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Report (54) cpps 2.��z 00il0z ,, 2_2 ,54.) •AC. II • s • I • 4. W YAT p. FIRE PROTECTION, INC. 9095 S.W. Burnham Tigard, OR 97223 ARLINGTON HEIGHTS #113 12723 SW WILLOW POINT LANE TIGARD, OREGON 97223 FIRE PROTECTION HYDRAULIC CALCULATIONS HYDRAULIC CALCULATIONS for Job Information Project Name:Arlington Heights#113 Contract No.:C14 4640 City: Tigard, OR 97223 Project Location: 12723SW Willow Point Lane Date:6/9/2014 Contractor Information Name of Contractor: Wyatt Fire Protection Address: 9095 SW Burnham Dr City: Tigard, OR 97223 Phone Number: (503)684-2928 E-mail:a.payne@wyattfire.com Name of Designer: Ashley Payne Authority Having Jurisdiction: City of Tigard Design Remote Area Name Foyer Remote Area Location Occupancy Classification Residential_NewCommodityl Density(gpm/ft2) 0.058 Area of Application(ft2) 512 Coverage per Sprinkler(ft2) 256 Number of Calculated Sprinklers 2 In-Rack Demand(gpm) 0 Special Heads Hose Streams(gpm) 0 Total Water Required(incl.Hose Streams)(gpm) 29.9 Required Pressure at Source(psi) 52.3 Type of System Wet Volume-Entire System (gal) 3.8 gal Water Supply Information Date Location Source Public Suppy Notes File:C:\Users\Ashley\Documents\Projects\Arlington\113\Arlington 113.tyc3 Date 6/9/2014 Copyright©2002-2012 Tyco Fire Protection Products Page 1 Job:Arlington Heights#113 Node Labels: Node Reference Pipe Labels: Off Diagram for Design Area : Foyer n12 n11 .414001 n17 h1 n18 n6 n4 3 2 1 File:C:\Users\Ashley\Documents\Projects\Arlington\1131Arlington 113.tyc3 Date 6/9/2014 Copyright©2002-2012 Tyco Fire Protection Products Page 2 Job:Arlington Heights#113 Hydraulic Analysis for : Foyer Calculation Info Calculation Mode Demand Hydraulic Model Hazen-Williams Fluid Name Water @ 60F (15.6C) Fluid Weight, (Ib/ft3) N/A for Hazen-Williams calculation. Fluid Dynamic Viscosity, (lb•s/ft2) N/A for Hazen-Williams calculation. Water Supply Parameters Supply 1 : S Flow(gpm) Pressure(psi) 0 118 L 1230 54 Hoses Inside Hose Flow/Standpipe Demand(gpm) Outside Hose Flow(gpm) Additional Outside Hose Flow(gpm) Other(custom defined) Hose Flow(gpm) Total Hose Flow(gpm) Sprinklers Ovehead Sprinkler Flow(gpm) 29.9 InRack Sprinkler Flow(gpm) 0 Other(custom defined)Sprinkler Flow(gpm) 0 Total Sprinkler Flow(gpm) 29.9 Other Required Margin of Safety(psi) 0 Base of Riser -Pressure(psi) 52.3 Base of Riser -Flow(gpm) 29.9 Demand w/o System Pump(s) N/A File:C:\Users\Ashley\Documents\Projects\Arlington\113\Arlington 113.tyc3 Date 6/9/2014 Copyright©2002-2012 Tyco Fire Protection Products Page 3 Job:Arlington Heights#113 Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Elev Hgroup Tot. Pres. Discharge K-Fact. Req. Discharge Req. Pres. ft psi gpm gpm/psilh gpm psi S 0 SUPPLY 52.3 -29.9 n1 3 NODE 50.2 n2 5 NODE 45.3 n3 6.5 NODE 44 n4 9 NODE 40.9 n5 9 NODE 38 n6 9 NODE 31.7 n7 18 NODE 22.1 n8 18 NODE 20.8 n9 18 NODE 19.5 n10 18 NODE 17.1 n11 18 NODE 17.5 n12 18 NODE 18.6 n14 18 NODE 20.6 n16 18 NODE 21.5 n17 18 NODE 14.1 n18 9 NODE 12.3 n20 9 NODE 8.1 h2 9 HEAD 7 14.8 5.6 14.8 7 hl 9 HEAD 7.3 15.1 5.6 14.8 7 File:C:\Users\Ashley\Documents\Projects\Arlington\113\Arlington 113.tyc3 Date 6/9/2014 Copyright©2002-2012 Tyco Fire Protection Products Page 4 Job name:Arlington Heights#113 Sheet number: PIPE INFORMATION Node 1 Elev 1 K-Factor 1 Flow added(q)* Nominal ID Fittings L C Factor total (Pt) Node 2 Elev 2 K-Factor 2 Total flow (Q) Actual ID quantity x (name) = length F Pf per ft elev (Pe) NOTES T frict (Pf) (ft) (gpm/psis/z) (gpm) (in) (ft) (ft) (psi) (psi) h2 9 5.6 14.8 .75 lx(BM.Tee-Br)=3 5.83 150 7 n20 9 14.8 0.874 3 0.1197 0 8.83 1.1 n20 9 15.1 .75 1x(BM.90)=4 5.58 150 8.1 n18 9 29.9 0.874 4 0.4403 0 9.58 4.2 '6 n18 9 0 .75 lx(BM.90)=4 9 150 12.3 n17 18 29.9 0.874 4 0.4403 -3.9 13 5.7 n17 18 0 .75 ix(BM.Tee-Br)=3 3.83 150 14.1 n10 18 29.9 0.874 3 0.4403 0 6.83 3 n10 18 -11.7 .75 lx(BM.Tee-Br)=3 10.83 150 17.1 n9 18 18.2 0.874 3 0.1757 0 13.83 2.4 n9 18 0 .75 lx(BM.90)=4 3 150 19.5 n8 18 18.2 0.874 4 0.1757 0 7 1.2 n8 18 0 .75 lx(BM.Tee-Br)=3 4.5 150 20.8 n7 18 18.2 0.874 3 0.1757 0 7.5 1.3 _ n7 18 11.7 .75 lx(BM.90)=4 9 150 22.1 n6 9 29.9 0.874 4 0.4403 3.9 13 5.7 • n6 9 0 .75 lx(BM.90)=4 10.25 150 31.7 n5 9 29.9 0.874 4 0.4403 0 14.25 6.3 n5 9 0 .75 lx(BM.90)=4 2.67 150 38 n4 9 29.9 0.874 4 0.4403 0 6.67 2.9 n4 9 0 .75 1x(coupling)=2.01 2.5 150 40.9 n3 6.5 29.9 0.874 2.01 0.4403 1.1 4.51 2 n3 6.5 0 1 1x(coupling)=1 1.5 120 44 n2 5 29.9 1.049 1 0.2737 0.6 2.5 0.7 n2 5 0 1 2 0 45.3 Ames20008 ni 3 29.9 0 0 1.9988 0.9 2 4 A n1 3 0 1 3 120 50.2 S 0 29.9 1.049 0 0.2737 1.3 '1 3 0.8 h1 9 5.6 15.1 .75 ix(BM.Tee-Br)=3 3.17 150 7.3 n20 9 15.1 0.874 3 0.1243 0 6.17 0.8 n10 18 0 .75 1x(BM.Tee-Br)=3 1.67 150 17.1 ' n11 18 11.7 0.874 3 0.0774 0 4.67 0.4 1 n11 18 0 .75 lx(BM.Tee-Br)=3 11.17 150 17.5 ' n12 18 11.7 0.874 3 0.0774 0 14.17 1.1 n12 18 0 .75 lx(BM.Tee-Run)=1 21.16 150 18.6 n14 18 11.7 0.874 lx(BM.90)=4 5 0.0774 0 26.16 2 ©2006 National Fire Protection Association Page 5 Job name:Arlington Heights#113 Sheet number: PIPE INFORMATION Node 1 Elev 1 K-Factor 1 Flow added(q)* Nominal ID Fittings L C Factor total (Pt) Node 2 Elev 2 K-Factor 2 Total flow (Q) Actual ID quantity x (name) = length F Pf per ft elev (Pe) NOTES T frict (Pf) (ft) (gPm/Psis/z) (9Pm) (in) (ft) (ft) (psi) (psi) n14 18 0 .75 lx(BM.Tee-Run)=1 8.17 150 20.6 n16 18 11.7 0.874 lx(BM.Tee-Br)=3 4 0.0774 0 12.17 0.9 n16 18 0 .75 lx(BM.Tee-Br)=3 4.16 150 21.5 n7 18 11.7 0.874 3 0.0774 0 7.16 0.6 * Discharge shown for flowing nodes only ©2006 National Fire Protection Association Page 6