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HomeMy WebLinkAbout1838 CLIFF SWALLOW LN; ; AS120117; Permit11/3/2020 AS120117 Permit Data City of Carlsbad Sprinkler Permit Permit No: AS120117 1838 CLIFF Job Address: Status: APPROVED SWALLOW LN Permit Type: SPRINK Applied 9/26/2012 Parcel No: 2150507300 Approved: 9/26/2012 Lot #: 0 Reference No.: Issued: 9/26/2012 PC #: Inspector: Project Title: CARLSBAD III NEW 13R FIRE SPRINKLER SYSTEM Applicant: INNOVATIVE FIRE PROTECTION SUITE 101 8779 COTTONWOOD AV SANTEE, CA (619) 593-8200 (619)593-9133 Owner: CITY VENTURES HOMEBUILDING L L C STE 150 3121 MICHELSON DR IRVINE CA Fees ($) Add'I Fees ($) Total ($) Balance ($) 476 0 476 0 1/1 L) LA--) / i ri . t J r, - These plans have heel] revies ed tor ljtar'eiit Compliance with t' j. current applicable codes and stittdu'ds in hitce in neturisdictioti. The owner or contractor riiav iitilite this ft\ICO ill support of' an application Uiir a hiiikline PC[ mil su tutu the espress understanding that this reviesu Ill iii war relies en the owner in coutriciiur or their protessuonal engineer or architect f or sole respuntsihilit tol kill coiutpluauuce with said codes and suatudards, tuicluditig Ille hu1dni5 code iii' tdr any responsihilty for utetucucttets, eri'ors, ourutssuoits or lieu, linelice in these plans ivluethcr or not toted i ll this review. Date: Rev ueweu ETR E('ON I NI EN I) AI'PRt )v,A I, RECOMMENI) APPRO VAL AS NOTED fr' $13 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE3 66.5 49.5 712.0 64.8 203.0 63.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 203.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 103.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE3 -1.0 SOURCE 63.0 103.0 DC 3.0 61.2 DA 3.0 54.2 U.1 1.0 - - - - 54.8 BOR 1.0 - - - - 54.7 TOR 9.5 - - - - 50.2 1 9.5 - - - - 47.8 2 9.5 - - - - 47.0 - - - 3 9.5 - - - - 46.8 - - - 4 20.0 - - - - 42.7 5 20.0 - - - - 42.3 6 20.0 - - - - 41.7 7 20.0 - - - - 40.6 8 20.0 - - - - 40.2 9 20.0 - - - - 40.6 10 20.0 - - - - 40.6 10A 19.5 - - - - 40.8 - - - hA 19.5 - - - - 40.8 - - - 12 20.0 - - - - 40.6 12A 19.5 - - - - 40.8 - - - 13A 19.5 - - - - 40.8 - - - 14 20.0 ----- 41.5 15 20.0 - - - - 41.3 16 30.0 - - - - 36.8 - - - 17 34.0 - - - - 34.0 18 30.0 - - - - 34.9 - - - 19 34.0 - - - - 32.2 20 30.0 - - - - 36.5 21 34.0 - - - - 34.1 22 30.5 - - - - 30.3 - - - 23 30.5 - - - - 28.7 23A 30.0 K= 4.90 27.3 25.6 24A 30.0 K= 4.90 27.4 25.6 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25 30.5 - - - - 29.5 - - - 25A 30.0 K= 4.90 28.1 26.0 26A 30.0 K= 4.90 27.6 25.7 BB1 34.0 - - - - 33.4 - - - BB2 34.0 - - - - 32.5 BB3 34.0 - - - - 32.5 --- BB4 34.0 - - - - 32.9 BB5 34.0 - - - - 33.7 - - - SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRI-\N FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd 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: 1 103.0 5.850 PL 40.00 PF 0.1 SOtJRCE3 -1.0 SRCE 63.0 (N/A) 1.2 150 FTG TLG FE -1.7 DC 3.0 0.0 61.2 0.0 0.000 TL 148.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 61.2 0.0 7.0 psi, 103.0 gpm DA 3.0 0.0 54.2 0.0 Pipe: 3 103.0 4.070 FL 65.00 PF 0.4 DA 3.0 0.0 54.2 0.0 2.5 150 FTG E2T PE 0.9 [3.1 1.0 0.0 54.8 0.0 0.002 TL 144.66 PV Pipe: 4 103.0 4.220 PL 5.00 PF 0.1 [3.1 1.0 0.0 54.8 0.0 2.4 140 FTG E PE 0.0 BOR 1.0 0.0 54.7 0.0 0.002 TL 21.73 PV Pipe: 5 103.0 2.703 FL 7.50 FE' 0.8 BOR 1.0 0.0 54.7 0.0 5.8 120 FTG C PE -3.7 TOR 9.5 0.0 50.2 0.0 0.027 TL 29.26 PV Pipe: 6 103.0 2.423 PL 32.00 PF 2.4 TOR 9.5 0.0 50.2 0.0 7.2 150 FTG 4E PE 0.0 1 9.5 0.0 47.8 0.0 0.030 TL 80.00 PV Pipe: 7 69.4 2.003 FL 11.00 PF 0.8 1 9.5 0.0 47.8 0.0 7.1 150 FTG T PE 0.0 2 9.5 0.0 47.0 0.0 0.037 TL 21.00 PV Pipe: 8 30.9 2.003 PL 22.50 PF 0.3 2 9.5 0.0 47.0 0.0 3.2 150 FTG T PE 0.0 3 9.5 0.0 46.8 0.0 0.008 TL 32.50 PV Pipe: 11 33.6 1.598 PL 10.50 PF 0.6 1 9.5 0.0 47.8 0.0 5.4 150 FTG E PE -4.5 4 20.0 0.0 42.7 0.0 0.029 TL 19.50 PV Pipe: 12 33.6 1.598 PL 5.50 PE' 0.4 4 20.0 0.0 42.7 0.0 5.4 150 FTG E PE 0.0 5 20.0 0.0. 42.3 0.0 0.029 TL 14.50 PV Pipe: 13 33.6 1.598 FL 5.00 PF 0.6 5 20.0 0.0 42.3 0.0 5.4 150 FTG 2T FE 0.0 6 20.0 0.0 41.7 0.0 0.029 TL 21.00 PV Pipe: 14 38.4 1.598 FL 16.00 PF 1.9 2 9.5 0.0 47.0 0.0 6.1 150 FTG 3ET PE -4.5 7 20.0 0.0 40.6 0.0 0.037 TL 51.00 PV 1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRPM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd 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: 15 38.4 1.598 PL 2.00 PF 0.4 7 20.0 0.0 40.6 0.0 6.1 150 FTG T PE 0.0 8 20.0 0.0 40.2 0.0 0.037 TL 10.00 PV Pipe: 16 30.9 1.598 PL 10.50 PF 0.7 3 9.5 0.0 46.8 0.0 4.9 150 FTG ET PE -4.5 14 20.0 0.0 41.5 0.0 0.025 TL 27.50 PV Pipe: 17 30.9 1.598 PL 2.50 PF 0.3 14 20.0 0.0 41.5 0.0 4.9 150 FTG E PE 0.0 15 20.0 0.0 41.3 0.0 0.025 TL 11.50 PV Pipe: 18 0.0 1.394 PL 4.50 PF 0.0 7 20.0 0.0 40.6 0.0 0.0 150 FTG ---- PE .0.0 9 20.0 0.0 40.6 0.0 0.000 TL 4.50 PV Pipe: 19 0.0 1.101 PL 0.50 PF 0.0 9 20.0 0.0 40.6 0.0 0.0 150 FTG T PE 0.0 10 20.0 0.0 40.6 0.0 0.000 TL 5.50 PV Pipe: 20 0.0 1.101 PL 0.50 PF 0.0 10 20.0 0.0 40.6 0.0 0.0 150 FTG T PE 0.2 bA 19.5 0.0 40.8 0.0 0.000 TL 5.50 PV Pipe: 21 . 0.0 1.101 PL 9.00 PF 0.0 10 20.0 0.0 40.6 0.0 0.0 150 FTG E PE 0.2 hA 19.5 0.0 40.8 0.0 0.000 TL 16.00 PV Pipe: 22 0.0 1.394 PL 13.50 PF 0.0 9 20.0 0.0 40.6 0.0 0.0 150 FTG E PE 0.0 12 20.0 0.0 40.6 0.0 . 0.000 TL 21.50 PV Pipe: 23 0.0 1.101 PL 0.50 PF 0.0 12 20.0 0.0 40.6 0.0 0.0 150 FTG T PE 0.2 12A 19.5 0.0 40.8 0.0 0.000 TL 5.50 PV Pipe: 24 0.0 1.101 PL 9.00 PF 0.0 12 20.0 0.0 40.6 0.0 0.0 150 FTG E PE 0.2 13A 19.5 0.0 40.8 0.0 0.000 TL 16.00 PV Pipe: 25 33.6 1.598 PL 10.00 PF 0.5 6 20.0 0.0 41.7 0.0 5.4 150 FTG E PE -4.3 16 30.0 0.0 36.8 0.0 0.029 TL 19.00 PV Pipe: 26 33.6 1.598 PL 12.00 PF 1.0 16 30.0 0.0 36.8 0.0 5.4 150 FTG 3T PE -1.7 17 34.0 0.0 34.0 0.0 0.029 TL 36.00 PV Pipe: 29 38.4 1.598 PL 11.00 PF 1.0 8 20.0 0.0 40.2 0.0 6.1 150 FTG ET PE -4.3 18 30.0 0.0 34.9 0.0 0.037 TL 28.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\04815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd 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: 30 38.4 1.598 PL 9.00 PF 1.0 18 30.0 0.0 34.9 0.0 6.1 150 FTG ET PE -1.7 19 34.0 0.0 32.2 0.0 0.037 TL 26.00 PV Pipe: 31 30.9 1.598 FL 10.00 PF 0.4 15 20.0 0.0 41.3 0.0 4.9 150 FTG T PE -4.3 20 30.0 0.0 36.5 0.0 0.025 TL 18.00 PV Pipe: 32 30.9 1.598 FL 9.00 PF 0.6 20 30.0 0.0 36.5 0.0 4.9 150 FTG 2T FE -1.7 21 34.0 0.0 34.1 0.0 0.025 TL 25.00 PV Pipe: 33 103.0 1.598 PL 6.50 PF 3.3 19 34.0 0.0 32.2 0.0 16.5 150 FTG T PE 1.5 22 30.5 0.0 30.3 0.0 0.230 TL 14.50 PV Pipe: 34 51.2 1.394 FL 7.50 PF 1.7 22 30.5 0.0 30.3 0.0 10.8 150 FTG T FE 0.0 23 30.5 0.0 28.7 0.0 0.123 TL 13.50 PV Pipe: 35 25.6 1.101 FL 3.00 PF 1.6 23 30.5 0.0 28.7 0.0 8.6 150 FTG ET PE 0.2 23A 30.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 36 25.6 1.101 PL 7.00 PF 1.5 23 30.5 0.0 28.7 0.0 8.6 150 FTG E PE 0.2 24A 30.0 4.9 27.4 25.6 0.108 TL 14.00 PV Pipe: 37 51.7 1.394 FL 6.50 PF 0.8 22 30.5 0.0 30.3 0.0 10.9 150 FTG ---- PE 0.0 25 30.5 0.0 29.5 0.0 0.125 TL 6.50 PV Pipe: 38 26.0 1.101 FL 3.00 PF 1.7 25 30.5 0.0 29.5 0.0 8.8 150 FTG ET FE 0.2 25A 30.0 4.9 28.1 26.0 0.110 TL 15.00 PV Pipe: 39 25.7 1.101 PL 6.00 PF 2.2 25 30.5 0.0 29.5 0.0 8.7 150 FTG 2E PE 0.2 26A 30.0 4.9 27.6 25.7 0.108 TL 20.00 PV Pipe: 40 33.6 1.598 FL 13.00 PF 0.6 17 34.0 0.0 34.0 0.0 5.4 150 FTG T FE 0.0 BB1 34.0 0.0 33.4 0.0 0.029 TL 21.00 PV Pipe: 41 33.6 1.598 PL 6.50 PF 0.9 BB1 34.0 0.0 33.4 0.0 5.4 150 FTG 2ET FE 0.0 BB2 34.0 0.0 32.5 0.0 0.029TL 32.50 PV Pipe: 42 33.6 1.598 FL 3.00 PF 0.3 BB2 34.0 0.0 32.5 0.0 5.4 150 FTG T FE 0.0 19 34.0 0.0 32.2 0.0 0.029 TL 11.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd 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: 43 -30.9 1.598 PL 7.00 PF 0.4 19 34.0 0.0 32.2 0.0 4.9 150 FTG T PE 0.0 BB3 34.0 0.0 32.5 0.0 0.025 TL 15.00 PV Pipe: 44 -30.9 1.598 PL 6.00 PF 0.3 BB3 34.0 0.0 32.5 0.0 4.9 150 FTG T PE 0.0 BB4 34.0 0.0 32.9 0.0 0.025 TL 14.00 PV Pipe: 45 -30.9 1.598 PL 6.50 PF 0.8 BB4 34.0 0.0 32.9 0.0 4.9 150 FTG 2ET PE 0.0 BBS 34.0 0.0 33.7 0.0 0.025 TL 32.50 PV Pipe: 46 -30.9 1.598 PL 9.50 PF 0.4 BB5 34.0 0.0 33.7 0.0 4.9 150 FTG T PE 0.0 21 34.0 0.0 34.1 0.0 0.025 TL 17.50 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.099 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 16.5 ft/sec at pipe 33. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-3rd FLOOR PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEii ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 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 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 80.0 70.0 G A 60.0 U G E 50.0 P R E S 40.0 S U R E 30.0 p s 20.0 i WATER SUPPLY ANALYSIS Static: 66.50 psi Resid: 49.50 psi Flow: 712.0 gpm LEGEND 1 Available pressure 64.83 psi @ 203.0 gpm 2 Required pressure 63.04 psi 8 203.0 gpm 2 A. Source Supply Curve B. System Demand Curve 10.0 0.0 -14. 200 300 400 500 600 IUU FLOW (GPM) uu uu SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. 0 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE3 66.5 49.5 712.0 64.8 203.8 58.9 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 203.8 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 103.8 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE3 -1.0 SOURCE 58.9 103.8 DC 3.0 - - - - 57.1 DA 3.0 - - - - 50.1 U.1 1.0 - - - - 50.6 - - - BOR 1.0 - - - - 50.5 TOR 9.5 - - - - 46.1 1 9.5 - - - - 43.6 - - - 2 9.5 - - - - 42.6 3 . 9.5 - - - - 42.5 - - - 4 20.0 - - - - 38.7 5 20.0 - - - - 38.5 6 20.0 - - - - 38.2 7 20.0 - - - - 33.5 - - - 8 20.0 - - - - 34.0 9 20.0 - - - - 31.5 10 20.0 - - - - 29.3 - - - bA 19.5 K= 490 28.9 26.3 hA 19.5 K= 4.90 27.8 25.8 12 20.0 - - - - . 28.8 12A 19.5 K= 4.90 28.4 26.1 13A 19.5 K= 4.90 27.3 25.6 14 20.0 - - - - 37.7 15 20.0 - - - - 37.6 16. 30.0 - - - - 33.6 17 34.0 - - - - 31.3 18 30.0 - - - - 30.9 19 34.0 - - - - 30.3 20 30.0 - - - - 33.0 21 34.0 - - - - 31.1 22 30.5 - - - - 31.8 23 30.5 . - - - - 31.8 23A 30.0 - - - - 32.0 24A 30.0 - - - - 32.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRN4 FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-2nd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25 30.5 - -- - 31.8 - - - 25A 30.0 - - - - 32.0 - - - 26A 30.0 - - - - 32.0 BB1 34.0 - - - - 31.0 BB2 34.0 - - - - 30.5 BB3 34.0 - - - - 30.5 BB4 34.0 - - - - 30.6 BB5 34.0 - - - - 30.9 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR 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: 1 103.8 5.850 PL 40.00 PF 0.1 SOURCE3 -1.0 SRCE 58.9 (N/A) 1.2 150 FTG TLG PE -1,7 DC 3.0 0.0 57.1 .0.0 0.000 TL 148.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 57.1 0.0 7.0 psi, 103.9 gpm DA 3.0 0.0 50.1 0.0 Pipe: 3 103.9 4.070 PL 65.00 PF 0.4 DA 3.0 0.0 50.1 0.0 2.6 150 FTG E2T PE 0.9 U.1 1.0 0.0 50.6 0.0 0.002 TL 144.66 PV Pipe: 4 103.9 4.220 PL 5.00 PF 0.1 U.1 1.0 0.0 50.6 0.0 2.4 140 FTG E PE 0.0 BOR 1.0 0.0 50.5 0.0 0.002 TL 21.73 PV Pipe: 5 103.9 2.703 PL 7.50 PF 0.8 BOR 1.0 0.0 50.5 0.0 5.8 120 FTG C PE -3.7 TOR 9.5 0.0 46.1 0.0 0.027 TL 29.26 PV Pipe: 6 103.9 2.423 PL 32.00 PF 2.5 TOR 9.5 0.0 46.1 0.0 7.2 150 FTG 4E PE 0.0 1 9.5 0.0 43.6 0.0 . 0.031 TL 80.00 PV Pipe: 7 80.0 2.003 PL 11.00 FE' 1.0 1 9.5 0.0 43.6 0.0 8.2 150 FTG T PE 0.0 2 9.5 0.0 42.6 0.0 0.048 TL 21.00 PV Pipe: 8 18.6 2.003 FL 22.50 PF 0.1 2 9.5 0.0 42.6 0.0 1.9 150 FTG T PE 0.0 3 9.5 0.0 42.5 0.0 0.003 TL 32.50 PV Pipe: 11 23.8 1.598 PL 10.50 PF 0.3 1 9.5 0.0 43.6 0.0 3.8 150 FTG E PE -4.5 4 20.0 0.0 38.7 0.0 0.015 TL 19.50 PV Pipe: 12 23.8 1.598 PL 5.50 PF 0.2 4 20.0 0.0 38.7 0.0 3.8 150 FTG E PE 0.0 5 20.0 0.0 38.5 0.0 0.015 TL 14.50 PV Pipe: 13 23.8 1.598 PL 5.00 PF 0.3 5 20.0 0.0 38.5 0.0 3.8 150 FTG 2T FE 0.0 6 . 20.0 0.0 38.2 0.0 0.015 TL 21.00 PV Pipe: 14 61.5 1.598 PL 16.00 PF 4.5 2 9.5 0.0 42.6 0.0 . 9.8 150 FTG 3ET FE -4.5 7 20.0 0.0 33.5 0.0 0.088 TL 51.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRPM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD 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: 15 -42.4 1.598 PL 2.00 PF 0.4 7 20.0 0.0 33.5 0.0 6.8 150 FTG T PE 0.0 8 20.0 0.0 34.0 0.0 0.045 TL 10.00 PV Pipe: 16 18.6 1.598 PL 10.50 PF 0.3 3 9.5 0.0 42.5 0.0 3.0 150 FTG ET PE -4.5 14 20.0 0.0 37.7 0.0 0.010 TL 27.50 PV Pipe: 17 18.6 1.598 PL 2.50 PF 0.1 14 20.0 0.0 37.7 0.0 3.0 150 FTG E FE 0.0 15 20.0 0.0 37.6 0.0 0.010 TL 11.50 PV Pipe: 18 103.9 1.394 PL 4.50 PF 2.0 7 20.0 0.0 33.5 0.0 21.8 150 FTG ---- PE 0.0 9 20.0 0.0. 31.5 0.0 0.454 TL 4.50 PV Pipe: 19 52.1 1.101 FL 0.50 PF 2.2 9 20.0 0.0 31.5 0.0 17.6 150 FTG T PE 0.0 10 20.0 0.0 29.3 0.0 0.401 TL 5.50 PV Pipe: 20 26.3 1.101 PL 0.50 PF 0.6 10 20.0 0.0 29.3 0.0 8.9 150 FTG T FE 0.2 bA 19.5 4.9 28.9 26.3 0.113 TL 5.50 PV Pipe: 21 25.8 1.101 PL 9.00 PF 1.7 10 20.0 0.0 29.3 0.0 8.7 150 FTG E FE 0.2 hA 19.5 4.9 27.8 25.8 0.109 TL 16.00 PV Pipe: 22 51.7 1.394 FL 13.50 PF 2.7 9 20.0 0.0 31.5 0.0 10.9 150 FTG E FE 0.0 12 20.0 0.0 28.8 0.0 0.125 TL 21.50 PV Pipe: 23 26.1 1.101 PL 0.50 PF 0.6 12 20.0 0.0 28.8 0.0 8.8 150 FTG T PE 0.2 12A 19.5 4.9 28.4 26.1 0.111 TL 5.50 PV Pipe: 24 25.6 1.101 FL 9.00 PF 1.7 12 20.0 0.0 28.8 0.0 8.6 150 FTG E FE 0.2 13A 19.5 4.9 27.3 25.6 0.107 TL 16.00 PV Pipe: 25 23.8 1.598 FL 10.00 PF 0.3 6 20.0 0.0 38.2 0.0 3.8 150 FTG E FE -4.3 16 30.0 0.0 33.6 0.0 0.015 TL 19.00 PV Pipe: 26 23.8 1.598 FL 12.00 PF 0.6 16 30.0 0.0 33.6 0.0 3.8 150 FTG 3T FE -1.7 17 34.0 0.0 31.3, 0.0 0.015 TL 36.00 PV Pipe: 29 -42.4 1.598 FL 11.00 PF 1.2 8 20.0 0.0 34.0 0.0 6.8 150 FTG ET PE -4.3 18 30.0 0.0 30.9 0.0 0.045 TL 28.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-2nd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUM. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 30 -42.4 1.598 PL 9.00 PF 1.2 18 30.0 0.0 30.9 0.0 6.8 150 FTG ET PE -1.7 19 34.0 0.0 30.3 0.0 0.045 TL 26.00 PV Pipe: 31 18.6 1.598 PL 10.00 PP 0.2 15 20.0 0.0 37.6 0.0 3.0 150 FTG T FE -4.3 20 30.0 0.0 33.0 0.0 0.010 TL 18.00 PV Pipe: 32 18.6 1.598 FL 9.00 PF 0.2 20 30.0 0.0 33.0 0.0 3.0 150 FTG 2T PE -1.7 21 34.0 0.0 31.1 0.0 0.010 TL 25.00 PV Pipe: 33 0.0 1.598 PL 6.50 PF 0.0 19 34.0 0.0 30.3 0.0 0.0 150 FTG T FE 1.5 22 30.5 0.0 31.8 0.0 0.000 TL 14.50 PV Pipe: 34 0.0 1.394 FL 7.50 PF 0.0 22 30.5 0.0 31.8 0.0 0.0 150 FTG T FE 0.0 23 30.5 0.0 31.8 0.0 0.000 TL 13.50 PV Pipe: 35 0.0 1.101 FL 3.00 PF 0.0 23 30.5 0.0 31.8 0.0 0.0 150 FTG ET PE 0.2 23A 30.0 0.0 32.0 0.0 0.000 TL 15.00 PV Pipe: 36 0.0 1.101 FL 7.00 PF 0.0 23 30.5 0.0 31.8 0.0 0.0 150 FTG E FE 0.2 24A 30.0 0.0 32.0 0.0 0.000 TL 14.00 PV Pipe: 37 0.0 1.394 PL 6.50 PF 0.0 22 30.5 0.0 31.8 0.0 0.0 150 FTG ---- FE 0.0 25 30.5 0.0 31.8 0.0 0.000 TL 6.50 PV Pipe: 38 0.0 1.101 FL 3.00 FE' 0.0 25 30.5 0.0 31.8 0.0 0.0 150 FTG ET FE 0.2 25A 30.0 0.0 32.0 0.0 0.000 TL 15.00 FV Pipe: 39 0.0 1.101 FL 6.00 PF 0.0 25 30.5 0.0 31.8 0.0 0.0 150 FTG 2E FE 0.2 26A 30.0 0.0 32.0 0.0 0.000 TL 20.00 PV Pipe: 40 23.8 1.598 FL 13.00 FE' 0.3 17 34.0 0.0 31.3 0.0 3.8 150 FTG .T FE 0.0 BB1 34.0 0.0 31.0 0.0 0.015 TL 21.00 PV Pipe: 41 23.8 1.598 FL 6.50 PF 0.5 BB1 34.0 0.0 31.0 0.0 3.8 150 FTG 2ET FE 0.0 BB2 34.0 0.0 30.5 0.0 0.015 TL 32.50 PV Pipe: 42 23.8 1.598 PL 3.00 FE' 0.2 BB2 34.0 0.0 30.5 0.0 3.8 150 FTG T FE 0.0 19 34.0 0.0 30.3 0.0 0.015 TL 11.00 PV 10 SPRINKLER SYSTEM HYDRAULIC ANALYSIS -Page 6 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD 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: 43 -18.6 1.598 PL 7.00 PF 0.1 19 34.0 0.0 30.3 0.0 3.0 150 FTG T PE 0.0 BB3 34.0 0.0 30.5 0.0 0.010 TL 15.00 PV Pipe: 44 -18.6 1.598 PL 6.00 PF 0.1 BB3 34.0 0.0 30.5 0.0 3.0 150 FTG T PE 0.0 BB4 34.0 0.0 30.6 0.0 0.010 TL 14.00 PV Pipe: 45 -18.6 1.598 PL 6.50 PF 0.3 BB4 34.0 0.0 30.6 0.0 3.0 150 FTG 2ET PE 0.0 BB5 34.0 0.0 30.9 0.0 0.010 TL 32.50 PV Pipe: 46 -18.6 1.598 PL 9.50 PF 0.2 BB5 34.0 0.0 30.9 0.0 3.0 150 FTG T PE 0.0 21 34.0 0.0 31.1 0.0 0.010 TL 17.50 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.004 gpm and a maximum imbalance at any node of 0.157 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 21.8 ft/sec at pipe 18. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRA14 FILES\HRS SYSTEMS\HASS82\C4815-B200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-2nd FLOOR PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Eli Tee LngEli ChkVlv BfyViv GatVlv AlmChk DPViv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 PAGE: H MATERIAL: CPVC HWC: 150 Diameter Equivalent Fitting Lengths in Feet (in) E T R K C L B L Ell Tee TEERUN COUPLG EL45 1.101 7.00 5.00 1.00 0.00 1.00 1.00 0.00 1.00 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 C U) 0 0 0 0 (N SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-3200.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 200 FOUR HEAD CALC-2nd FLOOR o 0 0 0 Cl 0 0 0 0 • • • • • . • • 0 0 0 0 0 0 0 0 0 CD U) ç) (N ED 0.)CJ)U) ZD 01 -Q.U)-d--- p SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 0 PRESS. 0 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE2 66.5 49.5 712.0 64.8 204.0 60.5 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 204.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 104.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE2 -1.0 SOURCE 60.5 104.0 DC 3.0 - - - - 58.7 DA 3.0 - - - - 51.7 U.1 1.0 - - - - 52.1 BOR 1.0 - - - - 52.0 TOR 9.5 - - - - 47.6 1 9.5 - - - - 45.2 2 9.5 ---- 44.0 3 9.5 - - - - 42.2 - - - 4 9.5 - - - - 42.1 - - - 5 20.0 - - - - 40.4 6 20.0 - - - - 40.3 7 20.0 - - - - 40.1 8 20.0 - - - - 39.3 9 20.0 - - - - 39.3 10 20.0 - - - - 33.7 - - - 11. 20.0 ---- 34.1 12 20.0 - - - - 31.6 13 20.0 - - - - 29.4 13A 19.5 K= 4.90 29.0 26.4 14A 19.5 K= 4.90 27.9 25.9 15 20.0 ---- 28.8 15A 19.5 K= 4.90 28.4 26.1 16A 19.5 K= 4.90 27.3 25.6 17 20.0 - - - - 37.5 - - - 18 20.0 - - - - 37.4 - - - 19 30.5 - - - - 35.3 20 34.0 - --- 33.5 21 30.5 - - - - 34.7 22 30.5 - - - - 34.6 23 30.5 - - - - 31.1 - - - 24 34.0 - - - - 30.7 - - - 25 30.5 - - - - 32.7 I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-2nd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 26 34.0 - - - - i 31.0 27 30.5 - - - - 34.6 28 30.5 -, - - - 34.6 - - - 28A 30.0 - - - - 34.8 29A 30.0 - - - - 34.8 30 30.5 - - - - 34.6 30A 30.0 - - - - 34.8 31A 30.0 - - - - 34.8 - - - EB1 34.0 - - - - 32.8 BB2 34.0 - - - - 32.5 BB3 34.0 - - - - 32.3 BB4 34.0 - - - - 30.9 BB5 34.0 - - - - 30.8 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CPLC-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: 1 104.0 5.850 PL 40.00 PF 0.1 SOURCE2 -1.0 SRCE 60.5 (N/A) 1.2 150 FTG TLG FE -1.7 DC 3.0 0.0 58.7 0.0 0.000 TL 148.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 58.7 0.0 7.0 psi, 104.0 gpm DA 3.0 0.0 51.7 0.0 Pipe: 3 104.0 4.070 FL 140.00 PF 0.5 DA 3.0 0.0 51.7 0.0 2.6 150 FTG ET FE 0.9 U.1 1.0 0.0 52.1 0.0 0.002 TL 187.80 PV Pipe: 4 104.0 4.220 FL 5.00 PF 0.1 U.1 1.0 0.0 52.1 0.0 2.4 140 FTG E PE 0.0 BOR 1.0 0.0 52.0 0.0 0.002 TL 21.73 PV Pipe: 5 104.0 2.703 PL 7.50 PF 0.8 BOR 1.0 0.0 52.0 0.0 5.8 120 FTG C FE -3.7 TOR 9.5 0.0 47.6 0.0 0.027 TL 29.26 PV Pipe: 6 104.0 2.423 FL 30.00 PF 2.4 TOR 9.5 0.0 47.6 0.0 7.2 150 FTG 4E PE 0.0 1 9.5 0.0 45.2 0.0 0.031 TL 78.00 PV Pipe: 7 85.9 2.003 PL 11.00 PF 1.1 1 9.5 0.0 45.2 0.0 8.7 150 FTG T FE 0.0 2 9.5 0.0 44.0 0.0 0.055 TL 21.00 PV Pipe: 8 76.7 2.003 PL 31.50 PF 1.8 2 9.5 0.0 44.0 0.0 7.8 150 FTG T PE 0.0 3 9.5 00 42.2 0.0 0.044 TL 41.50 PV Pipe: 9 13.9 2.003 PL 12.00 PF 0.0 3 9.5 0.0 42.2 0.0 1.4 150 FTG T PE 0.0 4 9.5 0.0 42.1 0.0 0.002 TL 22.00 PV Pipe: 11 18.0 1.598 PL 10.50 PF 02 1 9.5 0.0 45.2 0.0 2.9 150 FTG E PE -4.5 5 20.0 0.0 40.4 0.0 0.009 TL 19.50 PV Pipe: 12 18.0 1.598 FL 5.50 PF 0.1 5 20.0 0.0 40.4 0.0 2.9 150 FTG E FE 0.0 6 20.0 0.0 40.3 0.0 0.009 TL 14.50 PV Pipe: 13 18.0 1.598 PL 5.00 PF 0.2 6 20.0 0.0 40.3 0.0 2.9 150 FTG 2T FE 0.0 7 20.0 0.0 40.1 0.0 0.009 TL 21.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-3300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD 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: 14 9.2 1.598 PL 16.00 PF 0.1 2 9.5 0.0 44.0 0.0 1.5 150 FTG 3ET PE -4.5 8 20.0 0.0 39.3 0.0 0.003 TL 51.00 PV Pipe: 15 9.2 1.598 PL 2.00 PF 0.0 8 20.0 0.0 39.3 0.0 1.5 150 FTG T PE 0.0 9 20.0 0.0 39.3 0.0 0.003 TL 10.00 PV Pipe: 16 62.9 1.598 PL 16.00 PF 4.0 3 9.5 0.0 42.2 0.0 10.1 150 FTG 3E PE -4.5 10 20.0 0.0 33.7 0.0 0.092 TL 43.00 PV Pipe: 17 -41.1 1.598 PL 1.50 PF 0.4 10 20.0 0.0 33.7 0.0 6.6 150 FTG T PE 0.0 11 20.0 0.0 34.1 0.0 0.042 TL 9.50 PV Pipe: 18 104.0 1.394 PL 4.50 PP 2.0 10 20.0 0.0 33.7 0.0 21.9 150 FTG ---- PE 0.0 12 20.0 0.0 31.6 0.0 0.455 TL 4.50 PV Pipe: 19 52.2 1.101 PL 0.50 PF 2.2 12 20.0 0.0 31.6 0.0 17.6 150 FTG T PE 0.0 13 20.0 0.0 29.4 0.0 0.402 TL 5.50 PV Pipe: 20 26.4 1.101 PL 0.50 PF 0.6 13 20.0 0.0 29.4 0.0 8.9 150 FTG T PE 0.2 13A 19.5 4.9 29.0 26.4 0.114 TL 5.50 PV Pipe: 21 25.9 1.101 PL 9.00 PP 1.8 13 20.0 0.0 29.4 0.0 8.7 150 FTG E PE 0.2 14A 19.5 4.9 27.9 25.9 0.109 TL 16.00 PV Pipe: 22 51.7 1.394 PL 14.50 PF 2.8 12 20.0 0.0 31.6 0.0 10.9 150 FTG E PE 0.0 15 20.0 0.0 28.8 0.0 0.125 TL 22.50 PV Pipe: 23 26.1 1.101 PL 0.50 PF 0.6 15 20.0 0.0 28.8 0.0 8.8 150 FTG T PE 0.2 15A 19.5 4.9 28.4 26.1 0.111 TL 5.50 PV Pipe: 24 25.6 1.101 PL 9.00 PP 1.7 15 20.0 0.0 28.8 0.0 8.6 150 FTG E PE 0.2 16A 19.5 4.9 27.3 25.6 0.107 TL 16.00 PV Pipe: 25 13.9 1.598 PL 10.50 PF 0.1 4 9.5 0.0 42.1 0.0 2.2 150 FTG E PE -4.5 17 20.0 0.0 37.5 0.0 0.006 TL 19.50 PV Pipe: 26 13.9 1.598 PL 2.50 PF 0.1 17 20.0 0.0 37.5 0.0 2.2 150 FTG B PE 0.0 18 20.0 0.0 37.4 0.0 0.006 TL 11.50 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD 1,11 BUILDING TYPE 300 FOUR HEAD 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: 29 18.0 1.598 PL 13.00 PF 0.3 7 20.0 0.0 40.1 0.0 2.9 150 FTG ET PE -4.5 19 30.5 0.0 35.3 0.0 0.009 TL 30.00 PV Pipe: 30 18.0 1.598 PL 9.00 PF 0.2 19 30.5 0.0 35.3 0.0 2.9 150 FTG 2T PE -1.5 20 34.0 0.0 33.5 0.0 0.009 TL 25.00 PV Pipe: 31 9.2 1.598 PL 13.50 PF 0.1 9 20.0 0.0 39.3 0.0 1.5 150 FTG E2T PE -4.5 21 30.5 0.0 34.7 0.0 0.003 TL 38.50 PV Pipe: 32 9.2 1.598 PL 6.50 PF 0.0 21 30.5 0.0 34.7 0.0 1.5 150 FTG T PE 0.0 22 30.5 0.0 34.6 0.0 0.003 TL 14.50 PV Pipe: 33 -41.1 1.598 PL 13.50 PF 1.6 11 20.0 0.0 34.1 0.0 6.6 150 FTG E2T PE -4.5 23 30.5 0.0 31.1 0.0 0.042 TL 38.50 PV Pipe: 34 -41.1 1.598 PL 10.50 PP 1.1 23 30.5 0.0 31.1 0.0 6.6 150 FTG 2T PE -1.5 24 34.0 0.0 30.7 0.0 0.042 TL 26.50 PV Pipe: 35 13.9 1.598 PL 11.00 PF 0.2 18 20.0 0.0 37.4 0.0 2.2 150 FTG 2T PE -4.5 25 30.5 0.0 32.7 0.0 0.006 TL 27.00 PV Pipe: 36 13.9 1.598 PL 9.50 PF 0.2 25 30.5 0.0 32.7 0.0 2.2 150 FTG 3T PE -1.5 26 34.0 0.0 31.0 0.0 0.006 TL 33.50 PV Pipe: 37 0.0 1.598 PL 3.00 PF 0.0 22 30.5 0.0 34.6 0.0 0.0 150 FTG T PE 0.0 27 30.5 0.0 34.6 0.0 0.000 TL 11.00 PV Pipe: 38 0.0 1.394 PL 7.50 PF 0.0 27 30.5 0.0 34.6 0.0 0.0 150 FTG T PE 0.0 28 30.5 0.0 34.6 0.0 0.00.0 TL 13.50 PV Pipe: 39 0.0 1.101 PL 3.00 PF 0.0 28 30.5 0.0 34.6 0.0 0.0 150 FTG ET PE 0.2 28A 30.0 0.0 34.8 0.0 0.000 TL 15.00 PV Pipe: 40 0.0 1.101 PL 7.00 PF 0.0 28 30.5 0.0 34.6 0.0 0.0 150 FTG E PE 0.2 29A 30.0 0.0 34.8 0.0 0.000 TL 14.00 PV Pipe: 41 0.0 1.394 PL 6.00 PF 0.0 27 30.5 0.0 34.6 0.0 0.0 150 FTG ---- PE 0.0 30 30.5 0.0 34.6 0.0 0.000 TL 6.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 1 103.0 5.850 PL 40.00 PF 0.1 SOURCE2 -1.0 SRCE 62.1 (N/A) 1.2 150 FTG TLG PE 71.7 DC 3.0 0.0 60.3 0.0 0.000 TL 148.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 60.3 0.0 7.0 psi, 103.0 gpm DA 3.0 0.0 53.3 0.0 Pipe: 3 103.0 4.070 PL 140.00 PF 0.5 DA 3.0 0.0 53.3 0.0 2.5 150 FTG ET PE 0.9 U.1 1.0 0.0 53.7 0.0 0.002 TL 187.80 PV Pipe: 4 103.0 4.220 FL 5.00 FE' 0.1 U.1 1.0 0.0 53.7 0.0 2.4 140 FTG E PH 0.0 BOR 1.0 0.0 53.7 0.0 0.002 TL 21.73 PV Pipe: 5 103.0 2.703 PL 7.50 PF 0.8 BOR 1.0 0.0 53.7 0.0 5.8 120 FTG C PE -3.7 TOR 9.5 0.0 49.2 0.0 0.027 TL 29.26 PV Pipe: 6 103.0 2.423 FL 30.00 FE' 2.4 TOR 9.5 0.0 49.2 0.0 7.2 150 FTG 4E PE 0.0 1 9.5 0.0 46.9 0.0 0.030 TL 78.00 PV Pipe: 7 68.3 2.003 PL 11.00 FE' 0.8 1 9.5 0.0 46.9 0.0 7.0 150 FTG T FE 0.0 2 9.5 0.0 46.1 0.0 0.036 TL 21.00 PV Pipe: 8 30.4 2.003 PL 31.50 PF 0.3 2 9.5 0.0 46.1 0.0 3.1 150 FTG T PE 0.0 3 9.5 0.0 45.8 0.0 0.008 TL 41.50 PV Pipe: 9 14.3 2.003 PL 12.00 PF 0.0 3 9.5 0.0 45.8 0.0 1.5 150 FTG T PH 0.0 4 9.5 0.0 45.7 0.0 0.002 TL 22.00 PV Pipe: 11 34.7 1.598 FL 10.50 PF 0.6 1 9.5 0.0 46.9 0.0 5.6 150 FTG E PH -4.5 5 20.0 0.0 41.7 0.0 0.031 TL 19.50 PV Pipe: 12 34.7 1.598 PL 5.50 PF 0.4 5 20.0 0.0 41.7 0.0 5.6 150 FTG E PE 0.0 6 20.0 0.0 41.3 0.0 0.031 TL 14.50 PV Pipe: 13 34.7 1.598 PL 5.00 PF 0.6 6 20.0 0.0 41.3 0.0 5.6 150 FTG 2T PH 0.0 7 20.0 0.0 40.6 0.0 0.031 TL 21.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 14 37.9 1.598 FL 16.00 FE' 1.8 2 9.5 0.0 46.1 0.0 6.1 150 FTG 3ET PE -4.5 8 20.0 0.0 39.7 0.0 0.036 TL 51.00 PV Pipe: 15 37.9 1.598 PL 2.00 PF 0.4 8 20.0 0.0 39.7 0.0 6.1 150 FTG T FE 0.0 9 20.0 0.0 39.3 0.0 0.036 TL 10.00 PV Pipe: 16 16.2 1.598 PL 16.00 PF 0.3 3 9.5 0.0 45.8 0.0 2.6 150 FTG 3E FE -4.5 10 20.0 0.0 40.9 0.0 0.007 TL 43.00 PV Pipe: 17 16.2 1.598 PL 1.50 PF 0.1 10 20.0 0.0 40.9 0.0 2.6 150 FTG T PE 0.0 11 20.0 0.0 40.8 0.0 0.007 TL 9.50 PV Pipe: 18 0.0 1.394 PL 4.50 PF 0.0 10 20.0 0.0 40.9 0.0 0.0 150 FTG ---- FE 0.0 12 20.0 0.0 40.9 0.0 0.000 TL 4.50 PV Pipe: 19 0.0 1.101 PL 0.50 FE' 0.0 12 20.0 0.0 40.9 0.0 0.0 150 FTG T FE 0.0 13 20.0 0.0 40.9 0.0 0.000 TL 5.50 PV Pipe: 20 0.0 1.101 PL 0.50 PF 0.0 13 20.0 0.0 40.9 0.0 0.0 150 FTG T PE 0.2 13A 19.5 0.0 41.1 0.0 0.000 TL 5.50 PV Pipe: 21 0.0 1.101 PL 9.00 PF 0.0 13 20.0 0.0 40.9 0.0 0.0 150 FTG E FE 0.2 14A 19.5 0.0 41.1 0.0 0.000 TL 16.00 PV Pipe: 22 0.0 1.394 FL 14.50 PF 0.0 12 20.0 0.0 40.9 0.0 0.0 150 FTG E PE 0.0 15 20.0 0.0 40.9 0.0 0.000 TL 22.50 PV Pipe: 23 . 0.0 1.101 FL 0.50 PF 0.0 15 20.0 0.0 40.9 0.0 0.0 150 FTG T FE 0.2 15A 19.5 0.0 41.1 0.0 0.000 TL 5.50 PV Pipe: 24 0.0 1.101 FL 9.00 FE' 0.0 15 20.0 0.0 40.9 0.0 0.0 150 FTG E FE 0.2 16A 19.5 0.0 41.1 0.0 0.000 TL 16.00 PV Pipe: 25 14.3 1.598 FL 10.50 PF 0.1 4 9.5 0.0 45.7 0.0 2.3 150 FTG E PE -4.5 17 20.0 0.0 41.1 0.0 0.006 TL 19.50 PV Pipe: 26 14.3 1.598 PL 2.50 PF 0.1 17 20.0 0.0 41.1 0.0 2.3 150 FTG E FE 0.0 18 20.0 0.0 41.0 0.0 0.006 TL 11.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page ,5 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 29 34.7 1.598 PL 13.00 FE' 0.9 7 20.0 0.0 40.6 0.0 5.6 150 FTG ET PE -4.5 19 30.5 0.0 35.1 0.0 0.031 TL 30.00 PV Pipe: 30 34.7 1.598 FL 9.00 PF 0.8 19 30.5 0.0 35.1 0.0 5.6 150 FTG 2T PE -1.5 20 34.0 0.0 32.9 0.0 0.031 TL 25.00 PV Pipe: 31 37.9 1.598 PL 13.50 PF 1.4 9 20.0 0.0 39.3 0.0 6.1 150 FTG E2T PH -4.5 21 30.5 0.0 33.4 0.0 0.036 TL 38.50 PV Pipe: 32 37.9 1.598 PL 6.50 PF 0.5 21 30.5 0.0 33.4 0.0 6.1 150 FTG T PE 0.0 22 30.5 0.0 32.9 0.0 0.036 TL 14.50 PV Pipe: 33 16.2 1.598 FL 13.50 FE' 0.3 11 20.0 0.0 40.8 0.0 2.6 150 FTG E2T FE -4.5 23 30.5 0.0 36.0 0.0 0.007 TL 38.50 PV Pipe: 34 16.2 1.598 FL 10.50 PF 0.2 23 30.5 0.0 36.0 0.0 2.6 150 FTG 2T PE -1.5 24 34.0 0.0 34.3 0.0 0.007 TL 26.50 PV Pipe: 35 14.3 1.598 PL 11.00 PF 0.2 18 20.0 0.0 41.0 0.0 2.3 150 FTG 2T FE -4.5 25 30.5 0.0 36.3 0.0 0.006 TL 27.00 PV Pipe: 36 14.3 1.598 FL 9.50 PF 0.2 25 30.5 0.0 36.3 0.0 2.3 150 FTG 3T FE -1.5 26 34.0 0.0 34.6 0.0 0.006 TL 33.50 PV Pipe: 37 103.0 1.598 FL 3.00 PF 2.5 22 30.5 0.0 32.9 0.0 16.5 150 FTG T FE 0.0 27 30.5 0.0 30.3 0.0 0.230 TL 11.00 PV Pipe: 38 51.2 1.394 PL 7.50 PF 1.7 27 30.5 0.0 30.3 0.0 10.8 150 FTG T FE 0.0 28 30.5 0.0 28.7 0.0 0.123 TL 13.50 PV Pipe: 39 25.6 1.101 FL 3.00 FE' 1.6 28 -30.5 0.0 28.7 0.0 8.6 150 FTG ET PE 0.2 28A 30.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 40 25.6 1.101 FL 7.00 PF 1.5 28 30.5 0.0 28.7 0.0 8.6 150 FTG E FE 0.2 29A 30.0 4.9 27.4 25.6 0.108 TL 14.00 PV Pipe: 41 51.8 1.394 FL 6.00 FE' 0.8 27 30.5 0.0 30.3 0.0 10.9 150 FTG ---- PH 0.0 30 30.5 0.0 29.6 0.0 0.125 TL 6.00 PV 'I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/5/2012 C:\PROGRAM FILES\RRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 42 26.0 1.101 PL 3.50 PF 1.7 30 30.5 0.0 29.6 0.0 8.8 150 FTG ET PE 0.2 30A 30.0 4.9 28.1 26.0 0.110 TL 15.50 PV Pipe: 43 25.8 1.101 PL 5.00 PF 2.1 30 30.5 0.0 29.6 0.0 8.7 150 FTG 2E FE 0.2 31A 30.0 4.9 27.7 25.8 0.109 TL 19.00 PV Pipe: 44 34.7 1.598 PL 22.50 PF 1.5 20 34.0 0.0 32.9 0.0 5.6 150 FTG 2ET FE 1.5 22 30..5 0.0 32.9 0.0 0.031 TL 48.50 PV Pipe: 45 -30.4 1.598 FL 7.00 PF 0.4 22 30.5 0.0 32.9 0.0 4.9 150 FTG T PE -1.5 BB1 34.0 0.0 31.7 0.0 0.024 TL 15.00 PV Pipe: 46 -30.4 1.598 PL 6.00 PF 0.3 BB1 34.0 0.0 31.7 0.0 4.9 . 150 FTG T FE 0.0 BB2 34.0 0.0 32.1 0.0 0.024 TL 14.00 PV Pipe: 47 -30.4 1.598 FL 5.00 P 0.3 BB2 34.0 0.0 32.1 0.0 4.9 150 FTG T FE 0.0 BB3 34.0 0.0 32.4 0.0 0.024 TL 13.00 PV Pipe: 48 -30.4 1.101 FL 6.00 FE' 1.6 BB3 34.0 0.0 32.4 0.0 10.2 150 FTG T FE 0.0 BB4 34.0 0.0 34.0 0.0 0.148 TL 11.00 FV Pipe: 49 -30.4 1.598 FL 3.50 PF 0.3 BB4 34.0 0.0 34.0 0.0 4.9 150 FTG T FE 0.0 24 34.0 0.0 34.3 0.0 0.024 TL 11.50 PV Pipe: 50 -14.3 1.598 PL 3.00 FE' 0.1 24 34.0 0.0 34.3 0.0 2.3 150 FTG T FE 0.0 BB5 34.0 0.0 34.3 0.0 0.006 TL 11.00 FV Pipe: 51 -14.3 1.598 FL 20.00 PF 0.2 BBS 34.0 0.0 34.3 0.0 2.3 150 FTG 2E PE 0.0 26 34.0 0.0 34.6 0.0 0.006 TL 38.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems,. Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd FLOOR The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.066 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 16.5 ft/sec at pipe 37. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.PIP PAGE: * MATERIAL: S40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G A D N Ell Tee LngEll ChkVlv BfyVlv GatVlv AlmChk DPVlv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 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 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 0w 0. 0.1-IF-I 0 00 140 OC F-i •>,•0 I-- C) - l (I?C') (1)C U)0Q10 0(N u'J0.E 14 0 z G) 0 04 a) F4a)cn0 z 0. 0-. -4 - 'I a) -4(1) 0U)OW .00. 00.144-) (U F-i SU) 4(V) --Ic'J0>. I -A c p r-i U)(l) (U. 0'' W(N D 0-W / r-1(N ir I 0 0 0 '-4 0 0 a) 0 LI) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/5/2012 C:\PROGRAM FILES\I-iRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD ITT RTJTT.DTNP TYPF '1)1) vritlR 14F.Ar) (AT.(-rC PT.(Y)R 0 0 0 0 0 0 0 0 '-4 0 0 0 0 C) 0 0 0 0 ID N 0 U) (U' C') (N C,1a)C))DC-i -0.U)-H---- SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR READ CALC-3rd fLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE2 66.5 49.5 712.0 64.8 203.0 62.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 203.0 GPM TOTAL ROSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 103.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE2 -1.0 SOURCE 62.1 103.0 DC 3.0 - - - - 60.3 DA 3.0 - - - - 53.3 U.1 1.0 - - - - 53.7 BOR 1.0 53.7 TOR 9.5 - - - - 49.2 - - - 1 9.5 - - - - 46.9 - - - 2 9.5 - - - - 46.1 - - - 3 9.5 - - - 45.8 - - - 4 9.5 - - - - 45.7 5 20.0 - - - - 41.7 6 20.0 - - - - 41.3 7 20.0 - - - - 40.6 8 20.0 - - - - 39.7 9 20.0 - - - - 39.3 - - - 10 20.0 - - - - 40.9 - - - 11 20.0 - - - - 40.8 12 20.0 - - - - 40.9 - - - 13 20.0 - - - - 40.9 13A 19.5 - - - - 41.1 14A 19.5 - - - - 41.1 - - - 15 20.0 - - - - 40.9 - - - 15A 19.5 - --- 41.1 16A 19.5 - - - - 41.1 - - - 17 20.0 - - - - 41.1 18 20.0 - - - - 41.0 19 30.5 - - - - 35.1 20 34.0 - - - - 32.9 21 30.5 - - - - 33.4 22 30.5 - - - - 32.9 23 30.5 - - - - 36.0 - - - 24 34.0 - - - - 34.3 25 30.5 ---- 36.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd fLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 26 34.0 - - - - 34.6 27 30.5 - - - - 30.3 28 30.5 - - - - 28.7 28A 30.0 K= 4.90 27.3 25.6 29A 30.0 K= 4.90 27.4 25.6 30 30.5 - - - - 29.6 30A 30.0 K= 4.90 28.1 26.0 31A 30.0 K= 4.90 27.7 25.8 BB1 34.0 - - - - 31.7 BB2 34.0 - - - - 32.1 BB3 34.0 ---- 32.4 BB4 34.0 - - - - 34.0 - - - BB5 34.0 - - - - 34.3 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRA14 FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 1 103.0 5.850 PL 40.00 PF 0.1 SOURCH2 -1.0 SRCE 62.1 (N/A) 1.2 150 FTG TLG PH -1.7 DC 3.0 0.0 60.3 0.0 0.000 TL 148.55 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 60.3 0.0 7.0 psi, 103.0 gpm DA 3.0 0.0 53.3 0.0 Pipe: 3 103.0 4.070 PL 140.00 PF 0.5 DA 3.0 0.0 53.3 0.0 2.5 150 FTG ET PE 0.9 U.1 1.0 0.0 53.7 0.0 0.002 TL 187.80 PV Pipe: 4 103.0 4.220 PL 5.00 PF 0.1 U.1 1.0 0.0 53.7 0.0 2.4 140 FTG E PE 0.0 BOR 1.0 0.0 53.7 0.0 0.002 TL 21.73 PV Pipe: 5 103.0 2.703 PL 7.50 PF 0.8 BOR 1.0 0.0 53.7 0.0 5.8 120 FTG C PH -3.7 TOR 9.5 0.0 49.2 0.0 0.027 TL 29.26 PV Pipe: 6 103.0 2.423 PL 30.00 PF 2.4 TOR 9.5 0.0 49.2 0.0 7.2 150 FTG 4E PH 0.0 1 9.5 0.0 46.9 0.0 0.030 TL 78.00 PV Pipe: 7 68.3 2.003 PL 11.00 PF 0.8 1 9.5 0.0 46.9 0.0 7.0 150 FTG I T PH 0.0 2 9.5 0.0 46.1 0.0 0.036 TL 21.00 PV Pipe: 8 30.4 2.003 PL 31.50 PF 0.3 2 9.5 0.0 46.1 0.0 3.1 150 FTG T PE 0.0 3 9.5 0.0 45.8 0.0 0.008 TL 41.50 PV Pipe: 9 14.3 2.003 PL 12.00 PF 0.0 3 9.5 0.0 45.8 0.0 1.5 150 FTG T PH 0.0 4 9.5 0.0 45.7 0.0 0.002 TL 22.00 PV Pipe: 11 34.7 1.598 FL 10.50 PF 0.6 1 9.5 0.0 46.9 0.0 5.6 150 FTG E PH -4.5 5 20.0 0.0 41.7 0.0 0.031 TL 19.50 PV Pipe: 12 34.7 1.598 PL 5.50 PF 0.4 5 20.0 0.0 41.7 0.0 5.6 150 FTG H PH 0.0 6 20.0 0.0 41.3 0.0 0.031 TL 14.50 PV Pipe: 13 34.7 1.598 PL 5.00 PF 0.6 6 20.0 0.0 41.3 0.0 5.6 150 FTG 2T PH 0.0 7 20.0 0.0 40.6 0.0 0.031 TL 21.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 14 37.9 1.598 PL 16.00 PF 1.8 2 9.5 0.0 46.1 0.0 6.1 150 FTG 3ET PE -4.5 8 20.0 0.0 39.7 0.0 0.036 TL 51.00 PV Pipe: 15 37.9 1.598 FL 2.00 FE' 0.4 8 20.0 0.0 39.7 0.0 6.1 150 FTG T FE 0.0 9 20.0 0.0 39.3 0.0 0.036 TL 10.00 PV Pipe: 16 16.2 1.598 PL 16.00 PF 0.3 3 9.5 0.0 45.8 0.0 2.6 150 FTG 3E FE -4.5 10 20.0 0.0 40.9 0.0 0.007 TL 43.00 PV Pipe: 17 16.2 1.598 FL 1.50 PF 0.1 10 20.0 0.0 40.9 0.0 2.6 150 FTG T FE P.O 11 20.0 0.0 40.8 0.0 0.007 TL 9.50 PV Pipe: 18 0.0 1.394 FL 4.50 PF 0.0 10 20.0 0.0 40.9 0.0 0.0 150 FTG ---- FE 0.0 12 20.0 0.0 40.9 0.0 0.000 TL 4.50 PV Pipe: 19 0.0 1.101 FL 0.50 PF 0.0 12 20.0 0.0 40.9 0.0 0.0 150 FTG T FE 0.0 13 20.0 0.0 40.9 0.0 0.000 TL 5.50 PV Pipe: 20 0.0 1.101 FL 0.50 PF 0.0 13 20.0. 0.0 40.9 0.0 0.0 150 FTG T PE 0.2 13A 19.5 0.0 41.1 0.0 0.000 TL 5.50 PV Pipe: 21 0.0 1.101 FL 9.00 PF 0.0 13 20.0 0.0 40.9 0.0 0.0 150 FTG B FE 0.2 14A 19.5 0.0 41.1 0.0 0.000 TL 16.00 PV Pipe: 22 0.0 1.394 FL 14.50 PF 0.0 12 20.0 0.0 40.9 0.0 0.0 150 FTG B PE 0.0 15 20.0 0.0 40.9 0.0 0.000 TL 22.50 PV Pipe: 23 0.0 1.101 FL 0.50 PF 0.0 15 20.0 0.0 40.9 0.0 0.0 150 FTG T FE 0.2 15A 19.5 0.0 41.1 0.0 0.000 TL 5.50 PV Pipe: 24 0.0 1.101 FL 9.00 PF 0.0 15 20.0 0.0 40.9 0.0 0.0 150 FTG E FE 0.2 16A 19.5 0.0 41.1 0.0 0.000 TL 16.00 PV Pipe: 25 14.3 1.598 FL 10.50 PF 0.1 4 9.5 0.0 45.7 0.0 2.3 150 FTG E FE -4.5 17 20.0 0.0 41.1 0.0 0.006 TL 19.50 PV Pipe: 26 14.3 1.598 FL 2.50 PF 0.1 17 20.0 0.0 41.1 0.0 2.3 150 FTG E FE 0.0 18 20.0 0.0 41.0 0.0 0.006 TL 11.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 29 34.7 1.598 PL 13.00 PF 0.9 7 20.0 0.0 40.6 0.0 5.6 150 FTG ET PE -4.5 19 30.5 0.0 35.1 0.0 0.031 TL 30.00 PV Pipe: 30 34.7 1.598 PL 9.00 PF 0.8 19 30.5 0.0 35.1 0.0 5.6 150 FTG 2T PE -1.5 20 34.0 0.0 32.9 0.0 0.031 TL 25.00 PV Pipe: 31 37.9 1.598 PL 13.50 PF 1.4 9 20.0 0.0 39.3 0.0 6.1 150 FTG E2T PE -4.5 21 30.5 0.0 33.4 0.0 0.036 TL 38.50 PV Pipe: 32 37.9 1.598 PL 6.50 PF 0.5 21 30.5 0.0 33.4 0.0 6.1 150 FTG T PE 0.0 22 30.5 0.0 32.9 0.0 0.036 TL 14.50 PV Pipe: 33 16.2 1.598 PL 13.50 PF 0.3 11 20.0 0.0 40.8 0.0 2.6 150 FTG E2T PE -4.5 23 30.5 0.0 36.0 0.0 0.007 TL 38.50 PV Pipe: 34 16.2 1.598 PL 10.50 PF 0.2 23 30.5 0.0 36.0 0.0 2.6 150 FTG 2T PE -1.5 24 34.0 0.0 34.3 0.0 0.007 TL 26.50 PV Pipe: 35 14.3 1.598 PL 11.00 PF 0.2 18 20.0 0.0 41.0 0.0 2.3 150 FTG 2T PE -4.5 25 30.5 0.0 36.3 0.0 0.006 TL 27.00 PV Pipe: 36 14.3 1.598 PL 9.50 PF 0.2 25 30.5 0.0 36.3 0.0 2.3 150 FTG 3T PE -1.5 26 34.0 0.0 34.6 0.0 0.006 TL 33.50 PV Pipe: 37 103.0 1.598 PL 3.00 PF 2.5 22 30.5 0.0 32.9 0.0 16.5 150 FTG T PE 0.0 27 30.5 0.0 30.3 0.0 0.230 TL 11.00 PV Pipe: 38 51.2 1.394 PL 7.50 PF 1.7 27 30.5 0.0 30.3 0.0 10.8 150 FTG T PE 0.0 28 30.5 0.0 28.7 0.0 0.123 TL 13.50 PV Pipe: 39 25.6 1.101 PL 3.00 PP 1.6 28 30.5 0.0 28.7 0.0 8.6 150 FTG ET PE 0.2 28A 30.0 4.9 27.3 25.6 0.107 TL 15.00 PV Pipe: 40 25.6 1.101 PL 7.00 PF 1.5 28 30.5 0.0 28.7 0.0 8.6 150 FTG E PE 0.2 29A 30.0 4.9 27.4 25.6 0.108 TL 14.00 PV Pipe: 41 51.8 1.394 PL 6.00 PF 0.8 27 30.5 0.0 30.3 0.0 10.9 150 FTG ---- PE 0.0 30 30.5 0.0 29.6 0.0 0.125 TL 6.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/5/2012 C:\PROGRP.M FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd 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: 42 26.0 1.101 FL 3.50 PF 1.7 30 30.5 0.0 29.6 0.0 8.8 150 FTG ET PE 0.2 30A 30.0 4.9 28.1 26.0 0.110 TL 15.50 PV Pipe: 43 25.8 1.101 PL 5.00 PF 2.1 30 30.5 0.0 29.6 0.0 8.7 150 FTG 2E PE 0.2 31A 30.0 4.9 27.7 25.8 0.109 TL 19.00 PV Pipe: 44 34.7 1.598 FL 22.50 PF 1.5 20 34.0 0.0 32.9 0.0 5.6 150 FTG 2ET FE 1.5 22 30.5 0.0 32.9 0.0 0.031 TL 48.50 PV Pipe: 45 -30.4 1.598 PL 7.00 FE' 0.4 22 30.5 0.0 32.9 0.0 4.9 150 FTG T PE -1.5 BB1 34.0 0.0 31.7 0.0 0.024 TL 15.00 PV Pipe: 46 -30.4 1.598 PL 6.00 PF 0.3 BB1 34.0 0.0 31.7 0.0 4.9 150 FTG T PE 0.0 BB2 34.0 0.0 32.1 0.0 0.024 TL 14.00 PV Pipe: 47 -30.4 1.598 FL 5.00 PF 0.3 BB2 34.0 0.0 32.1 0.0 4.9 150 FTG T PE 0.0 BB3 34.0 0.0 32.4 0.0 0.024 TL 13.00 PV Pipe: 48 -30.4 1.101 PL 6.00 PF 1.6 BB3 34.0 0.0 32.4 0.0 10.2 150 FTG T FE 0.0 BB4 34.0 0.0 34.0 0.0 0.148 TL 11.00 FV Pipe: 49 -30.4 1.598 FL 3.50 PF 0.3 BB4 34.0 0.0 34.0 0.0 4.9 150 FTG T PE 0.0 24 34.0 0.0 34.3 0.0 .0.024 TL 11.50 PV Pipe: 50 -14.3 1.598 FL 3.00 PF 0.1 24 34.0 0.0 34.3 0.0 2.3 150 FTG T FE 0.0 BBS 34.0 0.0 34.3 0.0 0.006 TL 11.00 PV Pipe: 51 -14.3 1.598 FL 20.00 PF 0.2 BBS 34.0 0.0 34.3 0.0 2.3 150 FTG 2E FE 0.0 26 34.0 0.0 34.6 0.0 0.006 TL 38.00 PV NOTES (HASS): (1) Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRi'M FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd fLOOR The system has been calculated to.provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.066 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 16.5 ft/sec at pipe 37. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 BfyVlv GatVlv AlmChk DPVlv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 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 1.394 8.00 6.00 1.00 0.00 1.00 2.00 0.00 2.00 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 I ID 0 0 '-I 0 C U) 0 0 LI) 0 C) 0 0 C,) 0 C (N SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815-B300.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 300 FOUR HEAD CALC-3rd fLOOR E 0. 0.1-il-I ci) 00 14(D 11)0 • c-I •>t) U)Q U)CQ.CU WC'l U)C'0.E ci z Q. -- lCI) 0U)OW 00. w0.c4-I-' HC') --4('0>, -H U) i 14 U) U) (ci. 0. 0-Ic').. cD DgIW / / -- IImI Cl 0 ID 0 0 0 C) Q . . . . • • • • C) CD C) C 0 C C CD U) N ko If) C') (N 0.U)U)U)1I —Q.U).H--- 0 N0. CD 0 C C SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-2nd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 66.5 49.5 712.0 64.8 205.9 61.0 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 205.9 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 105.9 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE -1.0 SOURCE 61.0 105.9 DC 3.0 - - - - 59.2 - - - DA 3.0 - - - - 52.2 U.1 1.0 - - - - 52.4 BOR 1.0 - - - - 52.3 TOR 9.5 - - - - 47.8 1 9.5 - - - - 45.6 - - - 2 9.5 - - - - 44.5 - - - 3 9.5 - - - - 43.2 - - - 4 9.5 - - - - 43.1 - - - 5 9.5 - - - - 43.1 - - - 6 20.0 - - - - 40.9 7 20.0 - - - - 40.7 8 20.0 - - - 40.6 - - - 9 20.0 - - - - 39.7 - - - 10 20.0 - - - - 39.6 - - - 11 20.0 - - - - 35.8 -- - 12 20.0 - - - - 35.1 13 20.0 - - - - 32.4 13A 19.5 K= 4.90 30.8 27.2 14A 19.5 K= 4.90 30.9 27.3 15 20.0 - - - - 29.3 iSA 19.5 K= 4.90 27.3 25.6 16 20.0 - - - - 29.1 16A 19.5 K= 4.90 27.8 25.8 17 20.0 - - - - 38.4 18 20.0 - - - - 38.4 - - - 19 20.0 - - - - 38.5 20 20.0 - - - - 38.5 21 30.5 - - - - 35.6 22 34.0 - - - - 33.7 23 30.5 - - - - 34.9 24 34.0 - - - - 33.2 $1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-2nd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25 30.5 - - - - 31.8 26 34.0 - - - - 31.7 27 30.5 - - - - 33.8 - - - 28 34.0 - - - - 32.2 29 30.5 33.9 30 34.0 - - - - 32.3 31 30.5 - - - - 31.8 - - - 31A 30.0 - - - - 32.0 - - - 32 30.5 - - - - 31.8 - - - 32A 30.0 - ---- 32.0 33 30.5 - - - - 31.8 - - - 33A 30.0 - - - - 32.0 34A 30.0 - - - - 32.0 BB1 34.0 - - - - 32.5 BB2 34.0 - - - - 32.1 BB3 34.0 - - - - 31.8 BB4 34.0 - - - - 30.3 3B5 34.0 - - - - 32.0 IN SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR 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.: 1 105.9 5.850 PL 15.00 PF 0.0 SOURCE -1.0 SRCE 61.0 (N/A) 1.3 150 FTG TG PE -1.7 DC 3.0 0.0 59.2 0.0 0.000 TL 98.74 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 59.2 0.0 7.0 psi, 105.9 gpm DA 3.0 0.0 52.2 0.0 Pipe: 3 105.9 4.070 PL 200.00 PF 0.6 DA 3.0 0.0 52.2 0.0 2.6 150 FTG ET PE 0.9 U.1 1.0 0.0 52.4 0.0 0.003 TL 247.80 PV Pipe: 4 105.9 4.220 PL 5.00 PF 0.1 U.1 1.0 0.0 52.4 0.0 2.4 140 FTG EL PE 0.0 BOR 1.0 0.0 52.3 0.0 0.002 TL 31.76 PV Pipe: 5 105.9 2.703 PL . 7.50 PF 0.8 BOR 1.0 0.0 52.3 0.0 5.9 120 FTG C PE -3.7 TOR 9.5 0.0 47.8 0.0 0.028 TL 29.26 PV Pipe: 6 . 105.9 2.423 PL 32.50 PF 2.2 TOR 9.5 0.0 47.8 0.0 7.4 150 FTG 3E PE 0.0 1 9.5 0.0 45.6 0.0 0.032 TL 68.50 .PV Pipe: 7 85.3 2.003 PL 11.00 PF 1.1 1 . 9.5 0.0 45.6 0.0 8.7 150 FTG T PE 0.0 2 9.5 0.0 44.5 0.0 0.054 TL 21.00 PV Pipe: 8 71.4 2.003 PL 22.50 PF 1.3 2 9.5 0.0 44.5 0.0 7.3 150 FTG T PE 0.0 3 9.5 0.0 43.2 0.0 0.039 TL 32.50 PV Pipe: 9 18.1 2.003 PL 31.50 PF 0.1 3 9.5 0.0 43.2 0.0 1.8 150 FTG T PE 0.0 4 9.5 0.0 43.1 0.0 0.003 TL 41.50 PV Pipe: 10 8.8 2.003 PL 12.00 PF 0.0 4 9.5 0.0 43.1 0.0 0.9 150 FTG T PE 0.0 5 9.5 0.0 43.1 0.0 0.001 TL 22.00 PV Pipe: 11 20.5 1.598 PL 10.50 PF 0.2 1 9.5 0.0 45.6 0.0 3.3 150 FTG E PE -4.5 6 20.0 0.0 40.9 0.0 0.012 TL 19.50 PV Pipe: 12 20.5 1.598 PL 5.50 PF 0.2 6 20.0 0.0 40.9 0.0 3.3 150 FTG B PE 0.0 7 20.0 0.0 40.7 0.0 0.012 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD 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 20.5 1.598 PL 3.00 PF 0.1 7 20.0 0.0 40.7 0.0 3.3 150 FTG T PE 0.0 8 20.0 0.0 40.6 0.0 0.012 TL 11.00 PV Pipe: 14 14.0 1.598 PL 16.00 PF 0.3 2 9.5 0.0 44.5 0.0 2.2 150 FTG 3ET PE -4.5 9 20.0 0.0 39.7 0.0 0.006 TL 51.00 PV Pipe: 15 14.0 1.598 PL 2.00 PF 0.1 9 20..0 0.0 39.7 0.0 2.2 150 FTG T PE 0.0 10 20.0 0.0 39.6 0.0 0.006 TL 10.00 PV Pipe: 16 53.3 1.598 PL 16.00 PF 2.9 3 9.5 0.0 43.2 0.0 8.5 150 FTG 3E PE -4.5 11 20.0 0.0 35.8 0.0 0.068 TL 43.00 PV Pipe: 17 53.3 1.598 PL 2.50 PF 0.7 11 20.0 0.0 35.8 0.0 8.5 150 FTG T PE 0.0 12 20.0 0.0 35.1 0.0 0.068 TL 10.50 PV Pipe: 18 105.9 1.598 PL 3.00 PF 2.7 12 20.0 0.0 35.1 0.0 16.9 150 FTG T PE 0.0 13 20.0 0.0 32.4 0.0 0.242 TL 11.00 PV Pipe: 19 27.2 1.101 PL 3.00 PF 1.8 13 20.0 0.0 32.4 0.0 9.2 150 FTG ET PE 0.2 13A 19.5 4.9 30.8 27.2 0.120 TL 15.00 PV Pipe: 20 27.3 1.101 PL 7.00 PF 1.7 13 20.0 0.0 32.4 0.0 9.2 150 FTG E PE 0.2 14A 19.5 4.9 30.9 27.3 0.121 TL 14.00 PV Pipe: 21 51.4 1.101 PL 8.00 PF 3.1 13 20.0 0.0 32.4 0.0 17.3 150 FTG ---- PE 0.0 15 20.0 0.0 29.3 0.0 0.390 TL 8.00 PV Pipe: 22 25.6 1.101 PL 8.50 PF 2.2 15 20.0 0.0 29.3 0.0 8.6 150 FTG ET PE 0.2 15A 19.5 4.9 27.3 25.6 0.107 TL 20.50 PV Pipe: 23 25.8 1.101 PL 2.00 PF 0.2 15 20.0 0.0 29.3 0.0 8.7 150 FTG ---- PE 0.0 16 20.0 0.0 29.1 0.0 0.109 TL 2.00 PV Pipe: 24 25.8 1.101 PL 2.00 PF 1.5 16 20.0 0.0 29.1 0.0 8.7 150 FTG ET PE 0.2 16A 19.5 4.9 27.8 25.8 0.109 TL 14.00 PV Pipe: 25 9.3 1.598 PL 16.00 PF 0.1 4 9.5 0.0 43.1 0.0 1.5 150 FTG 3ET PE -4.5 17 20.0 0.0 38.4 0.0 0.003 TL 51.00 PV I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRZ-\M FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD 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: 26 9.3 1.598 PL 2.00 PF 0.0 17 20.0 0.0 38.4 0.0 1.5 150 FTG T PE 0.0 18 20.0 0.0 38.4 0.0 0.003 TL 10.00 PV Pipe: 27 8.8 1.598 PL 10.50 PF 0.0 5 9.5 0.0 43.1 0.0 1.4 150 FTG E PE -4.5 19 20.0 0.0 38.5 0.0 0.002 TL 19.50 PV Pipe: 28 8.8 1.598 FL 2.50 PF 0.0 19 20.0 0.0 38.5 0.0 1.4 150 FTG E PE 0.0 20 20.0 0.0 38.5 0.0 0.002 TL 11.50 PV Pipe: 29 20.5 1.598 PL 15.00 PF 0.5 8 20.0 0.0 40.6 0.0 3.3 150 FTG E2T PE -4.5 21 30.5 0.0 35.6 0.0 0.012 TL 40.00 PV Pipe: 30 20.5 1.598 FL 9.00 PF 0.3 21 30.5 0.0 35.6 0.0 3.3 150 FTG ET PE -1.5 22 34.0 0.0 33.7 0.0 0.012 TL 26.00 PV Pipe: 31 14.0 1.598 FL 11.00 PF 0.2 10 20.0 0.0 39.6 0.0 2.2 150 FTG ET FE -4.5 23 30.5 0.0 34.9 0.0 0.006 TL 28.00 PV Pipe: 32 14.0 1.598 FL 13.00 FE' 0.2 23 30.5 0.0 34.9 0.0 2.2 150 FTG E2T PE -1.5 24 34.0 0.0 33.2 0.0 0.006 TL 38.00 PV Pipe: 33 -52.6 1.598 PL 10.50 PF 1.3 12 20.0 0.0 35.1 0.0 8.4 150 FTG E PE -4.5 25 30.5 0.0 31.8 0.0 0.066 TL 19.50 PV Pipe: 34 -52.6 1.598 FL 6.00 FE' 1.5 25 30.5 0.0 31.8 0.0 8.4 150 FTG 2T FE -1.5 26 34.0 0.0 31.7 0.0 0.066 TL 22.00 PV Pipe: 35 9.3 1.598 FL 11.00 PF 0.1 18 20.0 0.0 38.4 0.0 1.5 150 FTG ET FE -4.5 27 30.5 0.0 33.8 0.0 0.003 TL 28.00 PV Pipe: 36 9.3 1.598 FL 13.00 PF 0.1 27 30.5 0.0 33.8 0.0 1.5 150 FTG 3T FE -1.5 28 34.0 0.0 32.2 0.0 0.003 TL 37.00 PV Pipe: 37 8.8 1.598 FL 10.00 PF 0.0 20 20.0 0.0 38.5 0.0 1.4 150 FTG T FE -4.5 29 30.5 0.0 33.9 0.0 0.002 TL 18.00 PV Pipe: 38 8.8 1.598 FL 9.50 FE' 0.1 29 30.5 0.0 33.9 0.0 1.4 150 FTG 3T FE -1.5 30 34.0 0.0 32.3 0.0 0.002 TL 33.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD 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: 39 20.5 1.598 PL 22.50 PF 0.6 22 34.0 0.0 33.7 0.0 3.3 150 FTG 2ET PE 0.0 2,4 34.0 0.0 33.2 0.0 0.012 TL 48.50 PV Pipe: 40 34.5 1.598 PL 14.50 PF 0.7 24 34.0 0.0 33.2 0.0 5.5 150 FTG T PE 0.0 EB1 34.0 0.0 32.5 0.0 0.030 TL 22.50 PV Pipe: 41 34.5 1.598 PL 5.00 PF 0.4 BB1 34.0 0.0 32.5 0.0 5.5 150 FTG T PE 0.0 BB2 34.0 0.0 32.1 0.0 0.030 TL 13.00 PV Pipe: 42 34.5 1.598 FL 3.50 Pr 0.3 BB2 34.0 0.0 32.1 0.0 5.5 150 FTG T PE 0.0 26 34.0 0.0 31.7 0.0 0.030 TL 11.50 PV Pipe: 43 -18.1 1.598 PL 2.00 PF 0.1 26 34.0 0.0 31.7 0.0 2.9 150 FTG T PE 0.0 BB3 34.0 0.0 31.8 0.0 0.009 TL 10.00 FV Pipe: 44 -18.1 1.598 PL 11.00 PF 0.2 BB3 34.0 0.0 31.8 0.0 2.9 150 FTG T FE 0.0 BB5 34.0 0.0 32.0 0.0 0.009 TL 19.00 PV Pipe: 45 -18.1 1.598 FL 9.50 PF 0.2 BB5 34.0 0.0 32.0 0.0 2.9 150 FTG T FE 0.0 28 34.0 0.0 32.2 0.0 0.009 TL 17.50 PV Pipe: 46 -8.8 1.598 FL 23.00 Pr 0.1 28 34.0 0.0 32.2 0.0 1.4 150 FTG 2ET FE 0.0 30 34.0 0.0 32.3 0.0 , 0.002 TL 49.00 PV Pipe: 47 0.0 1.598 FL 1.50 Pr 0.0 25 30.5 0.0 31.8 0.0, 0.0 150 FTG ---- FE 0.0 31 30.5 0.0 31.8 0.0 0.000 TL 1.50 PV Pipe: 48 0.0 1.101 FL 8.00 PF 0.0 31 30.5 0.0 31.8 0.0 0.0 150 FTG ET FE 0.2 31A 30.0 0.0 32.0 0.0 0.000 TL 20.00 PV Pipe: 49 0.0 1.598 FL 1.00 Pr 0.0 31 30.5 0.0 31.8 , 0.0 0.0 150 FTG ---- FE 0.0 32 30.5 0.0 31.8 0.0 0.000 TL ' 1.00 PV Pipe: 50 0.0 1.101 FL 5.50 Pr 0.0 32 30.5 0.0 31.8 0.0 0.0 150 FTG E2T PE 0.2 32A 30.0 0.0 32.0 0.0 0.000 TL 22.50 PV Pipe: 51 0.0 1.101 FL 6.50 Pr 0.0 32A 30.0 0.0 32.0 0.0 0.0 150 FTG E FE -1.7 BB4 34.0 0.0 30.3 0.0 0.000 TL 13.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD 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: 52 0.0 1.101 PL 5.50 PF 0.0 32 30.5 0.0 31.8 0.0 0.0 150 FTG ---- PE 0.0 33 30.5 0.0 31.8 0.0 0.000 TL 5.50 PV Pipe: 53 0.0 1.101 PL 2.00 PF 0.0 33 30.5 0.0 31.8 0.0 0.0 150 FTG ET PS 0.2 33A 30.0 0.0 32.0 0.0 0.000 TL 14.00 PV Pipe: 54 0.0 1.101 PL 9.50 PF 0.0 33 30.5 0.0 31.8 0.0 0.0 150 FTG 2E PE 0.2 34A 30.0 0.0 32.0 0.0 0.000 TL 23.50 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 16080621 granted by HRS Systems, Inc. 208 South Public 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 0.062 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 17.3 ft/sec at pipe 21. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 BfyVlv GatVlv AlmChk DPViv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/5/2012 C:\-PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-2nd FLOOR 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 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 70.0 G A 60.0 U G E 50.0 P R E S 40.0 S U R E 30.0 p s 20.0 i WATER SUPPLY ANALYSIS Static: 66.50 psi Resid: 49.50 psi Flow: 712.0 gpm LEGEND 1 Available pressure 64.79 psi @ 205.9 gpm 2 Required pressure 60.95 psi @ 205.9 gpm Source Supply Curve System Demand Curve 10.0 -14.' 200 300 400 500 bUU 'uu ouu 1000 FLOW (GPM) SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 1 DATE: 9/5/2012 C:\PROGRAN FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd FLOOR WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. 8 PRESS. 8 DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 66.5 49.5 712.0 64.8 205.0 62.3 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 205.0 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 100.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 105.0 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) SOURCE -1.0 SOURCE 62.3 105.0 DC 3.0 - - - - 60..5 DA 3.0 - - - - 53.5 U.1 1.0 - - - - 53.7 BOR 1.0 - - - - 53.6 TOR 9.5 - - - - 49.2 1 9.5 - - - - 47.0 - - - 2 9.5 - - - - 45.9 - - - 3 9.5 - - - - 44.8 - - - 4 9.5 - - - - 44.6 - - - 5 9.5 - - - - 44.5 - - - 6 20.0 - - - - 42.2 7 20.0 - - - - 42.0 8 20.0 - - - - 41.9 - - - 9 20.0 - - - - 41.0 - - - 10 20.0 - - - - 40.9 - - - 11 20.0 - - - - 38.2 - - - 12 20.0 - - - - 37.7 - - - 13 20.0 - - - - 37.7 13A 19.5 - - - - 37.9 14A 19.5 - - - - 37.9 - - - 15 20.0 - - - - 37.7 15A 19.5 - - - - 37.9 16 20.0 - - - - 37.7 16A 19.5 - - - - 37.9 - - - 17 20.0 - - - - 39.8 - - - 18 20.0 - - - - 39.8 - - - 19 20.0 - - - - 39.9 - - 20 20.0 - - - - 39.9 - - - 21 30.5 - - - - 36.8 - - - 22 34.0 - - - - 35.0 23 30.5 - - - - 36.2 24 34.0 - - - - 34.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd FLOOR NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 25 30.5 - - - - 32.3 26 34.0 - - - - 32.7 27 30.5 - - - - 35.1 - - - 28 34.0 - - - - 33.4 - - - 29 30.5 - - - - 35.2 - - - 30 34.0 - - - - 33.6 31 30.5 - - - - 31.9 31A 30.0 K= 4.90 29.8 26.7 32 30.5 - - - - 31.8 - - - 32A 30.0 K= 4.90 29.4 26.6 33 30.5 - - - - 29.6 33A 30.0 K= 4.90 28.3 26.1 34A 30.0 K= 4.90 27.3 25.6 BB1 34.0 - - - - 33.6 BB2 34.0 - - - - 33.1 BB3 34.0 - - - - 32.8 BB4 34.0 - - - - 27.7 BB5 34.0 - - - - 33.1 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd 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: 1 105.0 5.850 PL 15.00 PF 0.0 SOURCE -1.0 SRCE 62.3 (N/A) 1.3 150 FTG TG PH -1.7 DC 3.0 0.0 60.5 0.0 0.000 TL 98.74 PV Pipe: 2 FIXED PRESSURE LOSS DEVICE DC 3.0 0.0 60.5 0.0 7.0 psi, 105.0 gpm DA 3.0 0.0 53.5 0.0 Pipe: 3 105.0 4.070 PL 200.00 PF 0.6 DA 3.0 0.0 53.5 0.0 2.6 150 FTG ET PH 0.9 U.1 1.0 0.0 53.7 0.0 0.003 TL 247.80 PV Pipe: 4 105.0 4.220 PL 5.00 PF 0.1 U.1 1.0 0.0 53.7 0.0 2.4 140 FTG EL PE 0.0 BOR 1.0 0.0 53.6 0.0 0.002 TL 31.76 PV Pipe: 5 105.0 2.703 PL 7.50 PF 0.8 BOR 1.0 0.0 53.6 0.0 5.9 120 FTG C PE -3.7 TOR 9.5 0.0 49.2 0.0 0.028 TL 29.26 PV Pipe: 6 105.0 2.423 PL 32.50 PF 2.1 TOR 9.5 0.0 49.2 0.0 7.3 150 FTG 3E PE 0.0 1 9.5 0.0 47.0 0.0 0.031 TL 68.50 PV Pipe: 7 83.4 2.003 PL 11.00 PF 1.1 1 9.5 0.0 47.0 0.0 8.5 150 FTG T PE 0.0 2 9.5 0.0 45.9 0.0 0.052 TL 21.00 PV Pipe: 8 67.4 2.003 PL 22.50 PF 1.1 2 9.5 0.0 45.9 0.0 6.9 150 FTG T PH 0.0 3 9.5 0.0 44.8 0.0 0.035 TL 32.50 PV Pipe: 9 23.8 2.003 PL 31.50 PF 0.2 3 9.5 0.0 44.8 0.0 2.4 150 FTG T PH 0.0 4 9.5 0.0 44.6 0.0 0.005 TL 41.50 PV Pipe: 10 11.6 2.003 PL 12.00 PF 0.0 4 9.5 0.0 44.6 0.0 1.2 150 FTG T PH 0.0 5 9.5 0.0 44.5 0.0 0.001 TL 22.00 PV Pipe: 11 21.5 1.598 PL 10.50 PF 0.2 1 9.5 0.0 47.0 0.0 3.4 150 FTG H PH -4.5 6 20.0 0.0 42.2 0.0 0.013 TL 19.50 PV Pipe: 12 21.5 1.598 PL 5.50 PF 0.2 6 20.0 0.0 42.2 0.0 3.4 150 FTG H PE 0.0 7 20.0 0.0 42.0 0.0 0.013 TL 14.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/5/2012 C:\PROGRN4 FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd 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 21.5 1.598 PL 3.00 PF 0.1 7 20.0 0.0 42.0 0.0 3.4 150 FTG T PE 0.0 8 20.0 0.0 41.9 0.0 0.013 TL 11.00 PV Pipe: 14 16.1 1.598 PL 16.00 PF 0.4 2 9.5 0.0 45.9 0.0 2.6 150 FTG 3ET FE -4.5 9 20.0 0.0 41.0 0.0 0.007 TL 51.00 PV Pipe: 15 16.1 1.598 FL 2.00 PF 0.1 9 20.0 0.0 41.0 0.0 2.6 150 FTG T PE 0.0 10 20.0 0.0 40.9 0.0 0.007 TL 10.00 PV Pipe: 16 43.6 1.598 FL 16.00 PF 2.0 3 9.5 0.0 44.8 0.0 7.0 150 FTG 3E PE -4.5 11 20.0 0.0 38.2 0.0 0.047 TL 43.00 PV Pipe: 17 43.6 1.598 PL 2.50 PF 0.5 11 20.0 0.0 38.2 0.0 7.0 150 FTG T PE 0.0 12 20.0 0.0 37.7 0.0 0.047 TL 10.50 PV Pipe: 18 0.0 1.598 PL 3.00 PF 0.0 12 20.0 0.0 37.7 0.0 0.0 150 FTG T PE 0.0 13 20.0 0.0 37.7 0.0 0.000 TL 11.00 PV Pipe: 19 0.0 1.101 PL 3.00 PF 0.0 13 20.0 0.0 37.7 0.0 0.0 150 FTG ET FE 0.2 13A 19.5 0.0 37.9 0.0 0.000 TL 15.00 PV Pipe: 20 0.0 1.101 PL 7.00 FE' 0.0 13 20.0 0.0 37.7 0.0 0.0 150 FTG E PE 0.2 14A 19.5 0.0 37.9 0.0 0.000 TL 14.00 PV Pipe: 21 0.0 1.101 PL 8.00 PF 0.0 13 20.0 0.0 37.7 0.0 0.0 150 FTG ---- FE 0.0 15 20.0 0.0 37.7 0.0 0.000 TL 8.00 PV Pipe: 22 0.0 1.101 FL 8.50 PF 0.0 15 20.0 0.0 37.7 0.0 0.0 150 FTG ET PE 0.2 iSA 19.5 0.0 37.9 0.0 0.000 TL 20.50 PV Pipe: 23 0.0 1.101 PL 2.00 PF 0.0 15 20.0 0.0 37.7 0.0 0.0 150 FTG ---- FE 0.0 16 20.0 0.0 37.7 0.0 0.000 TL 2.00 PV Pipe: 24 0.0 1.101 PL 2.00 PF 0.0 .16 20.0 0.0 37.7 0.0 0.0 150 FTG ET FE 0.2 16A 19.5 0.0 37.9 0.0 0.000 TL 14.00 PV Pipe: 25 12.2 1.598 FL 16.00 PF 0.2 4 9.5 0.0 44.6 0.0 2.0 150 FTG 3ET FE -4.5 17 20.0 0.0 39.8 0.0 0.004 TL 51.00 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/5/2012 C:\PROGRI\N FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd FLOOR PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. NOZ. PT DISC. VEL(FFS) HW(C) (FT) SUN. NODES (FT) (K) (PSI) (GPM) FL/FT (PSI) Pipe: 26 12.2 1.598 PL 2.00 FE' 0.0 17 20.0 0.0 39.8 0.0 2.0 150 FTG T PE 0.0 18 - 20.0 0.0 39.8 0.0 0.004 TL 10.00 PV Pipe: 27 11.6 1.598 PL 10.50 PF 0.1 5 9.5 0.0 44.5 0.0 1.9 150 FTG E FE -4.5 19 20.0 0.0 39.9 0.0 0.004 TL 19.50 PV Pipe: 28 11.6 1.598 FL 2.50 PF 0.0 19 20.0 0.0 39.9 0.0 1.9 150 FTG E FE 0.0 20 20.0 0.0 39.9 0.0 0.004 TL 11.50 PV Pipe: 29 21.5 1.598 PL 15.00 PF 0.5 8 20.0 0.0 41.9 0.0 3.4 150 FTG E2T PE -4.5 .21 30.5 0.0 36.8 0.0 0.013 TL 40.00 PV Pipe: 30 21.5 1.598 PL 9.00 PF 0.3 21 30.5 0.0 36.8 0.0 3.4 150 FTG ET FE -1.5 22 34.0 0.0 35.0 0.0 0.013 TL 26.00 PV Pipe: 31 16.1 1.598 FL 11.00 PF 0.2 10 20.0 0.0 40.9 0.0 2.6 150 FTG ET FE '-4.5 23 30.5 0.0 36.2 0.0 0.007 TL 28.00 PV Pipe: 32 16.1 1.598 FL 13.00 PF 0.3 23 30.5 0.0 36.2 0.0 2.6 150 FTG E2T FE. -1.5 24 34.0 0.0 34.4 0.0 0.007 TL 38.00 PV Pipe: 33 43.6 1.598 FL 10.50 PF 0.9' 12 20.0 0.0 37.7 0.0 7.0 150 FTG E FE -4.5 25 30.5 0.0 32.3 0.0 0.047 TL 19.50 PV Pipe: 34 -61.4 1.598 FL .6.00 PF 1.9 25 30.5 0.0 32.3 0.0 9.8 150 FTG 2T FE -1.5 26 34.0 0.0 32.7 0.0 0.088 TL 22.00 PV Pipe: 35 12.2 1.598 FL 11.00 PF 0.1 18 20.0 0.0 39.8 0.0 2.0 150 FTG ET FE -4.5 27 30.5 0.0 35.1 0.0 0.004 TL 28.00 PV Pipe: 36 12.2 1.598 FL 13.00 PF 0.2 27 30.5 0.0 35.1 0.0 2.0 150 FTG 3T FE -1.5 28 34.0 0.0 33.4 0.0 0.004 TL 37.00 PV Pipe: 37 11.6 1.598 FL 10.00 PF 0.1 20 20.0 0.0 39.9 0.0 1.9 150 FTG T FE -4.5 29 30.5 0.0 35.2 0.0 0.004 TL 18.00 PV Pipe: 38 11.6 1.598 FL 9.50 PF 0.1 29 30.5 0.0 35.2 0.0 1.9 150 FTG I 3T FE -1.5 30 34.0 0.0 33.6 0.0 0.004 TL 33.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/5/2012 C:\PROGRNJ FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd 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: 39 21.5 1.598 PL 22.50 PF 0.6 22 34.0 0.0 35.0 0.0 3.4 150 FTG 2ET PE 0.0 24 34.0 0.0 34.4 0.0 0.013 TL 48.50 PV Pipe: 40 37.6 1.598 PL 14.50 PF 0.8 24 34.0 0.0 34.4 0.0 6.0 150 FTG T PE 0.0 BB1 34.0 0.0 33.6 0.0 0.036 TL 22.50 PV Pipe: 41 37.6 1.598 PL 5.00 PF 0.5 BB1 34.0 0.0 33.6 0.0 6.0 150 FTG T PE 0.0 BB2 34.0 0.0 33.1 0.0 0.036 TL 13.00 PV Pipe: 42 37.6 1.598 PL 3.50 PF 0.4 BB2 34.0 0.0 33.1 0.0 6.0 150 FTG T PE 0.0 26 34.0 0.0 32.7 0.0 0.036 TL 11.50 PV Pipe: 43 -23.8 1.598 PL 2.00 PF 0.2 26 34.0 0.0 32.7 0.0 3.8 150 FTG T PE 0.0 B83 34.0 0.0 32.8 0.0 0.015 TL 10.00 PV Pipe: 44 -23.8 1.598 PL 11.00 PF 0.3 BB3 34.0 0.0 32.8 0.0 3.8 150 FTG T PE 0.0 BBS 34.0 0.0 33.1 0.0 0.015 TL 19.00 PV Pipe: 45 -23.8 1.598 PL 9.50 PF 0.3 BB5 34.0 0.0 33.1 0.0 3.8 150 FTG T PE 0.0 28 34.0 0.0 33.4 0.0 0.015 TL 17.50 PV Pipe: 46 -11.6 1.598 PL 23.00 FE' 0.2 28 34.0 0.0 33.4 0.0 1.9 150 FTG 2ET PE 0.0 30 34.0 0.0 33.6 0.0 0.004 TL 49.00 PV Pipe: 47 105.0 1.598 PL 1.50 PF 0.4 25 30.5 0.0 32.3 0.0 16.8 150 FTG ---- PE 0.0 31 30.5 0.0 31.9 0.0 0.238 TL 1.50 PV Pipe: 48 26.7 1.101 PL 8.00 PF 2.3 31 30.5 0.0 31.9 0.0 9.0 150 FTG ET PE 0.2 31A 30.0 4.9 29.8 26.7 0.116 TL 20.00 PV Pipe: 49 78.2 1.598 PL 1.00 PF 0.1 31 30.5 0.0 31.9 0.0 12.5 150 FTG ---- PE 0.0 32 30.5 0.0 31.8 0.0 0.138 TL 1.00 PV Pipe: SO 26.6, 1.101 PL 550 PF 2.6 32 30.5 0.0 31.8 0.0 9.0 150 FTG E2T PE 0.2 32A 30.0 4.9 29.4 26.6 0.115 TL 22.50 PV Pipe: 51 0.0 1.101 PL 6.50 PF 0.0 32A 30.0 4.9 29.4 26.6 0.0 150 FTG E PE -1.7 BB4 34.0 0.0 27.7 0.0 0.000 TL 13.50 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 9/5/2012 C:\PROGRAJ4 FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd 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: 52 51.7 1.101 PL, 5.50 PF 2.2 32 30.5 0.0 31.8 0.0 17.4 150 FTG ---- PE 0.0 33 30.5 0.0 29.6 0.0 0.394 TL 5.50 PV Pipe: 53 26.1 1.101 PL 2.00 PF 1.6 33 30.5 0.0 29.6 0.0 8.8 150 FTG ET PE 0.2 33A 30.0 4.9 28.3 26.1 0.111 TL 14.00 PV Pipe: 54 25.6 1.101 PL 9.50 PF 2.5 33 30.5 0.0 29.6 0.0 8.6 150 FTG 2E PE 0.2 34A 30.0 4.9 27.3 25.6 0.107 TL 23.50 PV NOTES (HASS): Calculations were performed by the HASS 8.2 computer program under license no. 1080621 granted by HRS Systems, Inc. 208 South Public Square Petersburg, TN 37144 (931) 659-9760 The system has been calculated to provide an average imbalance at each node of 0.002 gpm and a maximum imbalance at any node of 0.104 gpm. Total pressure at each node is used in balancing the system. Maximum water velocity is 17.4 ft/sec at pipe 52. Items listed in bold print on the cover sheet are automatically transferred from the calculation report. PIPE FITTINGS TABLE Pipe Table Name: FSS.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 BfyVlv GatVlv AlmChk DPVlv NPTee 2.703 9.33 18.65 6.22 21.76 10.88 1.55 15.54 15.54 18.65 4.070 10.54 21.09 6.33 23.20 12.65 2.11 21.09 21.09 21.09 4.220 12.58 25.15 7.55 27.67 15.09 2.52 25.15 25.15 25.15 5.850 24.63 51.31 16.42 55.42 18.47 4.10 43.10 43.10 51.31 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd FLOOR 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 1.598 9.00 8.00 1.00 0.00 1.00 2.00 0.00 2.00 2.003 11.00 10.00 1.00 0.00 1.00 2.00 0.00 2.00 2.423 12.00 12.00 2.00 0.00 2.00 3.00 0.00 3.00 I 0 0 C. Lo 0 0 C-.-) 0 0 UI SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 9/5/2012 C:\PROGRAM FILES\HRS SYSTEMS\HASS82\C4815.SDF JOB TITLE: CARLSBAD III BUILDING TYPE 400 FOUR HEAD CALC-3rd FLOOR Wa) I 0. 0.4 w vu O WO m 0tt)-f fn C) 0)OQ.0) WC'J O)C'Jp.E I-I a) W 1 0.a) )-i*,C/)Q Z 0. °-'--' -14 W 5 I -- HO) 00)OW 00. ø-)0.4-) Cl) p ::io) HO -14Lfl0>1 co (n (U. tr• :W('J w ko / -4 UI FIC N 0 0 0 0 0 0 0 Co 0 . • 0 • 0 . • 0 0 • • 0 . co H 0 0 0 0 I N ko Lo () C'.) H ti E 0 ("1 H 0 H r1 U) 0. 0 Lo Cl) 1) U) 0. C) LU tD kD Cl) '—I l-4) Z 4 >l 04 04 Cl) Contractor's Material and Test Certificate for Aboveground Piping As I 1 PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. PROPERTY ADDRESS 1854 ARROYO WILLOW LANE ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE ADDRESS 1854 AR PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS ZYES ENO EQUIPMENT USED IS APPROVED EYES 0 N IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION Z YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN El NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES Z YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA 25 0 YES El NO El NO El NO 0 NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 TycoBBi TY3180 2012 1/2 55 200 Tyco AP TY3190 2012 1/2 44 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR FLOW TYPE MAKE MODEL MIN SEC Flow POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE AIR POINT PRESSURE TIME WATER REACHED - TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC PSI PSI PSI MIN SEC YES NO WITH Q.O.D. W/O Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODEL I DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN SEC PRESSURE REDUCING LOCATION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE & FLOOR MODEL (FLOWING) FLOW RATE VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED El YES 0 NO EQUIPMENT OPERATES PROPERLY M YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? M YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 0 YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING R YES ONO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING M YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? 0 YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? 0 YES El NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? 0 YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA ZYES ENO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAME OF SPRINKER CONTRACTOR: Innovatiye-Fire Protection4nc. SIGNATURES WITNESSED BY C.TESTS OR PROPEFTY OWNR1SIGNED) TITLE DATE FOR SPRINKLER CONTRACTOR (SIGNED) TITLE DATE ADDITIONAL EXPLANATIONS AND NOTES: Contractor's Material and Test Certificate for Aboveground Piping A 12-0119 PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractors personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. -- PROPERTY ADDRESS 1851 ARROYO WILLOW CT ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE ADDRESS 1851 ARROY( PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS Z YES El NO EQUIPMENT USED IS APPROVED Z YES El NO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION Z YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN El NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES Z YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS Z YES NFPA25 DYES El NO El NO El NO El NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 Tyco BBI 1Y3180 2012 1/2 55 200 Tyco AP TY3190 2012 1/2 44 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE MODEL MIN SEC FLOW Flow POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. - DRY PIPE OPERATING TIME TOTRIP THROUGH TEST CONNECTION WATER PRESSURE AIR PRESSURE TRIP POINT AIR PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC PSI PSI PSI MIN SEC YES NO WITH Q.O.D. w/O Q.O.D. IFNO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODE J DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN SEC rIouFct LUUA I IUN MAFSL & Sb I I IN( STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING &FLOOR MODEL (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) OSTATI rostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTIONA damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test ff pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 1% psi in 24 hours. ' ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED El YES El NO EQUIPMENT OPERATES PROPERLY N YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF.SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? N YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 N YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING N YES ENO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING N YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? N YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? N YES El NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? N YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA NYES [:1 NO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAMEOF SPRINKER CONTRACTOR: Innovative.Fjie Protection,,4nc. SIGNATURES TESTS WITNESSED BY (SIGNED) TITLE DATE j FOR SPRINKLER CONTRACTOR (SIGNED) TITLE DATE ADDITIONAL EXPLANATIONS AND NOTES: ! I L Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. 4 ,' PROPERTY NAME CARLSBAD III - BUILDING 3 I DATE t-rl PROPERTY ADDRESS 1856 SEA ROCKET LANE 0 ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE I ADDRESS 1856 SEA ROCKET LANE - PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS EYES El NO EQUIPMENT USED IS APPROVED YES ONO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 0 YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN El NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES 0 YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS Z YES NFPA25 EYES El NO 0 NO 0 NO JNO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE . MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 112 326 165 Reliable FI/RES 49 2012 112 118 175 TycoBBI TY3180 2012 1/2 . 55 200 Tyco AP TY3190 2012 1/2 44 1 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST.CONNECTION OR TYPE MAKE I MODEL MIN SEC FLOW Flow I POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. - DRY PIPE OPERATING TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE AIR POINT PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC PSI PSI PSI MIN _J_ SEC YES NO WITH Q.O.D. W/° Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & PREACTION VALVES DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO El NO MAKE I I MODE LI I DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE_ YES I NO YES NO MIN I SEC PRESSURE I LOCATION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING &fjQQR MODEL (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static YES pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 1 1/2 psi in 24 hours. - ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED El YES El NO -EQUIPMENT OPERATES PROPERLY N YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? N YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI 7 CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 N YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING N YES E]NO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING YES -NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? -s-YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? -YES El NO : DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? .YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA NYES ONO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAME OF SPRINKER CONTRACTOR: Innovative Fire Protection, Inc. SIGNATURES TESTS WITNESSED BY R ROPERTY OWNER (SIGNED) TITLEC, DAT/?ZP. OR IS Py(Lç,CTOR (SIGNED) TIJE DATE >' 7 7 ADDITIONAL EXPLANANf'Jb NOTE'S Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractors representative and witnessed by an owner's representative. All defects' shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is C' understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. PROPERTY ADDRESS 1855 SEA ROCKET LANE ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE PLANS ADDRESS 1855 SEA ROCKET LANE INSTALLATION CONFORMS TO ACCEPTED PLANS EQUIPMENT USED IS APPROVED IF NO, EXPLAIN DEVIATIONS ED YES El NO YES DNO INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 0 YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN 0 NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES ED YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA25 DYES 0 NO 0 NO 0 NO NO 'a LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 Tyco BBI TY3180 2012 1/2 55 200 Tyco AP TY3190 2012 1/2 44 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE MODEL MIN SEC FLOW Flow POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING iTIME TO TRIP ,. ' THROUGH TEST ' CONNECTION WATER PRESSURE AIR PRESSURE RIP POINT AIR PRESSURE TIME WATER REACHED TEST OUTLET - ALARM OPERATED PROPERLY TEST ." MIN SEC PSI PSI PSI MIN SEC I YES NO :.wlTH. Q.O.D: W/O Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC DELUGE & PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODE J DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN SEC rNt.urw LULA I IUN MAIS,L & bti I INi STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING & FLOOR MODEL (FLOWING) VALVE TEST ., INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pessure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED 0 YES El NO EQUIPMENT OPERATES PROPERLY M YES fl NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? M YES []NO DRAIN: READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST SUPPLY TEST CONNECTION PSI 72 CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 0 YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING M YES EINO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING M YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? 0 YES 0 NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? 0 YES 0 NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? 0 YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA OYES DNO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS NAME OF SPRINKER CONTRACTOR: Innovative Fire Protection, Inc. SIGNATURES TESTS WITNESSED BY R OPERTY OWNER (SIGNED) TiTLE DATE, 2i- 6RIqRINKLA CQfITRAQ?(OR (SIGIIED) TIJkE DATE ctAi ADDI1]ONALEXPLAATIÔ'Ar4WF1b'T I. I fj l• '1' :Contractor's.Material and Test Cétificate for Aboveground Piping AS I2ct 2... PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. (1] A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to , ) comply with approving authority's requirements or local ordinances. PROPERTY NAME CARLSBAD III - BUILDING 7 I DATE 17 .IIlr3 PROPERTY ADDRESS 6921 BRASS BUTTONS ST ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE ADDRESS 6921 BRASS BUTTONS ST PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS 0 YES El NO EQUIPMENT USED IS APPROVED 0 YES El NO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 0 YES OFCONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN D NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES 0 YES SYSTEM COMPONENTS INSTRUCTIONS ZYES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA25 DYES El NO El NO 0 NO El NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 Tyco BBI TY3180 1 2012 1/2 55 1 200 Tyco AP TY3190 1 2012 1/2 44 1 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE'OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR ! TYPE MAKE MODEL MIN SEC FLOW Flow r .,.'tairE POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING 'TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE POINT AIR PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC I PSI PSI PSI MIN SEC YES NO WITH Q:O.D. W/O . Q.O.D. IF NO, EXPLAIN OPERATIbN fl PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES ISTHERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE I MODE U DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN I SEC PRESSURE REDUCING LOCATION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE &frLOOR MODEL (FLOWING) FLOW RATE VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at ntJsshn 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static pressUre in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damae All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 1% psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED E YES E NO EQUIPMENT OPERATES PROPERLY M YES D NO DQYOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? M YES D NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE IN TEST TESTS TEST .. SUPPLY TEST CONNECTION PSI CONNECTION OPEN WIDE PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 ZYES EJNO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING M YES EINO IF-,POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS . WELDED PIPING M YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? ED YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? Z YES El NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY;CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? M YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA YES [:1 NO NAMEPLATE DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. REMARKS . NA~401,91F, SPRINKER.CONTRACTOR: Iñróativé Fire Protection, Inc. SIGNATURES TESTS WLNESS D BY TITLE / DATE FOR SPRINKLER CONTRAR (SIGNED) TITLE _-- DATE ADDITIONAL EXPLANATIONS AND NOTE7V 2' I h I I I I''i ,ItI III: .4 Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's represe.ptatiI defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owiersandcontractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, póorworkmanship, or failure to comply with approving authority's requirements or local ordinances. PROPERTY NAME CARLSBAD Ill - BUILDING 9 I DATE H i PROPERTY ADDRESS 1864 BRANT LANE ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE C 1864 BRANT LANE PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS YES ONO EQUIPMENT USED IS APPROVED ED YES DNO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION Z YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN 0 NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES Z YES SYSTEM COMPONENTS INSTRUCTIONS ED YES CARE AND MAINTENANCE INSTRUCTIONS Z YES NFPA 25 0 YES 0 NO 0 NO 0 NO 0 NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 Tyco BBI a3180 2012 1/2 55 200 Tyco AP TY3190 2012 1/2 44 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE MODEL MIN SEC FLOW Flow POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING TIME TO TRIP THROUGH TEST CONNECTION WATER PRESSURE AIR PRESSURE TRIP POINT AIR_PRESSURE TIME WATER REACHED OUTLET .TEST ALARM OPERATED PROPERLY TEST MIN SEC I PSI PSI PSI MIN SEC YES NO WITH Q.O.D. W/O Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODE J DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATELVE RELEASE VA MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN SEC rmmaaumm LL)L,/\ I IUIN & tiLiTIN(.i STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING & FLOOR MODEL (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DECiPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/2 psi in 24 hours. 4 " ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON 2 DRY PIPING PNEUMATICALLY TESTED LI YES El NO EQUIPMENT OPERATES PROPERLY YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? M YES El NO DRAIN READING OF GAGE LOCATED EAR WATER RESIDUAL PRESSURE WITH VALVE I...TEST TESTS TEST SUPPLY TEST CONNECTION -t PSI CONNECTION OPEN WIDE L 3 PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 YES El NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING R YES E1NO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING M YES El NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? ED YES El NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? Z YES El NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA 0 YES El NO NAMEPLATE REMARKS 13 DATE LEFT IN SERVICE WITH ALL CONTROL VALVES OPEN. ( -\ j I NAME OFRINKER CONTRACTOR: lnnovath/ire Protection. Inc. SIGNATURES /f TESTS WITNESSED BY FOR70PE7WNTNED FO/H1(LER CONTRACT -(ef E3 TITLE DATE ADDITIONAL EXPLNTIONS AND NOTES: Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. PROPERTY ADDRESS 1861 ALKALI HEATH LANE ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE HEATH LANE PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS ZYES ENO EQUIPMENT USED IS APPROVED ZYES Li NO IF NO, EXPLAIN DEVIATIONS INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION 0 YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN 0 NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES ED YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS 0 YES NFPA 25 Li YES Li NO Li NO Li NO Li NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FI/RES 49 2012 1/2 118 175 Tyco BBI 1Y3180 1 2012 1/2 1 55 1 200 Tyco AP TY3190 2012 1/2 1 44 1 200 PIPE AND FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE MODEL MIN SEC FLOW Flow I POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL SERIAL NO. DRY PIPE OPERATING TIME TO TRIP THROUGH TEST CONNECTION :. WATER PRESSURE AIR TRIP PRESSURE POINT AIR PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC PSI PSI PSI MIN SEC YES NO WITH Q.O.D. W/O Q.O.D. IF NO, EXPLAIN OPERATION Li PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El YES El NO DETECTING MEDIA SUPERVISED El YES El NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS , El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE MODE J DOES EACH CIRCUIT OPERATE SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE YES NO YES NO MIN I SEC PREbbUKh LL)LAI ION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING & FLOOR MODEL (FLOWING) VALVE TEST INLET (PSI) OUTLET (PSI) INLET (PSI) OUTLET (PSI) FLOW (GPM) HYDROSTATIC: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours or 50 psi (3.4 bars) above static TEST pressure in excess of 150 psi (10.2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 1% psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED LI YES LI NO EQUIPMENT OPERATES PROPERLY M YES El NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? R YES El NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VIAL IN TEST TESTS TEST SUPPLY TEST CONNECTION .Q PSI CONNECTION OPEN WIDE b 5 PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 Z YES LI NO OTHER EXPLAIN FLUSHED BY INSTALLER QFI.JJ'IDERGROUND SPRINKER PIPING NI YES ENO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? El YES El NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING NI YES [1 NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? NI YES LI NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? NI YES LI NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? NI YES El NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? El YES El NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA ZYES LINO NAMEPLATE DATE LEF IN SERVICE WITH ALL CONTROL VALVES OPEN. 1 REMARKS NAME 91F SPRINK6ACTOR: Innovaftive FireMotectio . Inc. SIGNATURES 1.11 4 TESTS LINE SED-BY FO PR ERTY OW R (SIGNED) ITLE LATE 0 SPRINKLER CONTRACTOR (SIGNED) TITLE DATE ADDITIONAL EXPLANATIONS AND NOTES: Contractor's Material and Test Certificate for Aboveground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the Contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. - - -- - PROPERTY ADDRESS 1862 ALKALI HEATH LANE ACCEPTED BY APPROVING AUTHORITIES (NAMES) CARLSBAD FIRE ALKALI HEATH LANE PLANS INSTALLATION CONFORMS TO ACCEPTED PLANS EQUIPMENT USED IS APPROVED IF NO, EXPLAIN DEVIATIONS ZYES DNO ZYES El NO INSTRUCTIONS HAS PERSON IN CHARGE OF FIRE EQUIPMENT BEEN INSTRUCTED AS TO LOCATION Z YES OF CONTROL VALVES AND CARE AND MAINTENANCE OF THEIS NEW EQUIPMENT? IF NO, EXPLAIN 0 NO HAVE COPIES OF THE FOLLOWING BEEN LEFT ON THE PREMISES ED YES SYSTEM COMPONENTS INSTRUCTIONS Z YES CARE AND MAINTENANCE INSTRUCTIONS ED YES NFPA25 DYES 0 NO 0 NO El NO 0 NO LOCATION SUPPLIES BUILDINGS SPRINKLERS MAKE MODEL YEAR OF MANUFACTURE ORIFICE SIZE QUANTITY -- TEMPERATURE RATING Reliable RFC 49 2012 1/2 326 165 Reliable FIIRES 49 2012 1/2 118 175 Tyco BBI D3180 2012 1/2 55 200 Tyco AP TY3190 2012 1/2 44 200 PIPE AND -_FITTINGS TYPE OF PIPE STEEL and CPVC TYPE OF FITTINGS STEEL and CPVC ALARM VALVE ALARM DEVICE MAXIMUM TIME TO OPERATE THROUGH TEST CONNECTION OR TYPE MAKE MODEL . MIN SEC FLOW Flow POTTER VSR 45 INDICATOR MAKE MODEL SERIAL NO. MAKE MODEL' SERIAL NO. DRY PIPE OPERATING TIME TO TRIP . THROUGH TEST CONNECTION WATER PRESSURE AIR TRIP PRESSURE POINT 4IR PRESSURE TIME WATER REACHED TEST OUTLET ALARM OPERATED PROPERLY TEST MIN SEC I PSI - . PSI PSI MIN SEC YES NO WITH Q.O.D. W/O Q.O.D. IF NO, EXPLAIN OPERATION El PNEUMATIC El ELECTRIC El HYDRAULIC PIPING SUPERVISED El__ YES El_NO -- DETECTING MEDIA SUPERVISED El_ YES El_NO DELUGE & DOES THE VALVE OPERATE FROM THE MANUAL TRIP AND/OR REMOTE CONTROL STATIONS El YES El NO PREACTION VALVES IS THERE AN ACCESSIBLE FACILITY IN EACH CIRCUIT IF NO, EXPLAIN FOR TESTING? El YES El NO MAKE I DOES EACH CIRCUIT OPERATE SUPERVISION SUPERVISION LOSS ALARM DOES EACH CIRCUIT OPERATE VALVE RELEASE MAXIMUM TIME TO OPERATE RELEASE ,MODE YES NO YES NO MIN SEC PRESSURE LOCATION MAKE & SETTING STATIC PRESSURE RESIDUAL PRESSURE FLOW RATE REDUCING & FLOOR MODEL (FLOWING) VALVE TEST INLET(PSI) OUTLET(PSI) INLET(PSI) OUTLET(PSI) FLOW(GPM) 7.t HYDROSTATI01 C: Hydrostatic tests shall be made at not less than 200 psi (13.6 bars) for two hours 0r50 psi (3.4 bars) above static iE'ST ' pressure in excess of 150 psi (10,2 bars) for two hours. Differential dry-pipe valve clappers shall be left open during test to prevent DESCRIPTION damage. All aboveground piping leakage shall be stopped. PNEUMATIC: Establish 40 psi (2.7 bars) air pressure and measure drop, which shall not exceed 11/2 psi (0.1 bars) in 24 hours. Test pressure tanks at normal water level and air pressure and measure air pressure drop which shall not exceed 11/z psi in 24 hours. ALL PIPING HYDROSTATICALLY TESTED AT 200 PSI FOR 2 HOURS IF NO, STATE REASON DRY PIPING PNEUMATICALLY TESTED Li YES Li NO EQUIPMENT OPERATES PROPERLY R YES Li NO DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT ADDITIVES AND CORROSIVE CHEMICALS, SODIUM SILICATE OR DERIVATIVES OF SODIUM SILICATE, BRINE, OR OTHER CORROSIVE CHEMICALS WERE NOT USED FOR TESTING SYSTEMS OR STOPPING LEAKS? M YES Li NO DRAIN READING OF GAGE LOCATED NEAR WATER RESIDUAL PRESSURE WITH VALVE INT&T TESTS TEST SUPPLY TEST CONNECTION O PSI CONNECTION OPEN WIDE b> PSI UNDERGROUND MAINS AND LEAD-IN CONNECTIONS TO SYSTEM RISERS FLUSHED BEFORE CONNECTION MADE TO SPRINKLER PIPING. VERIFIED BY COPY OF THE U FORM NO. 858 0 YES Li NO OTHER EXPLAIN FLUSHED BY INSTALLER OF UNDERGROUND SPRINKER PIPING fl YES LiNO IF POWDER DRIVEN FASTENERS ARE USED IN CONCRETE IF NO, EXPLAIN HAS REPRESENTATIVE SAMPLE TESTING BEEN COMPLETED? Li YES Li NO BLANK TEST NUMBER USED LOCATIONS NUMBER REMOVED GASKETS WELDED PIPING YES Li NO IF YES... DO YOU CERTIFY AS THE SPRINKLER CONTRACTOR THAT WELDING PROCEDURES COMPLY WITH THE REQUIREMENTS OF AT LEAST AWS D10.9. LEVEL AR 3? Z YES Li NO DO YOU CERTIFY THAT THE WELDING WAS PERFORMED BY WELDERS QUALIFIED IN COMPLIANCE WELDING WITH THE REQUIREMENTS OF AT LEAST AWS D1 0.9. LEVEL AR 3? 0 YES []NO DO YOU CERTIFY THAT WELDING WAS CARRIED OUT IN COMPLIANCE WITH A DOCUMENTED QUALITY CONTROL PROCEDURE TO INSURE THAT ALL DISCS ARE RETRIEVED, THAT OPENINGS IN PIPING ARE SMOOTH, THAT SLAG AND OTHER WELDING RESIDUE ARE REMOVED, AND THAT THE INTERNAL DIAMETERS OF PIPING ARE NOT PENETRATED? M YES Li NO CUTOUTS DO YOU CERTIFY THAT YOU HAVE A CONTROL FEATURE TO ENSURE THAT ALL CUTOUTS (DISCS) (DISCS) ARE RETRIEVED? D YES Li NO HYDRAULIC NAMEPLATE PROVIDED IF NO, EXPLAIN DATA EYES ONO NAMEPLATE DATE LEFT IN4ERVICE WITH ALL CONTROL VALVES OPEN. 13 - REMARKS /1 NAME OF VRINKER CONTRACTOR: InnovativjFire Protection, Inc. SIGNATURES I - TESTS WITNESSED BY - FOR PPERTYESIGNED1 TITLE DATE FOR/PR R CONTRACTOR D) TITL. DATE ADDITIONAL EXPL7S AND UNDERGROUND PIPING 24-17 Contractor's Material and Test Certificate for Underground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the contractor's representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job, A certificate shall be filled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faultymaterial, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. Property name C - Property address 19 3e â4 zmw44 D L-iJ Accepted by approving authorities (names) ----.----....------. - -.--' -.---- ........ P ' Plans ---.--... .... Installation conforms to accepted plans 1'. Yes U No Equipment used is approved 9LYes U No It no, state deviations Has person in charge of tire equipment been instructed as to location of Ja Yes U No control valves and care and maintenance of this new equipment? If no, explain Instructions Have copies of appropriate instructions and care and maintenance Yes Q No charts been left on premises? . .. If no, explain Location Supplies buildings Pipe types and class Type joint .............../&-.z Pipe conforms to .t.4L)44._. standard Yes U No Underground ' Fittings conform to standard' , j Yes [j No pipes and Joints If no, explain Joints needing anc ra e cia ped, strapped, or blocked in - Yes U No accordance with .. - - -- ---------standard It no, explain 2, shi' Flow the required rate until water is clear as indicated by no collection of foreign material in burlap bags at outlets such as -'' hy rants and blow-ohs. Flush at flows not less than 390 gpm (1476 Llmin) for 4 in. pipe, 880 gpm (3331 Llmin) for 6 in. pipe, 1560 gpm (5905 LJmin) for 8 in. pipe, 2440 gpm (9235 Llmin) for 10 in. pipe, and 3520 gpm (13,323 Limin) for 12 in. pipe. When supply cannot 7, /- puca.zIpulated flow rates, obtain maximum available. rostati . All piping and attached appurtenances subjected to system working pressure shall be hydrostatically tested at 200 psi Test (13. ar or 50 pal (3.4 bar) in excess of the system working pressure, whichever is greater, and shall maintain that pressure ± 5 psi description for 2 hours. Hydrosta tic Testing Allowance: Where additional water is added to the system to maintain the test pressures required by 10.10.2.2.1, the amount of water shall be measured and shall not exceed the limits of the following equation (For metric equation, see 10,10.2.2.4): L = testing allowance (makeup water), in gallons per hour SDJ L .. S = length of pipe tested, in feet 148,000 D = nominal diameter of the pipe, in inches P = average test pressure during the hydrostatic test, in pounds per square inch (gauge) New underground piping flushed according to s—Yes U No standard by (company) If no, explain ----.-----.-.---- How flushing flow was obtained Through what type opening Flushing ,Public water U Tank or reservoir U Fire pump U Hydrant butt Open pipe tests Lead-ins flushed according to tP.i_/i±t.. standard by (company) J4Yes U No If no, explain How flushing flow was obtained Through what type opening -- Public water J Tank or reservoir U Fire pump [ij Y connection to flange 43 Open pipe and spigot © 2007 National Fire Protection Association NFPA 24 (p. 1 of 2) FIGURE 10.10.1 Sample of Contractor's Material and Test Certificate for Underground Piping. 2007 Edition 24-18 INSTALLATION OF PRIVATE FIRE SERVICE MAINS AND THEIR APPURTENANCES At new underground piping hydrostatically tested at Joints covered Hydrostatic test psi for ____________ hours Yes Li No Total amount of leakage measured Leakage ____ gallons 2.. hours test Allowable leakage ----T gallons ____________ hous * Number installed Type and make All operate satisfactorily Hydrants z&c Yes Li No Water control valves left wide open @ Yes Li No If no, state reason -. Control valves Hose threads of fire department connections and hydrants interchangeable with '5 Li No those of fire department answering alarm Date left in service Remarks Name of installing contractor rm Tests witnessed by Signatures For property owner (signed) Title Date For~in~s tor (signed) Title I F)eE l , ) . z. Additional © 2007 National Fire Protection Association NFPA 24 (p. 2 of 2) FIGURE 10.10.1 Continued 2007 Edition UNDERGROUND PIPING 24-17 Contractor's Material and Test Certificate for Underground Piping PROCEDURE Upon completion of work, inspection and tests shall be made by the contractors representative and witnessed by an owner's representative. All defects shall be corrected and system left in service before contractor's personnel finally leave the job. A certificate shall be tilled out and signed by both representatives. Copies shall be prepared for approving authorities, owners, and contractor. It is understood the owner's representative's signature in no way prejudices any claim against contractor for faulty -material, poor workmanship, or failure to comply with approving authority's requirements or local ordinances. Property name Property address g '-''- Accepted by approving authorities (names Address Ao K Plans .. Installation conforms to accepted plans j, Yes Q No Equipment used is approved Li No If no, state deviations Has person in charge of fire equipment been instructed as to location of Yes Li No control valves and care and maintenance of this new equipment? If no, explain Instructions Have copies of appropriate instructions and care and maintenance J_yes U No charts been left on premises? -. If no, explain Location Supplies buildings Pipe types and class Type joint Pipe conforms / to standard Yes U No Underground Fittings conform to At-eJi standard . L Yes EJ No pipes and joints If no, explain Joints needing anc ra e cIa ped, strapped, or blocked in E- Yes EJ No accordance with . - . standard If no, explain ju hT. Flow the required rate until water is clear as indicated by no collection of foreign material in burlap bags at outlets such as —-I -iits and blow-offs. Flush at flows not less than 390 gpm (1476 LJmin) for 4 in. pipe, 880 gpm (3331 Llmin) for 6 in. pipe, 1560 gpm (5905 Umin) for 8 in. pipe, 2440 gpm (9235 1./mm) for 10 in, pipe, and 3520 gpm (13,323 Umin) for 12 in. pipe. When supply cannot produce stipulated flow rates, obtain maximum available. Os All piping and attached appurtenances subjected to system working pressure shall be hydrostatically tested at 200 psi . or 50 psi (3.4 bar) in excess of the system working pressure, whichever is greater, and shall maintain that pressure ± 5 psi Test description for 2 hours. Hydrostatic Testing Allowanc : Where additional water is added to the system to maintain the test pressures required by 10.10.2.2.1, the amount of water shall be measured and shall not exceed the limits of the following equation (For metric equation, see 10.10.2.2.4): L = testing allowance (makeup water), in gallons per hour SD-TP L = S = length of pipe tested, in feet 148,000 D = nominal diameter of the pipe, in inches P = average test pressure during the hydrostatic test, in pounds per square inch (gauge) New underground piping flushed according to Yes Li No standard by (company) If no, explain How flushing flow was obtained Through what type opening Flushing Public water U Tank or reservoir Li Fire pump U Hydrant butt Open pipe tests Lead-ins flushed according to I%LP L.JS/i.I standard by (company) Yes [J No If no, explain How flushing flow was obtained Through what type opening Public water [J Tank or reservoir U Fire pump EU Y connection to flange 44 Open pipe and Spigot © 2007 National Fire Protection Association NFPA 24 (p. 1 of 2) FIGURE 10.10.1 Sample of Contractor's Material and Test Certificate for Underground Piping. 2007 Edition 24—I8 INSTALLATION OF PRIVATE FIRE SERVICE MAINS AN!) THEIRAPI'URTENANCES Hydrostatic All new underground piping hydrostatically tested at - Joints covered test psi for -. hours Yes U No Total amount of leakage measured Leakage _gallons 2- hours -- test Allowable leakage gallons 2 hoUrs - Number installed Type and make All operate satisfactorily Hydrants 3 . Yes EJ No Water control Valves left wide open Yes Li No It no, state reason Control valves Hose threads of tire department connections and hydrants interchangeable with SLYes Li No those of fire department answering alarm Date left in service Remarks - Name of installing contractor Tests witnessed by Signatures For property owner (signed) Title Date For s tor (signed) Title .-, - / 2..i - .- Additional © 2007 National Fire Protection Association NFPA 24 (p. 2 of 2) FIGURE 10.10.1 Continued 2007 Edition Greaory Ryan From: Greg Jones <greg©cityventures.com> Sent: Tuesday, May 01, 2012 3:35 PM To: Gregory Ryan Cc: Greg Jones Subject: RE: La Costa Village Townhomes - Underground Plans. / Please see me responses below. Thanks, greg@cityventures.com City Vent u r e s VM\CJ5%-kt 0W' A-1 ci VehAro SckLA A&k From: Gregory Ryan [ma ilto: Gregory. Ryan©carlsbadca.gov] Sent: Tuesday, May 01, 2012 6:49 AM To: Greg Jones Subject: La Costa Village Townhomes - Underground Plans. Greg— I need the following information in order to process a permit for the Underground water-main plans for the fire sprinkler systems at your La Costa Village Townhomes project. Name of Contractor City Ventures Homebuilding LLC Contractor's License Number 941507 B City Business License 1233636 Address of Project - (just need one physical address to attach the permit to) 1841 Cliff Swallow Lane GREGORY L RYAN Deputy Fire Marshal Carlsbad Fire Department 1635 Faraday Avenue Carlsbad CA 92008 760.602.4663 Gregory. Ryancarlsbadca.gov 1