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HomeMy WebLinkAboutHydraulic Calculations Dry - FIR Inspections - 6/19/2017 HYDRAULIC CALCULATION SUMMARY SHEET *** ALTA FOREST PRODUCTS- SHELTON MILL UPGRADES *** PROJECT NAME:--> ALTA FOREST PRODUCTS- UPGRADES JOB NUMBER: WLC-7088 PROJECT ADDRESS:--> 780 W. State Rte. 108, Shelton WAshington 98584 DRAWING SHEET NUMBER:--> FP1.0 2.0 DATE CALCULATED:—> 6/19/2017 AUTHORITY HAVING JURISDICTION:--> PRIVATE INSURANCE PROVIDER ill Size Of System:----------------------------> 5,680 +\- SQ Ft * SCOPE OF WORK Type Of System:----------------------------> DRY Vol. Of Dry/Preaction/Anti-freeze System:--> 1,117.42 gal/ UPPER LVL Available Pressure-------------------------> 93.00 psi Required Pressure--------------------------> 76.2 psi Safety Factor------------------------------> 16.80 psi / 18.06% DESIGN DATA: Remote Area Number:------------------------> 1 Remote Area Location:--------------- > OVERHEAD SYSTEM NW BLDG. Occupancy Classification:------------------> EXTRA HAZARD Storage Commodity Classification:----------> N/A Storage Height:----------------------------> N/A Density:-----------------------------------> .30 GPM/SQ FT Area Of Application:-----------------------> 2,550 SQ FT Coverage Per Sprinkler:--------------------> 100 SQ FT CALCULATED Type Of Sprinkler Calculated:--------------> SR- SSU Sprinkler K-Factor:----------------- -----> 8.0K Number Of Sprinklers Calculated:-----------> 30 In-Rack Sprinkler Demand:------------------> N/A Number Of In-Rack Sprinklers Calculated:---> N/A Hose Streams Inside + Outside:-------------> 500 GPM Total Water Required (including hose) :-----> 1507.2 Flow And Pressure At Base Of Riser:--------> 1,007.20 gpm 65.00 psi WATER SUPPLY: Static psi:---> 115 Residual psi:--> 97 Flowing GPM:-- GPM-9-2 psi:-=S N/A=SEE-PUMP--CURVE A"-_ Test Date:----> 1.04.2007 Location:-----> HYD. ADJACENT- NORTHEAST OF EXITNG RISER ROOM Info From:----> VIKING AUTOMATIC SPRINKLER ONSITE FLOW TEST PUMP INFO: Pump Type:--> EXISTING PSI Rating:--> 75 GPM Rating:--> 1,500 INSTALLING CONTRACTOR: Name:---------> Viking Automatic Sprinkler Co. Address:------> 602 CALIFORNIA WAY SUITE 1 LONGVIEW WASHINGTON 98632 Phone:--------> 360.425.7620 Fax:--> 360.425.9025 Designer:-----> PAUL NIPPER WASHINGTON LIC#:--> VI-KI-NA-S373NT Portland Metro Lic.#:--> 28116 Calculations performed by HASS 8.6 under license # 38030713 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 6/20/20170X\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SRC 115.0 97.0 1353.8 93.0 1507.2 76.2 Required pressure is 16.9 psi (18%) less than available pressure. AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1507.2 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 0.0 GPM OTHER HOSE STREAM ALLOWANCES 500.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 1007.2 GPM NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 101 21.7 K= 8.00 14 .1 30.0 102 21.0 K= 8.00 14.5 30.4 103 20.3 K= 8.00 15.2 31.2 104 19.7 K= 8.00 16.4 32.4 105 21.7 K= 6.00 14.1 30.1 106 21.0 K= 8.00 14.5 30.5 107 20.3 K= 8.00 15.2 31.2 108 19.7 K= 8.00 16.4 32.4 109 21.7 K= 6.00 14.3 30.2 110 21.0 K= 8.00 14.7 30.7 - 1Z 20.3-_." _ b.UU l - r.�---- 112 19.7 K= 8.00 16.6 32.6 113 21.7 K= 6.00 14.7 30.6 114 21.0 K= 8.00 15.1 31.1 115 20.3 K= 8.00 15.8 31.8 116 19.7 K= 6.00 17.0 33.0 117 21.3 K= 8.00 17.6 33.5 117A 20.2 - - - - 20.3 - - - 118 20.2 K= 8.00 19.1 34.9 118A 19.0 - - - - 22.0 - - - 119 21.3 K= 5.00 21.4 37.0 120 20.2 K= 8.00 22.3 37.6 121 21.3 K= 8.00 22.3 37.8 122 20.2 K= 8.00 23.1 38.4 123 21.3 K= 8.00 23.6 38.8 124 20.2 K= 8.00 24.3 39.5 125 23.0 K= 8.00 17.8 33.8 126 23.0 K= 8.00 18.0 33.9 127 23.0 K= 8.00 18.3 34.3 128 23.0 K= 8.00 19.3 35.2 129 23.0 K= 6.00 20.8 36.5 130 22.2 K= 8.00 20.7 36.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit NODE ANALYSIS DATA NODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE (FT) (PSI) (GPM) 125A 22.3 - - - - 21.1 - - - 126A 22.3 - - - - 21.2 - - - 127A 22.3 - - - - 21.7 - - - 128A 22.3 - - - - 22.8 - - - 129A 22.3 - - - - 24.5 - - - 130A 19.8 - - - - 23.0 - - - 1A 19.7 - - - - 16.5 - - - 2A 19.7 - - - - 16.5 - - - 3A 19.7 - - - - 16.7 - - - 4A 19.7 - - - - 17.1 - - - 6A 20.1 - - - - 22.2 - - - 7A 20.1 - - - - 23.2 - - - 8A 20.1 - - - - 24.4 - - - 12A 22.3 - - - - 24.7 - - - A1 18.5 - - - - 18.5 - - - A2 18.5 - - - - 18.6 - - - A3 18.5 - - - - 18.8 - - - A4 18.5 - - - - 19.3 - - - A5 18.9 - - - - 22.1 - - - A6 18.9 - - - - 23.3 - - - A7 18.9 - - - 24.3 - - - A8 18.9 - - - - 25.6 - - - A9 19.8 - - - 25.4 - - - A10 19.8 - - - - 26.9 - - - All 19.8 - - - - 27.9 - - - Al2 19.9 - - - - 29.0 - - - A13 19.8 - - - - 36.2 - - - A14 21.0 - - - - 42.3 - - - A15 20.9 - - - - 43.9 - - - A16 20.8 - - - - 45.2 - - - -- -. _ ...........Al/ -- -- ���-_............_.- - - - fir........._. - - - A18 20.6 - - - - 46.6 - - - A19 20.0 - - - - 47.1 - - - A20 19.0 - - - - 51.5 - - A21 18.7 - - - - 52.1 - - - A22 13.2 - - - - 55.8 - - - A23 10.0 - - - - 57.6 - - - TOR 6.8 - - - - 60.7 - - - BOR 1.7 - - - - 65.0 - - - UG1 0.5 - - - - 67.1 - - - UG2 -4.0 - - - - 69.8 - - - UG3 -4.0 HOSE STREAM 74.9 500.0 SRC -4.0 SOURCE 76.2 1507.2 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 6/20/20170X\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit 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 -30.0 2.157 PL 10.00 PF 0.1 101 21.7 8.0 14 .1 30.0 2.6 100 FTG ---- PE 0.3 102 21.0 8.0 14.5 30.4 0.012 TL 10.00 PV Pipe: 2 -60.4 2.157 PL 10.00 PF 0.4 102 21.0 8.0 14.5 30.4 5.3 100 FTG ---- PE 0.3 103 20.3 8.0 15.2 31.2 0.042 TL 10.00 PV Pipe: 3 -91.6 2.157 PL 10.00 PF 0.9 103 20.3 8.0 15.2 31.2 8.0 100 FTG ---- PE 0.3 104 19.7 8.0 16.4 32.4 0.091 TL 10.00 PV Pipe: 4 -124.0 2.157 PL 0.56 PF 0.1 104 19.7 8.0 16.4 32.4 10.9 100 FTG ---- PE 0.0 lA 19.7 0.0 16.5 0.0 0.159 TL 0.56 PV Pipe: 5 -30.1 2.157 PL 10.00 PF 0.1 105 21.7 8.0 14.1 30.1 2.6 100 FTG ---- PE 0.3 106 21.0 8.0 14.5 30.5 0.012 TL 10.00 PV Pipe: 6 -60.5 2.157 PL 10.00 PF 0.4 106 21.0 8.0 14.5 30.5 5.3 100 FTG ---- PE 0.3 107 20.3 8.0 15.2 31.2 0.042 TL 10.00 PV Pipe: 7 -91.8 2.157 PL 10.00 PF 0.9 107 20.3 8.0 15.2 31.2 8.1 100 FTG ---- PE 0.3 108 19.7 8.0 16.4 32.4 0.091 TL 10.00 PV _ -- 8.._.. _............_.... ---- .........__.._-._.-1.2.4.._2 2:157_.-Pl;- ......._.0_:5-67___PF._. 108 19.7 8.0 16.4 32.4 10.9 100 FTG ---- PE 0.0 2A 19.7 0.0 16.5 0.0 0.160 TL 0.56 PV Pipe: 9 -30.2 2.157 PL 10.00 PF 0.1 109 21.7 8.0 14.3 30.2 2.7 100 FTG ---- PE 0.3 110 21.0 8.0 14.7 30.7 0.012 TL 10.00 PV Pipe: 10 -60.9 2.157 PL 10.00 PF 0.4 110 21.0 8.0 14 .7 30.7 5.3 100 FTG ---- PE 0.3 ill 20.3 8.0 15.4 31.4 0.043 TL 10.00 PV Pipe: 11 -92.3 2.157 PL 10.00 PF 0.9 ill 20.3 8.0 15.4 31.4 8.1 100 FTG ---- PE 0.3 112 19.7 8.0 16.6 32.6 0.092 TL 10.00 PV Pipe: 12 -124.9 2.157 PL 0.56 PF 0.1 112 19.7 8.0 16.6 32.6 11.0 100 FTG ---- PE 0.0 3A 19.7 0.0 16.7 0.0 0.161 TL 0.56 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 6/20/20170X\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit 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 -30.6 2.157 PL 10.00 PF 0.1 113 21.7 8.0 14.7 30.6 2.7 100 FTG ---- PE 0.3 114 21.0 8.0 15.1 31.1 0.012 TL 10.00 PV Pipe: 14 -61.7 2.157 PL 10.00 PF 0.4 114 21.0 8.0 15.1 31.1 5.4 100 FTG ---- PE 0.3 115 20.3 8.0 15.8 31.8 0.044 TL 10.00 PV Pipe: 15 -93.5 2.157 PL 10.00 PF 0.9 115 20.3 8.0 15.8 31.8 8.2 100 FTG ---- PE 0.3 116 19.7 8.0 17.0 33.0 0.094 TL 10.00 PV Pipe: 16 -126.5 2.157 PL 0.56 PF 0.1 116 19.7 8.0 17.0 33.0 11.1 100 FTG ---- PE 0.0 4A 19.7 0.0 17.1 0.0 0.165 TL 0.56 PV Pipe: 17 -33.5 1.049 PL 1.11 PF 2.2 117 21.3 8.0 17.6 33.5 12.4 100 FTG T PE 0.5 117A 20.2 0.0 20.3 0.0 0.474 TL 4.68 PV Pipe: 18 -34. 9 1.049 PL 1.17 PF 2.4 118 20.2 8.0 19.1 34.9 13. 0 100 FTG T PE 0.5 118A 19.0 0.0 22.0 0.0 0.511 TL 4.74 PV Pipe: 19 -37.0 2.157 PL 14.00 PF 0.2 119 21.3 8.0 21.4 37.0 3.2 100 FTG ---- PE 0.5 120 20.2 8.0 22.1 37.6 0.017 TL 14.00 PV Pipe: 20 -74.7 2.157 PL 0.73 PF 0.0 120 20.2 8.0 22.1 37.6 6.6 100 FTG - --_PE 0.0 20_:.�_�_.....0....----��-------.....0- ..0 .062 TL 0.73 PV Pipe: 21 -37.8 2.157 PL 14.00 PF 0.2 121 21.3 8.0 22.3 37.8 3.3 100 FTG ---- PE 0.5 122 20.2 8.0 23.1 38.4 0.018 TL 14.00 PV Pipe: 22 -76.3 2.157 PL 0.73 PF 0.0 122 20.2 8.0 23.1 38.4 6.7 100 FTG ---- PE 0.0 7A 20.1 0.0 23.2 0.0 0.065 TL 0.73 PV Pipe: 23 -38.8 2.157 PL 14.00 PF 0.3 123 21.3 8.0 23.6 38.8 3.4 100 FTG ---- PE 0.5 124 20.2 8.0 24.3 39.5 0.019 TL 14.00 PV Pipe: 24 -78.3 2.157 PL 0.73 PF 0.0 124 20.2 8.0 24.3 39.5 6.9 100 FTG ---- PE 0.0 8A 20.1 0.0 24.4 0.0 0.068 TL 0.7.3 PV Pipe: 25 -33. 8 1.049 PL 1.17 PF 3.0 125 23.0 8.0 17.8 33.8 12.5 100 FTG ET PE 0.3 125A 22.3 0.0 21.1 0.0 0.481 TL 6.17 PV i SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit FIPE 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 -33.9 1.049 PL 1 .17 PF 3.0 126 23.0 8.0 18.0 33.9 12.6 100 FTG ET PE 0.3 126A 22.3 0.0 21.2 0.0 0.484 TL 6.17 PV Pipe: 27 -34.3 1.049 PL 1.17 PF 3.0 127 23.0 8.0 18.3 34.3 12.7 100 FTG ET PE 0.3 127A 22.3 0.0 21.7 0.0 0.494 TL 6.17 PV Pipe: 28 -35.2 1.049 PL 1 .17 PF 3.2 128 23.0 8.0 19.3 35.2 13.0 100 FTG ET PE 0.3 128A 22.3 0.0 22.8 0.0 0.517 TL 6.17 PV Pipe: 29 -36.5 1.049 PL 1.17 PF 3.4 129 23.0 8.0 20.8 36.5 13.5 100 FTG ET PE 0.3 129A 22.3 0.0 24.5 0.0 0.554 TL 6.17 PV Pipe: 30 -33.8 2.157 PL 10.00 PF 0.1 125A 22.3 0.0 21.1 0.0 3.0 100 FTG ---- PE 0.0 126A 22.3 0.0 21.2 0.0 0.014 TL 10.00 PV Pipe: 31 -67.7 2.157 PL 8.42 PF 0.4 126A 22.3 0.0 21.2 0.0 5. 9 100 FTG ---- PE 0.0 127A 22.3 0.0 21.7 0.0 0.052 TL 8.42 PV Pipe: 32 -102.0 2.157 PL 10.00 PF 1.1 127A 22.3 0.0 21.7 0.0 9.0 100 FTG ---- PE 0.0 128A 22.3 0.0 22.8 0.0 0.111 TL 10.00 PV Pipe: 33 -137.1 2.157 PL 8.77 PF 1.7 128A 22.3 0.0 22.8 0.0 12.0 100 FTG ---- PE 0.0 129A 3---0� 4. 0.192 TL PV .. -. _ Pipe: 34 -173.6 2.157 PL 0.73 PF 0.2 129A 22.3 0.0 24.5 0.0 15.2 100 FTG ---- PE 0.0 12A 22.3 0.0 24.7 0.0 0.297 TL 0.73 PV Pipe: 35 -36.4 1.049 PL 2.34 PF 1.3 130 22.2 8.0 20.7 36.4 13.5 100 FTG ---- PE 1.0 130A 19.8 0.0 23.0 0.0 0.552 TL 2.34 PV Pipe: 36 -36.4 1.049 PL 3.83 PF 4.9 130A 19.8 0.0 23.0 0.0 13.5 100 FTG ET PE 0.0 All 19.8 0.0 27.9 0.0 0.552 TL 8.83 PV Pipe: 37 -124.0 2.157 PL 1.33 PF 1.6 1A 19.7 0.0 16.5 0.0 10.9 100 FTG ET PE 0.5 Al 16.5 0.0 18.5 0.0 0.159 TL 9.89 PV Pipe: 38 -124.2 2.157 PL 1.33 PF 1. 6 2A 19.7 0.0 16.5 0.0 10. 9 100 FTG ET PE 0.5 A2 18.5 0.0 18.6 0.0 0.160 TL 9.89 PV SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 7 DATE: 6/20/20170X\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit 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 -124 .9 2.157 PL 1.33 PF 1.6 3A 19.7 0.0 16.7 0.0 11.0 100 FTG ET PE 0.5 A3 18.5 0.0 18.8 0.0 0.161 TL 9.89 PV Pipe: 40 -126.5 2.157 PL 1.33 PF 1.6 4A 19.7 0.0 17.1 0.0 11.1 100 FTG ET PE 0.5 A4 18.5 0.0 19.3 0.0 0.165 TL 9.89 PV Pipe: 41 -74.7 2.157 PL 1.16 PF 0.6 6A 20.1 0.0 22.2 0.0 6.6 100 FTG ET PE 0.5 A6 18.9 0.0 23.3 0.0 0.062 TL 9.72 PV Pipe: 42 -76.3 2.157 PL 1.16 PF 0.6 7A 20.1 0.0 23.2 0.0 6.7 100 FTG ET , PE 0.5 A7 18.9 0.0 24.3 0.0 0.065 TL 9.72 PV Pipe: 43 -78.3 2.157 PL 1.16 PF 0.7 8A 20.1 0.0 24.4 0.0 6.9 100 FTG ET PE 0.5 A8 18.9 0.0 25.6 0.0 0.068 TL 9.72 PV Pipe: 44 -173.6 2.157 PL 2.46 PF 3.3 12A 22.3 0.0 24.7 0.0 15.2 100 FTG ET PE 1.0 Al2 19.9 0.0 29.0 0.0 0.297 TL 11.02 PV Pipe: 45 -124.0 4.260 PL 10.00 PF 0.1 Al 18.5 0.0 18.5 0.0 2.8 100 FTG ---- PE 0.0 A2 18.5 0.0 18.6 0.0 0.006 TL 10.00 PV Pipe: 46 -248.1 4.260 PL 10.00 PF 0.2 A2 18.5 0.0 18.6 0.0 5.6 100 FTG ---- PE 0.0 0=0.__1.8_g_._-.0 0.021 1 070.0-..pV- - Pipe: 48 -373.1 4.260 PL 10.00 PF 0.4 A3 18.5 0.0 18.8 0.0 8.4 100 FTG ---- PE 0.0 A4 18.5 0.0 19.3 0.0 0.044 TL 10.00 PV Pipe: 49 -499.5 4.260 PL 13.21 PF 1.7 A4 18.5 0.0 19.3 0.0 11.2 100 FTG 2E PE -0.7 117A 20.2 0.0 20.3 0.0 0.076 TL 22.92 PV Pipe: 50 -533.1 4.260 PL 14.00 PF 1.2 117A 20.2 0.0 20.3 0.0 12.0 100 FTG ---- PE 0.5 118A 19.0 0.0 22.0 0.0 0.086 TL 14.00 PV Pipe: 51 -568.0 4.260 PL 0.73 PF 0.1 118A 19.0 0.0 22.0 0.0 12.8 100 FTG ---- PE 0.0 A5 18.9 0.0 22.1 0.0 0.097 TL 0.73 PV Pipe: 52 -568.0 4.260 PL 8.00 PF 1.2 A5 18.9 0.0 22.1 0.0 12.8 100 FTG E PE 0.0 A6 18. 9 0.0 23.3 0.0 0.097 TL 12.85 PV i SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 8 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit 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: 53 -642.7 4.260 PL 8.00 PF 1.0 A6 18.9 0.0 23.3 0.0 14.5 100 FTG ---- PE 0.0 A7 18.9 0.0 24.3 0.0 0.122 TL 8.00 PV Pipe: 54 -718.9 4.260 PL 8.46 PF 1.3 A7 16.9 0.0 24.3 0.0 16.2 100 FTG ---- PE 0.0 A8 18.9 0.0 25.6 0.0 0.150 TL 8.46 PV Pipe: 55 -797.2 4.260 PL 1.17 PF 0.2 AS 18.9 0.0 25.6 0.0 17.9 100 FTG ---- PE -0.4 A9 19.8 0.0 25.4 0.0 0.181 TL 1.17 PV Pipe: 56 -797.2 4.260 PL 3.25 PF 1.5 A9 19.8 0.0 25.4 0.0 17.9 100 FTG E PE 0.0 A10 19.8 0.0 26.9 0.0 0.181 TL 8.10 PV Pipe: 57 -797.2 4.260 PL 0.83 PF 1.0 A10 19.8 0.0 26.9 0.0 17. 9 100 FTG E PE 0.0 All 19.8 0.0 27.9 0.0 0.181 TL 5.68 PV Pipe: 58 -833. 6 4.260 PL 5.75 PF 1.1 All 19.8 0.0 27.9 0.0 18.8 100 FTG ---- PE 0.0 Al2 19.9 0.0 29.0 0.0 0.197 TL 5.75 PV Pipe: 59 -1007.2 4.260 PL 25.67 PF 7.2 Al2 19.9 0.0 29.0 0.0 22.7 100 FTG ---- PE 0.1 A13 19.8 0.0 36.2 0.0 0.279 TL 25.67 PV Pipe: 60 -1007.2 4.260 PL 5.17 PF 6.7 A13 19.8 0.0 36.2 0.0 22.7 100 FTG ETF PE -0.5 A14 -D....._92-.3 T.0 -___-_._.... 0.27�3-1'L_..23:87-_ PV Pipe: 61 -1007.2 6.357 PL 31.83 PF 1.5 A14 21.0 0.0 42.3 0.0 10.2 100 FTG E PE 0.0 A15 20.9 0.0 43.9 0.0 0.040 TL 38.97 PV Pipe: 62 1007.2 6.357 PL 31.17 PF 1.2 A15 20.9 0.0 43.9 0.0 10.2 100 FTG ---- PE 0.0 A16 20.6 0.0 45.2 0.0 0.040 TL 31.17 PV Pipe: 64 -1007.2 6.357 PL 20.52 PF 0.8 A16 20.8 0.0 45.2 0.0 10.2 100 FTG ---- PE 0.1 A17 20.6 0.0 46.1 0.0 0.040 TL 20.52 PV Pipe: 65 -1007.2 6.357 PL 4.23 PF 0.5 A17 20.6 0.0 46.1 0.0 10.2 100 FTG E PE 0.0 A18 20.6 0.0 46.6 0.0 0.040 TL 11.37 PV Pipe: 66 -1007.2 6.357 PL 1.00 PF 0.3 A18 20.6 0.0 46.6 0.0 10.2 100 FTG E PE 0.3 A19 20.0 0.0 47.1 0.0 0.040 TL 6.14 PV SPRINKLER SYSTEM HYDRAUL=C ANALYSIS Page 9 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit 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: 67 -1007.2 6.357 PL 83.71 PF 3.9 A19 20.0 0.0 47.1 0.0 10.2 100 FTG 2E PE 0.4 A20 19.0 0.0 51.5 0.0 0.040 TL 97.98 PV Pipe: 68 -1007.2 6.357 PL 5.42 PF 0.5 A20 19.0 0.0 51.5 0.0 10.2 100 FTG E PE 0.1 A21 18.7 0.0 52.1 0.0 0.040 TL 12.56 PV Pipe: 69 -1007.2 6.357 PL 18.54 PF 1.3 A21 18.7 0.0 52.1 0.0 10.2 100 FTG 2E PE 2.3 A22 13.2 0.0 55.8 0.0 0.040 TL 32.81 PV Pipe: 70 -1007.2 6.357 PL 3.25 PF 0.4 A22 13.2 0.0 55.8 0.0 10.2 100 FTG E PE 1.4 A23 10.0 0.0 57.6 0.0 0.040 TL 10.39 PV Pipe: 71 -1007.2 6.357 PL 22.13 PF 1.7 A23 10.0 0.0 57.6 0.0 10.2 100 FTG 3E PE 1.4 TOR 6.8 0.0 60.7 0.0 0.040 TL 43.54 PV Pipe: 72 -1007.2 6.357 PL 5.08 PF 2.1 TOR 6.8 0.0 60.7 0.0 10.2 100 FTG EBD PE 2.2 BOR 1.7 0.0 65.0 0.0 0.040 TL 52.18 PV Pipe: 73 -1007.2 6.357 PL 0.83 PF 1.6 BOR 1.7 0.0 65.0 0.0 10.2 120 FTG ETC PE 0.5 UG1 0.5 0.0 67.1 0.0 0.028 TL 55.83 PV Pipe: 74 -1007.2 8.390 PL 105.00 PF 0.8 UG1 0.5 0.0 67.1 0.0 5.8 140 FTG EF PE 1.9 - ..0...-....69...8..._._.....�-----p 00 --fig. ,V - - - Pipe: 75 -1007.2 5.890 PL 144.00 PF 5.1 UG2 -4.0 0.0 69.8 0.0 11.9 140 FTG 2F PE 0.0 UG3 -4.0 H.S. 74.9 500.0 0.031 TL 164.00 PV Pipe: 76 -1507.2 8.390 PL 15.00 PF 1.3 UG3 -4.0 H.S. 74.9 500.0 8.7 140 FTG 2TG PE 0.0 SRC -4.0 SRCE 76.2 (N/A) 0.012 TL 113.00 PV NOTES (HASS) : (1) Calculations were performed by the HASS 8.6 computer program in accordance with NFPA13 (2016) under license no. 3603071320 granted by HRS Systems, Inc. 208 Southside Square Petersburg, TN 37144 (931) 659-9760 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 10 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit (2) The system has been calculated to provide an average imbalance at each node of 0.001 gpm and a maximum imbalance at any node of 0.091 gpm. (3) Total pressure at each node is used in balancing the system. Maximum water velocity is 22.7 ft/sec at pipe 60. (4) Items listed in bold print on the cover sheet are automatically transferred from the calculation report. (5) PIPE FITTINGS TABLE Pipe Table Name: VIKINGFM.PIP PAGE: A MATERIAL: SCH40 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T F B G C A D U Ell Tee 45ell Bfyvlv Gatvlv Chkvlv Almvlv Dryvlv Udelug -------------------------------------------------------- V R Viccup Runtee 1.049 2.00 5.00 1.00 2.20 1.00 5.00 10.00 0.10 0.00 2.00 2.00 PAGE: B MATERIAL: SCH10 HWC: 120 Diameter Equivalent Fitting Lengths in Feet (in) E T F B G C A D U Ell Tee 45ell Bfyvlv Gatvlv Chkvlv Almvlv Dryvlv Udelug -------------------------------------------------------- V R Viccup Runtee 0 10.00 .10 L19. 00 2.00 2.00 4.260 6.80 16.00 3.40 12.00 2.00 13.00 13.00 5.90 35.00 2.00 2.00 6.357 10.00 25.00 5.00 8.00 3.00 20.00 20.00 48.00 33.00 2.00 2.00 PAGE: D MATERIAL: DUCTL HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T F G C Ell Tee 45Ell Gatvlv Chkvlv 5.890 16.00 40.00 10.00 3.00 11.00 8.390 22.00 47.00 12.00 4.00 14.00 o � W H WATER SUPPLY ANALYSIS th H 120.0 _T _ Static: 115.00 psi Resid: 97.00 psi Flow: 1353.8 gpm r 0)LEGEND tv E o I 1 Available pressure r y ry j 93.05 psi @ 1507.2 gpm ►- o r* w � 100.0 _ - 2 Required pressure 1 0 76.18 psi @ 1507.2 gpm to i A 1. % ►° rn U �/ rt �u G _ �' - z A. Source Supply Curve- - tsj E 80.0 _ A. System Demand Curve- N. > N 2 / En R r x K tj ti to E tQ rH s 000 S 60.0 _ i N_ z tr U I aid R I tHn E H tom+ Wz �-+ m c) n rt ( 40.0 o ff �z P rtC: rrn Jam, 20.0 B J .n 13 En C] 0.0 H ro au in W r� m N -14.7 400 600 800 1000 1200 1400 16�00 1800 2000 FLOW (GPM) shed Lines indicate extrapolated values fromTest Results i :e pressures are based on hose stream deduction at the source I I SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 12 DATE: 6/20/2017OX\PERMIT\ALTA SHELTON EXISTING MILL-UPGRADE REV4-TEST.SDF JOB TITLE: Alta- Shelton- Existing Building Retrofit WATER SUPPLY CURVE 120+ I 110+ \\\\ 100+ \\\\ * <-97.0 psi @ 1354 gpm i Flow Test Point I 0 90+ I i I P 80+ R I E I X S I S 70+ U I R I E I 60+ ( I P I S I 50+ I I i 40+ I I i 30+ I I 20+ LEGEND " I " I X = Required Water Supply " 76.18 psi @ 1507.2 gpm " 10+ " 0 = Available Water Supply " I 93.05 psi @ 1507.2 gpm " " 0- -+--------------+------T--------+------------------+------------ 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) -o HYDRANT -HYDRANT OIL HOUSE -VEHICLE WASH OFFICE ZA000 OF 2,200 8F -SPRINKLER VALVE C IM.ANERMILL -FIRE WALL { ZPRImm SF 00 SP S H7C?RNd?j TEST J) ,•"'" STAND SAWMILL i� 591l000 BF 4 , GALLON ME TANK -HO6! 6TAN 67 PrE V / m .. .000 GALLON DIESEL TANK - Boa-°• -- - ~'1--�-.--._._ WYQRAN P 26 00MG SF 1 ✓- O~ HOSE STAND HOSE _ PIPE STAND PIPE 1�raak LA y 30 Con vR „ 3D'G400t 9�0m SF •+----� �cLI[G 4• _� I�U}� _..._.......... Sas MAN LA l_ 1'1ORTIIf IC tp� a— «� w lux:t � - 400- ar �I Static city water pressure 13 psi Churn suction pressure 13 psi Churn discharge pressure 102 psi Was 300 GPM flow conducted? Yes 0 No ❑ Hose size: N/A inch Tip size: N/A uich Hose length: N/A ft Pitot reading: Flowmeter GPV1: 1500 Was pump run for 10 minutes flowing? Yes X No ❑ Were all fire pumps tested? Yes © No ❑ i Flow Chart NO.S SIZE PUAIP PRESSURE PITOT FLOP RPAI VOLTS AMPS COJLMENTS OF NOZZELS PRESSURE DISCllG. SUCT. I NET CIIURN 102 13 189 - - 1825 Floivmefer 82 10 72 1500 1820 Flowmeter 61 6 55 2250 1821 Problems found: Jockey pump running constantly-not holding pressure. Corrections made: Date corrections made: By: THIS IS TO CERTIFY THAT THE FIRE PUMP SYSTEM HAS BEEN PROPERLY TESTED AND.INSPECTED-FOR RELIABILITY In COVER THE ITEMS IISTED IN THIS REPORT; IS CONSISTANT WITH MANUFACTURER'S REQUIREMENTS; AND ALL CORRECTIONS ARE TO BE MADE BY OWNER. Signature of Tester: Agency: Capitol Pump R sources Phone: (36 9 M30