL 10.50 PF 0.6 14 14.0 0.0 25.1 0.0 8.9 120 FTG ---- FE 0.0 24 14.0 0.0 25.8 0.0 0.061 TL 10.50 PV Pipe: 36 -238.5 2.635 FL 9.00 PF 1.3 24 14.0 0.0 25.8 0.0 14.0 120 FTG ---- FE 0.0 35 14.0 0.0 27.1 0.0 0.144 TL 9.00 PV Pipe: 37 -342.0 2.635 FL 7.00 PF 2.0 35 14.0 0.0 27.1 0.0 20.1 120 FTG ---- FE 0.0 38 14.0 0.0 29.0 0.0 0.280 TL 7.00 PV Pipe: 38 -397.4 2.635 FL 12.00 PF 13.6 38 14.0 0.0 29.0 0.0 23.4 120 FTG 3E PE 0.0 39 14.0 0.0 42.6 0.0 0.370 TL 36.71 PV .Pipe: 39 -397.4 3.260 FL 77.00 PF 13.8 9 14.0 0.0 42.6 0.0 15.3 120 FTG 3E FE 0.0 41 14.0 0.0 56.4 0.0 0.131 TL 105.22 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/1/2004 C:\HASS75\CANNONENTRy.SDF JOB TITLE: Cannon Court Entry and Lobby 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 -397.4 4.260 PL 13.00 PF 1.5 4t 14.0 0.0 56.4 0.0 8.9 120 FTG C PE 5.6 49 1.0 0.0 63.5 0.0 0.036 TL 41.97 PV Pipe: 41 -397.4 6.065 PL 70.00 PF 0.8 4, 1.0 0.0 63.5 0.0 4.4 150 FTG 4ET PE -0.4 42 2.0 0.0 63.9 0.0 0.004 TL 199.95 PV Pipe: 42 FIXED PRESSURE LOSS DEVICE 43 2.0 0.0 66.9 0.0 3.0 psi, 397.4 gpm 4W 2.0 0.0 63.9 0.0 Pipe: 43 -397.4 6.065 PL 60.00 PF 0.6 44 2.0 0.0 66.9 0.0 4.4 150 FTG ETG PE 0.9 SOURCE 0.0 SRCE. 68.4 (N/A) 0.004 TL 131.02 PV NOTES: Calculations were performed by the HASS 7.5 computer program under license no. 5004004430 granted by HRS Systems, Inc. 4792 LaVista Road. Tucker, GA 30084 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 23.4 ft/sec at pipe 38. (4) PIPE FITTINGS TABLE Pipe Table Name: STANDARD.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEl1 ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.635 8.24 16.47 5.49 19.22 9.61 1.37 13.73 13.73 16.47 3.260 9.41 20.16 6.72 21.50 13.44 1.34 17.47 17.47 20.16 4.260 13.17 26.33 7.90 28.97 15.80 2.63 26.33 26.33 26.33 n in Feet G A GatVlv AlmChk 1.00 10.00 1.00 10.00 1.00 10.00 3.00 28.00 D N DPVlv NPTee 10.00 5.00 10.00 6.00 10.00 8.00 28.00 30.00 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/l/2004 C:\HASS75\CANNONENTRY.SDF JOB TITLE: Cannon Court Entry and Lobby PAGE: A MATERIAL: S40 HWC: 120 .iameter Equivalent Fitting Lengths (in) E T L C B Eli Tee LngEll ChkVlv BfyVlv 1.049 2.00 5.00 2.00 5.00 6.00 1.380 3.00 6.00 2.00 7.00 6.00 1.610 4.00 8.00 2.00 9.00 6.00 6.065 14.00 30.00 9.00 32.00 10.00 0 > (I) 0 CD CD co u) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/1/2004 C:\HASS75\CANNONENTRy.SDF JOB TITLE: Cannon Court Entry and Lobby ID . I P I S (N 0 CD 0 CD CD CD CD oH CD CD CD CD (0 CD (N CD CO Q0 (N oH oH QUr— SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 6/1/2004 C:\HASS75\CANNONENTRY .SDF JOB TITLE: Cannon Court Entry and Lobby WATER SUPPLY CURVE 108+ 99+ I \\\\\ I \\\\\ 90+ \\\\ 0\\\\\ \\\\\ \\\\ 81+ * <-80.0 psi @ 693 gpm I Flow Test Point P 72+ R I E X S I S 63+ U R E I 54+ *P I 45+ ) I 36+ 27+ 18+ LEGEND I I, I X = Required Water Supply IT I 68.36 psi @ 497.4 gpm IT 9+ if I 0 = Available Water Supply it I 87.80 psi @ 497.4 gpm IT I, 0++-+---+----+-----+ ------+ --------+ --------+ ---------+ -----------+ 200 300 400 500 600 700 800 900 1000 is FLOW (GPM)