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FIR2025-0003+Calculations+1.7.2025_9.34.37_PM+4701098
INSTALLING CONTRACTOR STAMP: DESIGN ONLY STAMP: RECEIVED Jan 14 2025 CITY OF EDMONDS DEVELOPMENT SERVICES DEPARTMENT WASHINGTON STATE ■ Euplr�s ■ GEC 31� 2S CERTIFICATE OF COMrETENCY ■ FIRE SPRINKLER SYSTEMS FIR2025-0003 ■ ■ Libby Marie Babb 3791-0722-A Level ■ A-Pex Design Services, Inc. • i APEXDDS782K5 i � ■ SISIIE1lSIr atS � A-PEX Design Services Inc. sales@a-pexdesignservices.com 11112 47th Avenue West Mukilteo, WA 98275 425-493-9680 Job Name RYNER RAMAN - One Head Calculation (H.27) Drawing RESIDENTIAL Location 1050 WALNUT ST EDMONDS WA 98020 Remote Area 1 Contract 241231-01 Data File 241231-01 Ryner Raman 1050 Walnut St.wx1 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 A-PEX Design Services Inc. RYNER RAMAN - One Head Calculation (H.27) HYDRAULIC DESIGN INFORMATION SHEET Name - RYNER RAMAN Location - EDMONDS WA 98020 Building - RESIDENTIAL Contractor - NEW WAY ENERGY Calculated By - LIBBY BABB Construction: (X) Combustible ( ) OCCUPANCY - RESIDENTIAL Page 1 Date 12/31 /2024 Date - 12-31-2024 System No. - 1 Contract No. - 241231-01 Drawing No. - Non -Combustible Ceiling Height S Type of Calculation: ( )NFPA 13 Residential ( )NFPA 13R (X)NFPA 13D Y Number of Sprinklers Flowing: (X)1 ( )2 ( )4 ( ) S ( ) Other T ( )Specific Ruling Made by Date E M Listed Flow at Start Point - 17 Gpm System Type Listed Pres. at Start Point - 12 Psi (X) Wet ( ) Dry D MAXIMUM LISTED SPACING 18 x 18 ( ) Deluge ( ) PreAction E Domestic Flow Added - 0 Gpm Sprinkler or Nozzle S Additional Flow Added - Gpm Make LF SENJU SPRINKLER Model RC-RES I Elevation at Highest Outlet - 116 Feet Size 7/16 K-Factor 4.9 G Note: Temperature Rating 155 N Calculation Gpm Required 17 Psi Required 37.44 At Ref Pt STR Summary C-Factor Used: Overhead 150 Underground 150 W Water Flow Test: Pump Data: A Date of Test - Rated Cap. T Time of Test - @ Psi E Static (Psi) - 55 Elev. R Residual (Psi) - 20 Other Flow (Gpm) - 500 S Elevation - 100 P Location: P L Source of Information: Y Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply Curve C A-PEX Design Services Inc. Page 2 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 City Water Supply: Demand: C1 - Static Pressure 55 D1 - Elevation 6.930 C2 - Residual Pressure: 20 D2 - System Flow : 16.974 C2 - Residual Flow 500 D2 - System Pressure 37.438 Hose ( Demand ) D3 - System Demand : 16.974 Safety Margin 17.495 150 140 130 P 120 R 110 E 100 S 90 S 80 U 70 R 60 E 50 40 30 20 10 D1 50 100 150 200 250 300 350 400 450 FLOW (N^1.85) C2 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Fittings Used Summary A-PEX Design Services Inc. Page 3 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 Fitting Legend Abbrev. Name E 90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 G Generic Gate Valve 1 1 1 1 1 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 T 90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Utb Aquapex Tee - Branch 2 17 14 9 12 17 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Utr Aquapex Tee - Run 1 2 2 4 2 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Units Summary Diameter Units Length Units Flow Units Pressure Units Inches Feet US Gallons per Minute Pounds per Square Inch Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - NFPA 2007 A-PEX Design Services Inc. RYNER RAMAN - One Head Calculation (H.27) Page 4 Date 12/31 /2024 SUPPLY ANALYSIS Node at Static Residual Available Source Pressure Pressure Flow Pressure Total Demand Required Pressure STIR 55.0 20 500.0 54.933 16.97 37.438 NODE ANALYSIS Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes H.27 116.0 4.9 12.0 16.97 H.30 116.0 13.14 H.24 116.0 13.64 T.45 116.0 13.96 T.46 116.0 14.24 T.40 108.0 18.32 H.10 108.0 18.73 T.35 108.0 18.81 T.36 108.0 19.05 S.1 104.0 21.15 MTR 100.0 28.53 STIR 100.0 37.44 H.31 116.0 13.1 H.25 116.0 13.52 H.22 116.0 13.89 T.41 116.0 14.26 T.44 108.0 18.21 T.43 108.0 18.28 T.42 108.0 18.29 H.15 108.0 18.36 H.1 108.0 18.48 H.2 108.0 18.56 H.3 108.0 18.63 T.34 108.0 18.71 H.5 108.0 18.78 H.6 108.0 18.92 H.21 116.0 14.34 H.19 116.0 14.46 T.39 116.0 14.52 H.13 116.0 14.64 H.18 116.0 14.72 T.38 116.0 14.85 H.12 116.0 14.96 T.37 116.0 15.23 H.14 116.0 14.33 H.11 116.0 14.42 HA 116.0 14.61 H.9 116.0 14.84 H.8 116.0 14.98 T.33 116.0 15.1 T.47 108.0 18.22 T.48 108.0 18.22 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - NFPA 2007 A-PEX Design Services Inc. RYNER RAMAN - One Head Calculation (H.27) NODE ANALYSIS (cont.) Page 5 Date 12/31 /2024 Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes T.49 108.0 18.23 H.28 108.0 18.24 H.29 108.0 18.26 H.32 108.0 18.27 H.26 108.0 18.29 H.16 108.0 18.31 H.17 108.0 18.32 H.23 108.0 18.22 H.20 108.0 18.28 H.7 116.0 15.14 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams - 2007 A-PEX Design Services Inc. Page 6 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf H.27 116 4.90 8.47 1 Utr 2.0 23.000 150 12.000 to 0.0 2.000 0.0 H.30 116 8.47 0.862 0.0 25.000 0.0457 1.143 Vel = 4.66 H.30 116 0.0 1 Utr 2.0 9.000 150 13.143 to 0.0 2.000 0.0 H.24 116 8.47 0.862 0.0 11.000 0.0456 0.502 Vel = 4.66 H.24 116 0.0 1 Utr 2.0 5.000 150 13.645 to 0.0 2.000 0.0 T.45 116 8.47 0.862 0.0 7.000 0.0457 0.320 Vel = 4.66 T.45 116 0.0 1 Utr 2.0 4.000 150 13.965 to 0.0 2.000 0.0 T.46 116 8.47 0.862 0.0 6.000 0.0458 0.275 Vel = 4.66 T.46 116 -3.99 1 2Utb 34.0 16.000 150 14.240 to 0.0 28.000 3.465 T.40 108 4.48 0.862 0.0 44.000 0.0141 0.619 Vel = 2.46 T.40 108 1.13 1 Utr 2.0 17.000 150 18.324 to 0.0 2.000 0.0 H.10 108 5.61 0.862 0.0 19.000 0.0213 0.405 Vel = 3.08 H.10 108 0.0 1 Utr 2.0 2.000 150 18.729 to 0.0 2.000 0.0 T.35 108 5.61 0.862 0.0 4.000 0.0213 0.085 Vel = 3.08 T.35 108 6.30 1.5 Utb 12.0 4.000 150 18.814 to 0.0 12.000 0.0 T.36 108 11.91 1.244 0.0 16.000 0.0144 0.231 Vel = 3.14 T.36 108 5.06 1.5 T 3.443 10.000 150 19.045 to 0.0 3.443 1.732 S.1 104 16.97 1.244 0.0 13.443 0.0277 0.373 Vel = 4.48 S.1 104 0.0 1.5 2E 3.443 92.000 150 21.150 to 0.0 3.443 4.732 * * Fixed Loss = 3 MTR 100 16.97 1.244 0.0 95.443 0.0277 2.645 Vel = 4.48 MTR 100 0.0 0.75 E 1.85 20.000 150 28.527 to T 3.7 6.475 0.0 STIR 100 16.97 0.745 G 0.925 26.475 0.3366 8.911 Vel = 12.49 0.0 STIR 16.97 37.438 K Factor = 2.77 H.27 116 8.51 1 Utr 2.0 22.000 150 12.000 to 0.0 2.000 0.0 H.31 116 8.51 0.862 0.0 24.000 0.0460 1.105 Vel = 4.68 H.31 116 0.0 1 0.0 9.000 150 13.105 to 0.0 0.0 0.0 H.25 116 8.51 0.862 0.0 9.000 0.0461 0.415 Vel = 4.68 H.25 116 0.0 1 Utr 2.0 6.000 150 13.520 to 0.0 2.000 0.0 H.22 116 8.51 0.862 0.0 8.000 0.0460 0.368 Vel = 4.68 H.22 116 0.0 1 Utr 2.0 6.000 150 13.888 to 0.0 2.000 0.0 T.41 116 8.51 0.862 0.0 8.000 0.0461 0.369 Vel = 4.68 T.41 116 -4.47 1 2Utb 34.0 14.000 150 14.257 to 0.0 28.000 3.465 T.44 108 4.04 0.862 0.0 42.000 0.0116 0.487 Vel = 2.22 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 7 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf T.44 108 -1.12 1 Utr 2.0 9.000 150 18.209 to 0.0 2.000 0.0 T.43 108 2.92 0.862 0.0 11.000 0.0064 0.070 Vel = 1.61 T.43 108 -0.28 1 0.0 2.000 150 18.279 to 0.0 0.0 0.0 T.42 108 2.64 0.862 0.0 2.000 0.0055 0.011 Vel = 1.45 T.42 108 0.28 1 Utr 2.0 9.000 150 18.290 to 0.0 2.000 0.0 H.15 108 2.92 0.862 0.0 11.000 0.0064 0.070 Vel = 1.61 H.15 108 0.0 1 Utr 2.0 17.000 150 18.360 to 0.0 2.000 0.0 H.1 108 2.92 0.862 0.0 19.000 0.0064 0.121 Vel = 1.61 H.1 108 0.0 1 Utr 2.0 10.000 150 18.481 to 0.0 2.000 0.0 H.2 108 2.92 0.862 0.0 12.000 0.0063 0.076 Vel = 1.61 H.2 108 0.0 1 Utr 2.0 10.000 150 18.557 to 0.0 2.000 0.0 H.3 108 2.92 0.862 0.0 12.000 0.0063 0.076 Vel = 1.61 H.3 108 0.0 1 Utr 2.0 10.000 150 18.633 to 0.0 2.000 0.0 T.34 108 2.92 0.862 0.0 12.000 0.0063 0.076 Vel = 1.61 T.34 108 2.14 1 Utr 2.0 2.000 150 18.709 to 0.0 2.000 0.0 H.5 108 5.06 0.862 0.0 4.000 0.0177 0.071 Vel = 2.78 H.5 108 0.0 1 Utr 2.0 6.000 150 18.780 to 0.0 2.000 0.0 H.6 108 5.06 0.862 0.0 8.000 0.0176 0.141 Vel = 2.78 H.6 108 0.0 1 Utr 2.0 5.000 150 18.921 to 0.0 2.000 0.0 T.36 108 5.06 0.862 0.0 7.000 0.0177 0.124 Vel = 2.78 0.0 T.36 5.06 19.045 K Factor = 1.16 T.46 116 3.98 1 0.0 9.000 150 14.240 to 0.0 0.0 0.0 H.21 116 3.98 0.862 0.0 9.000 0.0113 0.102 Vel = 2.19 H.21 116 0.0 1 Utr 2.0 8.000 150 14.342 to 0.0 2.000 0.0 H.19 116 3.98 0.862 0.0 10.000 0.0113 0.113 Vel = 2.19 H.19 116 0.0 1 Utr 2.0 4.000 150 14.455 to 0.0 2.000 0.0 T.39 116 3.98 0.862 0.0 6.000 0.0113 0.068 Vel = 2.19 T.39 116 0.0 1 Utr 2.0 8.000 150 14.523 to 0.0 2.000 0.0 H.13 116 3.98 0.862 0.0 10.000 0.0113 0.113 Vel = 2.19 H.13 116 0.0 1 0.0 7.000 150 14.636 to 0.0 0.0 0.0 H.18 116 3.98 0.862 0.0 7.000 0.0114 0.080 Vel = 2.19 H.18 116 0.0 1 Utr 2.0 10.000 150 14.716 to 0.0 2.000 0.0 T.38 116 3.98 0.862 0.0 12.000 0.0113 0.136 Vel = 2.19 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 8 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf T.38 116 0.0 1 Utr 2.0 8.000 150 14.852 to 0.0 2.000 0.0 H.12 116 3.98 0.862 0.0 10.000 0.0113 0.113 Vel = 2.19 H.12 116 0.0 1 Utb 17.0 7.000 150 14.965 to Utr 2.0 16.000 0.0 T.37 116 3.98 0.862 0.0 23.000 0.0113 0.261 Vel = 2.19 T.37 116 2.32 1.5 Utb 12.0 16.000 150 15.226 to 0.0 12.000 3.465 T.35 108 6.3 1.244 0.0 28.000 0.0044 0.123 Vel = 1.66 0.0 T.35 6.30 18.814 K Factor = 1.45 T.41 116 4.47 1 Utr 2.0 3.000 150 14.257 to 0.0 2.000 0.0 H.14 116 4.47 0.862 0.0 5.000 0.0140 0.070 Vel = 2.46 H.14 116 0.0 1 Utr 2.0 5.000 150 14.327 to 0.0 2.000 0.0 H.11 116 4.47 0.862 0.0 7.000 0.0140 0.098 Vel = 2.46 H.11 116 0.0 1 Utr 2.0 11.000 150 14.425 to 0.0 2.000 0.0 HA 116 4.47 0.862 0.0 13.000 0.0140 0.182 Vel = 2.46 HA 116 0.0 1 Utr 2.0 15.000 150 14.607 to 0.0 2.000 0.0 H.9 116 4.47 0.862 0.0 17.000 0.0140 0.238 Vel = 2.46 H.9 116 0.0 1 0.0 10.000 150 14.845 to 0.0 0.0 0.0 H.8 116 4.47 0.862 0.0 10.000 0.0140 0.140 Vel = 2.46 H.8 116 0.0 1 Utr 2.0 6.000 150 14.985 to 0.0 2.000 0.0 T.33 116 4.47 0.862 0.0 8.000 0.0139 0.111 Vel = 2.46 T.33 116 -2.32 1 2Utb 34.0 13.000 150 15.096 to 0.0 28.000 3.465 T.34 108 2.15 0.862 0.0 41.000 0.0036 0.148 Vel = 1.18 0.0 T.34 2.15 18.709 K Factor = 0.50 T.44 108 1.12 1 Utr 2.0 7.000 150 18.209 to 0.0 2.000 0.0 T.47 108 1.12 0.862 0.0 9.000 0.0011 0.010 Vel = 0.62 T.47 108 -0.14 1 Utr 2.0 2.000 150 18.219 to 0.0 2.000 0.0 T.48 108 0.98 0.862 0.0 4.000 0.0008 0.003 Vel = 0.54 T.48 108 0.14 1 Utr 2.0 7.000 150 18.222 to 0.0 2.000 0.0 T.49 108 1.12 0.862 0.0 9.000 0.0011 0.010 Vel = 0.62 T.49 108 0.0 1 Utr 2.0 10.000 150 18.232 to 0.0 2.000 0.0 H.28 108 1.12 0.862 0.0 12.000 0.0011 0.013 Vel = 0.62 H.28 108 0.0 1 Utr 2.0 11.000 150 18.245 to 0.0 2.000 0.0 H.29 108 1.12 0.862 0.0 13.000 0.0011 0.014 Vel = 0.62 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 9 RYNER RAMAN - One Head Calculation (H.27) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf H.29 108 0.0 1 0.0 14.000 150 18.259 to 0.0 0.0 0.0 H.32 108 1.12 0.862 0.0 14.000 0.0011 0.016 Vel = 0.62 H.32 108 0.0 1 Utr 2.0 11.000 150 18.275 to 0.0 2.000 0.0 H.26 108 1.12 0.862 0.0 13.000 0.0011 0.014 Vel = 0.62 H.26 108 0.0 1 Utr 2.0 14.000 150 18.289 to 0.0 2.000 0.0 H.16 108 1.12 0.862 0.0 16.000 0.0011 0.017 Vel = 0.62 H.16 108 0.0 1 Utr 2.0 10.000 150 18.306 to 0.0 2.000 0.0 H.17 108 1.12 0.862 0.0 12.000 0.0011 0.013 Vel = 0.62 H.17 108 0.0 1 0.0 5.000 150 18.319 to 0.0 0.0 0.0 T.40 108 1.12 0.862 0.0 5.000 0.0010 0.005 Vel = 0.62 0.0 T.40 1.12 18.324 K Factor = 0.26 T.47 108 0.14 0.75 Utb 17.0 3.000 150 18.219 to Utr 2.0 19.000 0.0 H.23 108 0.14 0.671 0.0 22.000 0.0001 0.002 Vel = 0.13 H.23 108 0.0 0.75 Utb 17.0 3.000 150 18.221 to 0.0 17.000 0.0 T.48 108 0.14 0.671 0.0 20.000 0 0.001 Vel = 0.13 0.0 T.48 0.14 18.222 K Factor = 0.03 T.43 108 0.27 0.75 Utb 17.0 2.000 150 18.279 to 0.0 17.000 0.0 H.20 108 0.27 0.671 0.0 19.000 0.0003 0.005 Vel = 0.24 H.20 108 0.0 0.75 Utb 17.0 2.000 150 18.284 to Utr 2.0 19.000 0.0 T.42 108 0.27 0.671 0.0 21.000 0.0003 0.006 Vel = 0.24 0.0 T.42 0.27 18.290 K Factor = 0.06 T.33 116 2.32 1 Utr 2.0 8.000 150 15.096 to 0.0 2.000 0.0 H.7 116 2.32 0.862 0.0 10.000 0.0042 0.042 Vel = 1.28 H.7 116 0.0 1 Utb 17.0 7.000 150 15.138 to 0.0 14.000 0.0 T.37 116 2.32 0.862 0.0 21.000 0.0042 0.088 Vel = 1.28 0.0 T.37 2.32 15.226 K Factor = 0.59 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 INSTALLING CONTRACTOR STAMP: DESIGN ONLY STAMP: A010 DESIGN ■ E]c WASHINGTON STATE ■ 6 ■ DEC 31, 2S CERTIFICATE OF COMPETENCY FIRE SPRINKLER SYSTEMS ■ Libby Marie Babb ■ 3791-0722-A Level 1 ■ A-Pex Design Services, Inc. i APEXDDS782K5 ■ Sgnatlln DOO j A-PEX Design Services Inc. sales@a-pexdesignservices.com 11112 47th Avenue West Mukilteo, WA 98275 425-493-9680 Job Name RYNER RAMAN - Two Head Calculation (H.31 & H.25) Drawing RESIDENTIAL Location 1050 WALNUT ST EDMONDS WA 98020 Remote Area 1 Contract 241231-01 Data File 241231-01 Ryner Raman 1050 Walnut St.wx2 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 A-PEX Design Services Inc. RYNER RAMAN - Two Head Calculation (H.31 & H.25) HYDRAULIC DESIGN INFORMATION SHEET Name - RYNER RAMAN Location - EDMONDS WA 98020 Building - RESIDENTIAL Contractor - NEW WAY ENERGY Calculated By - LIBBY BABB Construction: (X) Combustible ( ) OCCUPANCY - RESIDENTIAL Page 1 Date 12/31 /2024 Date - 12-31-2024 System No. - 1 Contract No. - 241231-01 Drawing No. - Non -Combustible Ceiling Height S Type of Calculation: ( )NFPA 13 Residential ( )NFPA 13R (X)NFPA 13D Y Number of Sprinklers Flowing: ( )1 (X)2 ( )4 ( ) S ( ) Other T ( )Specific Ruling Made by Date E M Listed Flow at Start Point - 13 Gpm System Type Listed Pres. at Start Point - 7.04 Psi (X) Wet ( ) Dry D MAXIMUM LISTED SPACING 16 x 16 ( ) Deluge ( ) PreAction E Domestic Flow Added - 0 Gpm Sprinkler or Nozzle S Additional Flow Added - Gpm Make LF SENJU SPRINKLER Model RC-RES I Elevation at Highest Outlet - 116 Feet Size 7/16 K-Factor 4.9 G Note: Temperature Rating 155 N Calculation Gpm Required 26.0681 Psi Required 49.8 At Ref Pt STR Summary C-Factor Used: Overhead 150 Underground 150 W Water Flow Test: Pump Data: A Date of Test - Rated Cap. T Time of Test - @ Psi E Static (Psi) - 55 Elev. R Residual (Psi) - 20 Other Flow (Gpm) - 500 S Elevation - 100 P Location: P L Source of Information: Y Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply Curve C A-PEX Design Services Inc. Page 2 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 City Water Supply: Demand: C1 - Static Pressure 55 D1 - Elevation 6.930 C2 - Residual Pressure: 20 D2 - System Flow : 26.068 C2 - Residual Flow 500 D2 - System Pressure 49.798 Hose ( Demand ) D3 - System Demand : 26.068 Safety Margin 5.053 150 140 130 P 120 R 110 E 100 S 90 S 80 U 70 R 60 E 50 40 30 20 10 D1 50 100 150 200 250 300 350 400 450 FLOW (N^1.85) C2 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Fittings Used Summary A-PEX Design Services Inc. Page 3 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 Fitting Legend Abbrev. Name E 90' Standard Elbow 2 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 G Generic Gate Valve 1 1 1 1 1 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 T 90' Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Utb Aquapex Tee - Branch 2 17 14 9 12 17 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Utr Aquapex Tee - Run 1 2 2 4 2 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Units Summary Diameter Units Length Units Flow Units Pressure Units Inches Feet US Gallons per Minute Pounds per Square Inch Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - NFPA 2007 A-PEX Design Services Inc. RYNER RAMAN - Two Head Calculation (H.31 & H.25) Page 4 Date 12/31 /2024 SUPPLY ANALYSIS Node at Static Residual Available Source Pressure Pressure Flow Pressure Total Demand Required Pressure STR 55.0 20 500.0 54.852 26.07 49.798 NODE ANALYSIS Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes H.31 116.0 4.9 7.04 13.0 H.27 116.0 8.45 H.30 116.0 9.93 H.24 116.0 10.58 T.45 116.0 10.99 T.46 116.0 11.34 T.40 108.0 15.53 H.10 108.0 16.32 T.35 108.0 16.48 T.36 108.0 16.95 S.1 104.0 19.51 MTR 100.0 30.09 STR 100.0 49.8 H.25 116.0 4.9 7.11 13.07 H.22 116.0 8.35 T.41 116.0 9.58 T.44 108.0 14.78 T.43 108.0 14.96 T.42 108.0 14.99 H.15 108.0 15.17 H.1 108.0 15.49 H.2 108.0 15.69 H.3 108.0 15.89 T.34 108.0 16.09 H.5 108.0 16.27 H.6 108.0 16.64 H.14 116.0 9.8 H.11 116.0 10.12 HA 116.0 10.69 H.9 116.0 11.45 H.8 116.0 11.89 T.33 116.0 12.25 T.47 108.0 14.84 T.48 108.0 14.86 T.49 108.0 14.93 H.28 108.0 15.01 H.29 108.0 15.11 H.32 108.0 15.21 H.26 108.0 15.3 H.16 108.0 15.41 H.17 108.0 15.5 H.21 116.0 11.49 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - NFPA 2007 A-PEX Design Services Inc. RYNER RAMAN - Two Head Calculation (H.31 & H.25) NODE ANALYSIS (cont.) Page 5 Date 12/31 /2024 Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes H.19 116.0 11.65 T.39 116.0 11.74 H.13 116.0 11.9 H.18 116.0 12.02 T.38 116.0 12.21 H.12 116.0 12.37 T.37 116.0 12.74 H.23 108.0 14.85 H.20 108.0 14.97 H.7 116.0 12.41 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams - 2007 A-PEX Design Services Inc. Page 6 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf H.31 116 4.90 9.72 1 Utr 2.0 22.000 150 7.040 to 0.0 2.000 0.0 H.27 116 9.72 0.862 0.0 24.000 0.0589 1.414 Vel = 5.34 H.27 116 0.0 1 Utr 2.0 23.000 150 8.454 to 0.0 2.000 0.0 H.30 116 9.72 0.862 0.0 25.000 0.0589 1.473 Vel = 5.34 H.30 116 0.0 1 Utr 2.0 9.000 150 9.927 to 0.0 2.000 0.0 H.24 116 9.72 0.862 0.0 11.000 0.0589 0.648 Vel = 5.34 H.24 116 0.0 1 Utr 2.0 5.000 150 10.575 to 0.0 2.000 0.0 T.45 116 9.72 0.862 0.0 7.000 0.0589 0.412 Vel = 5.34 T.45 116 0.0 1 Utr 2.0 4.000 150 10.987 to 0.0 2.000 0.0 T.46 116 9.72 0.862 0.0 6.000 0.0590 0.354 Vel = 5.34 T.46 116 -4.83 1 2Utb 34.0 16.000 150 11.341 to 0.0 28.000 3.465 T.40 108 4.89 0.862 0.0 44.000 0.0165 0.728 Vel = 2.69 T.40 108 3.11 1 Utr 2.0 17.000 150 15.534 to 0.0 2.000 0.0 H.10 108 8.0 0.862 0.0 19.000 0.0411 0.781 Vel = 4.40 H.10 108 0.0 1 Utr 2.0 2.000 150 16.315 to 0.0 2.000 0.0 T.35 108 8.0 0.862 0.0 4.000 0.0410 0.164 Vel = 4.40 T.35 108 9.61 1.5 Utb 12.0 4.000 150 16.479 to 0.0 12.000 0.0 T.36 108 17.61 1.244 0.0 16.000 0.0297 0.475 Vel = 4.65 T.36 108 8.46 1.5 T 3.443 10.000 150 16.954 to 0.0 3.443 1.732 S.1 104 26.07 1.244 0.0 13.443 0.0613 0.824 Vel = 6.88 S.1 104 0.0 1.5 2E 3.443 92.000 150 19.510 to 0.0 3.443 4.732 * * Fixed Loss = 3 MTR 100 26.07 1.244 0.0 95.443 0.0613 5.851 Vel = 6.88 MTR 100 0.0 0.75 E 1.85 20.000 150 30.093 to T 3.7 6.475 0.0 STR 100 26.07 0.745 G 0.925 26.475 0.7443 19.705 Vel = 19.19 0.0 STR 26.07 49.798 K Factor = 3.69 H.31 116 3.29 1 0.0 9.000 150 7.040 to 0.0 0.0 0.0 H.25 116 3.29 0.862 0.0 9.000 0.0079 0.071 Vel = 1.81 H.25 116 4.90 13.06 1 Utr 2.0 6.000 150 7.111 to 0.0 2.000 0.0 H.22 116 16.35 0.862 0.0 8.000 0.1544 1.235 Vel = 8.99 H.22 116 0.0 1 Utr 2.0 6.000 150 8.346 to 0.0 2.000 0.0 T.41 116 16.35 0.862 0.0 8.000 0.1545 1.236 Vel = 8.99 T.41 116 -8.34 1 2Utb 34.0 14.000 150 9.582 to 0.0 28.000 3.465 T.44 108 8.01 0.862 0.0 42.000 0.0412 1.731 Vel = 4.40 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 7 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf T.44 108 -3.10 1 Utr 2.0 9.000 150 14.778 to 0.0 2.000 0.0 T.43 108 4.91 0.862 0.0 11.000 0.0166 0.183 Vel = 2.70 T.43 108 -0.46 1 0.0 2.000 150 14.961 to 0.0 0.0 0.0 T.42 108 4.45 0.862 0.0 2.000 0.0140 0.028 Vel = 2.45 T.42 108 0.46 1 Utr 2.0 9.000 150 14.989 to 0.0 2.000 0.0 H.15 108 4.91 0.862 0.0 11.000 0.0166 0.183 Vel = 2.70 H.15 108 0.0 1 Utr 2.0 17.000 150 15.172 to 0.0 2.000 0.0 H.1 108 4.91 0.862 0.0 19.000 0.0167 0.317 Vel = 2.70 H.1 108 0.0 1 Utr 2.0 10.000 150 15.489 to 0.0 2.000 0.0 H.2 108 4.91 0.862 0.0 12.000 0.0166 0.199 Vel = 2.70 H.2 108 0.0 1 Utr 2.0 10.000 150 15.688 to 0.0 2.000 0.0 H.3 108 4.91 0.862 0.0 12.000 0.0167 0.200 Vel = 2.70 H.3 108 0.0 1 Utr 2.0 10.000 150 15.888 to 0.0 2.000 0.0 T.34 108 4.91 0.862 0.0 12.000 0.0167 0.200 Vel = 2.70 T.34 108 3.55 1 Utr 2.0 2.000 150 16.088 to 0.0 2.000 0.0 H.5 108 8.46 0.862 0.0 4.000 0.0455 0.182 Vel = 4.65 H.5 108 0.0 1 Utr 2.0 6.000 150 16.270 to 0.0 2.000 0.0 H.6 108 8.46 0.862 0.0 8.000 0.0456 0.365 Vel = 4.65 H.6 108 0.0 1 Utr 2.0 5.000 150 16.635 to 0.0 2.000 0.0 T.36 108 8.46 0.862 0.0 7.000 0.0456 0.319 Vel = 4.65 0.0 T.36 8.46 16.954 K Factor = 2.05 T.41 116 8.34 1 Utr 2.0 3.000 150 9.582 to 0.0 2.000 0.0 H.14 116 8.34 0.862 0.0 5.000 0.0444 0.222 Vel = 4.59 H.14 116 0.0 1 Utr 2.0 5.000 150 9.804 to 0.0 2.000 0.0 H.11 116 8.34 0.862 0.0 7.000 0.0444 0.311 Vel = 4.59 H.11 116 0.0 1 Utr 2.0 11.000 150 10.115 to 0.0 2.000 0.0 HA 116 8.34 0.862 0.0 13.000 0.0445 0.578 Vel = 4.59 HA 116 0.0 1 Utr 2.0 15.000 150 10.693 to 0.0 2.000 0.0 H.9 116 8.34 0.862 0.0 17.000 0.0444 0.755 Vel = 4.59 H.9 116 0.0 1 0.0 10.000 150 11.448 to 0.0 0.0 0.0 H.8 116 8.34 0.862 0.0 10.000 0.0445 0.445 Vel = 4.59 H.8 116 0.0 1 Utr 2.0 6.000 150 11.893 to 0.0 2.000 0.0 T.33 116 8.34 0.862 0.0 8.000 0.0445 0.356 Vel = 4.59 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 8 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf T.33 116 -4.79 1 2Utb 34.0 13.000 150 12.249 to 0.0 28.000 3.465 T.34 108 3.55 0.862 0.0 41.000 0.0091 0.374 Vel = 1.95 0.0 T.34 3.55 16.088 K Factor = 0.89 T.44 108 3.10 1 Utr 2.0 7.000 150 14.778 to 0.0 2.000 0.0 T.47 108 3.1 0.862 0.0 9.000 0.0071 0.064 Vel = 1.70 T.47 108 -0.39 1 Utr 2.0 2.000 150 14.842 to 0.0 2.000 0.0 T.48 108 2.71 0.862 0.0 4.000 0.0055 0.022 Vel = 1.49 T.48 108 0.39 1 Utr 2.0 7.000 150 14.864 to 0.0 2.000 0.0 T.49 108 3.1 0.862 0.0 9.000 0.0071 0.064 Vel = 1.70 T.49 108 0.0 1 Utr 2.0 10.000 150 14.928 to 0.0 2.000 0.0 H.28 108 3.1 0.862 0.0 12.000 0.0072 0.086 Vel = 1.70 H.28 108 0.0 1 Utr 2.0 11.000 150 15.014 to 0.0 2.000 0.0 H.29 108 3.1 0.862 0.0 13.000 0.0072 0.093 Vel = 1.70 H.29 108 0.0 1 0.0 14.000 150 15.107 to 0.0 0.0 0.0 H.32 108 3.1 0.862 0.0 14.000 0.0071 0.099 Vel = 1.70 H.32 108 0.0 1 Utr 2.0 11.000 150 15.206 to 0.0 2.000 0.0 H.26 108 3.1 0.862 0.0 13.000 0.0072 0.093 Vel = 1.70 H.26 108 0.0 1 Utr 2.0 14.000 150 15.299 to 0.0 2.000 0.0 H.16 108 3.1 0.862 0.0 16.000 0.0071 0.114 Vel = 1.70 H.16 108 0.0 1 Utr 2.0 10.000 150 15.413 to 0.0 2.000 0.0 H.17 108 3.1 0.862 0.0 12.000 0.0072 0.086 Vel = 1.70 H.17 108 0.0 1 0.0 5.000 150 15.499 to 0.0 0.0 0.0 T.40 108 3.1 0.862 0.0 5.000 0.0070 0.035 Vel = 1.70 0.0 T.40 3.10 15.534 K Factor = 0.79 T.46 116 4.82 1 0.0 9.000 150 11.341 to 0.0 0.0 0.0 H.21 116 4.82 0.862 0.0 9.000 0.0161 0.145 Vel = 2.65 H.21 116 0.0 1 Utr 2.0 8.000 150 11.486 to 0.0 2.000 0.0 H.19 116 4.82 0.862 0.0 10.000 0.0161 0.161 Vel = 2.65 H.19 116 0.0 1 Utr 2.0 4.000 150 11.647 to 0.0 2.000 0.0 T.39 116 4.82 0.862 0.0 6.000 0.0162 0.097 Vel = 2.65 T.39 116 0.0 1 Utr 2.0 8.000 150 11.744 to 0.0 2.000 0.0 H.13 116 4.82 0.862 0.0 10.000 0.0161 0.161 Vel = 2.65 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen -Williams A-PEX Design Services Inc. Page 9 RYNER RAMAN - Two Head Calculation (H.31 & H.25) Date 12/31/2024 Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftng's Pe ******* Notes Node2 Elev2 Fact Qt Act Eqv. Ln. Total Pf/Ft Pf H.13 116 0.0 1 0.0 7.000 150 11.905 to 0.0 0.0 0.0 H.18 116 4.82 0.862 0.0 7.000 0.0161 0.113 Vel = 2.65 H.18 116 0.0 1 Utr 2.0 10.000 150 12.018 to 0.0 2.000 0.0 T.38 116 4.82 0.862 0.0 12.000 0.0161 0.193 Vel = 2.65 T.38 116 0.0 1 Utr 2.0 8.000 150 12.211 to 0.0 2.000 0.0 H.12 116 4.82 0.862 0.0 10.000 0.0161 0.161 Vel = 2.65 H.12 116 0.0 1 Utb 17.0 7.000 150 12.372 to Utr 2.0 16.000 0.0 T.37 116 4.82 0.862 0.0 23.000 0.0161 0.371 Vel = 2.65 T.37 116 4.80 1.5 Utb 12.0 16.000 150 12.743 to 0.0 12.000 3.465 T.35 108 9.62 1.244 0.0 28.000 0.0097 0.271 Vel = 2.54 0.0 T.35 9.62 16.479 K Factor = 2.37 T.47 108 0.39 0.75 Utb 17.0 3.000 150 14.842 to Utr 2.0 19.000 0.0 H.23 108 0.39 0.671 0.0 22.000 0.0005 0.012 Vel = 0.35 H.23 108 0.0 0.75 Utb 17.0 3.000 150 14.854 to 0.0 17.000 0.0 T.48 108 0.39 0.671 0.0 20.000 0.0005 0.010 Vel = 0.35 0.0 T.48 0.39 14.864 K Factor = 0.10 T.43 108 0.46 0.75 Utb 17.0 2.000 150 14.961 to 0.0 17.000 0.0 H.20 108 0.46 0.671 0.0 19.000 0.0007 0.013 Vel = 0.42 H.20 108 0.0 0.75 Utb 17.0 2.000 150 14.974 to Utr 2.0 19.000 0.0 T.42 108 0.46 0.671 0.0 21.000 0.0007 0.015 Vel = 0.42 0.0 T.42 0.46 14.989 K Factor = 0.12 T.33 116 4.80 1 Utr 2.0 8.000 150 12.249 to 0.0 2.000 0.0 H.7 116 4.8 0.862 0.0 10.000 0.0159 0.159 Vel = 2.64 H.7 116 0.0 1 Utb 17.0 7.000 150 12.408 to 0.0 14.000 0.0 T.37 116 4.8 0.862 0.0 21.000 0.0160 0.335 Vel = 2.64 0.0 T.37 4.80 12.743 K Factor = 1.34 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087