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Specifications (30) ES Q\A- CCC-if CALCULATION SUMMARY o c ` ,01.hcA Project Name:DURHAM EDUCATION CENTER'�d00 331d40 d40 Project Location: 8040 SW DURHAM RD Drawing No. : City: TIGARD, OR 97224 `f UN 2 6 2018 fas t ? . 67) 01 ' ioNi Design Areas Design Area Calc. Mode Occupancy Area of Total Water Pressure @ Min. Min. Min. Calculated Hose Margin To Name (Model) Application Source Density Pressure Flow Heads Streams Source (ft2) (gpm) (psi) (gpm/ft2) (psi) (gpm) # (gpm) (psi) 1 Demand (HW) LIGHT HAZ 1500 333.4 Required 0.1 16.1 22.5 10 100 14.2 87.5 2 Demand (HW) LIGHT HAZ 1500 308 Required 0.1 16.1 22.5 9 100 2.3 99.5 File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 1 HYDRAULIC CALCULATIONS for Job Information Project Name:DURHAM EDUCATION CENTER Contract No. : City: TIGARD, OR 97224 Project Location: 8040 SW DURHAM RD Date:4/30/2018 Contractor Information Name of Contractor: FIRESTOP COMPANY Address: 3203 NORTHEAST 65TH ST,SPACE 2 City: VANCOUVER, WA 98663 Phone Number: E-mail: RYAN.BROYLES@BROWNINGFIRE.NET Name of Designer: R.BROYLES Authority Having Jurisdiction: CITY OF TIGARD Design Remote Area Name 1 Remote Area Location COMMONS OPEN AREA Occupancy Classification LIGHT HAZ Density(gpm/ft2) 0.1 Area of Application(ft2) 1500 if. Coverage per Sprinkler(ft2) 225 G 1" Number of Calculated Sprinklers 10 / 77506 PE 5-3-2018 In-Rack Demand(gpm) 0 OREGON Special Heads "n1/1/ 10 X00 Pte' Hose Streams(gpm) 100 �RY L • O'k\ Total Water Required(incl.Hose Streams)(gpm) 333.4 EXPIRATION DATE:12/31/18 Required Pressure at Source(psi) 87.5 Type of System Wet Volume-Entire System (gal) 123.1 gal Water Supply Information Date 5/18/17 Location 7980 SW DURHAM Source W1 Notes File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 2 Job:DURHAM EDUCATION CENTER • Hydraulic Analysis for : 1 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 :W1 Flow(gpm) Pressure(psi) 0 102 1475 97 6680 20 Supply Analysis Residual Available Static Pressure Flow Total Demand Required Pressure Node at Source Pressure Pressure (psi) (psi) (gpm) (psi) (gpm) (psi) W1 102 97 1475 101.8 333.4 87.5 Hoses Inside Hose Flow/Standpipe Demand(gpm) Outside Hose Flow(gpm) Additional Outside Hose Flow(gpm) 100 Other(custom defined) Hose Flow(gpm) Total Hose Flow(gpm) 100 Sprinklers Ovehead Sprinkler Flow(gpm) 233.4 InRack Sprinkler Flow(gpm) 0 Other(custom defined)Sprinkler Flow(gpm) 0 Total Sprinkler Flow(gpm) 233.4 Other Required Margin of Safety(psi) 0 W1 -Pressure(psi) 87.5 W1 -Flow(gpm) 233.4 Demand w/o System Pump(s) N/A File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 4 I Job:DURHAM EDUCATION CENTER Hydraulic Analysis for : I •Svsbam DranandII. ., 150 1 t , 731. ...-_._. ...__.__ ..........._.__ ._.,.,._....... .__a. .-....._ _ .k1--'_.__._..._. ,.. __. ...._ _.._,--. E I 1 s F f [ E U1 I -' I 3 1. i� : I f : ,! i { # , qj 4 I ... -. i . _ .. , 4 b 7 2503 3000 :...M i... 4Sco s'10 S9)0 6000 --- FI , 7gpiTt File:C:\Users'Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 5 Job:DURHAM EDUCATION CENTER Hydraulic Analysis for : 1 Graph Labels Label Description Values Flow (gpm) Pressure (psi) S1 Supply point#1 -Static 0 102 S2 Supply point#2 1475 97 S3 Supply point#3 6680 20 D1 Elevation Pressure 0 14.3 D2 System Demand 233.4 87.5 D3 System Demand+Add.Out.Hose 333.4 87.5 Curve Intersections &Safety Margins Curve Name Intersection Safety Margin Pressure (psi) Flow (gpm) Pressure (psi) @ Flow (gpm) Supply 101.8 257 14.2 333.4 Open Heads Required Calculated Head Ref. Head Type Coverage K-Factor Density Flow Pressure Density Flow Pressure (ft2) (gpm/Psi'/2) (gpm/ft2) (gpm) (psi) (gpm/ft2) (gpm) (psi) Al Overhead 225 5.6 0.1 22.5 16.1 0.1 22.5 16.1 Sprinkler ASO Overhead 225 5.6 0.1 22.5 16.1 0.113 25.4 20.6 Sprinkler A2 Overhead 225 5.6 0.1 22.5 16.1 0.101 22.8 16.6 Sprinkler A3 Overhead 225 5.6 0.1 22.5 16.1 0.104 23.3 17.3 Sprinkler A4 Overhead 225 5.6 0.1 22.5 16.1 0.101 22.6 16.3 Sprinkler A5 Overhead 225 5.6 0.1 22.5 16.1 0.102 23 16.8 Sprinkler A6 Overhead 225 5.6 0.1 22.5 16.1 0.104 23.5 17.5 Sprinkler A7 Overhead 225 5.6 0.1 22.5 16.1 0.102 23 16.9 Sprinkler A8 Overhead 225 5.6 0.1 22.5 16.1 0.104 23.4 17.4 Sprinkler A9 Overhead 225 5.6 0.1 22.5 16.1 0.106 23.9 18.1 Sprinkler File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 6 Job:DURHAM EDUCATION CENTER Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Type K-Fact. Discharge Coverage Tot. Pres. Req. Pres. Elev Hgroup Open/Closed Overdischarge Density Elev. Pres. Req. Discharge 9Pm/Psi'/z gpm ft2 psi psi ft gpm gpm/ft2 psi gpm 002 Node 18 30 NODE -14.3 006 Node 18.2 30 NODE -14.3 007 Node 18.8 30 NODE -14.3 008 Node 21.7 30 NODE -14.3 009 Node 21.7 30 NODE -14.3 185 Node 82.9 -3 NODE 0 186-I Node 83.2 -3 NODE 0 186-0 Node 83 -3 NODE 0 188-I Node 87.3 -3 NODE 0 188-0 Node 83.6 -3 NODE 0 Al Overhead Sprinkler 5.6 22.5 225 16.1 16.1 30 HEAD Open 0 0.1 -14.3 22.5 A10 Overhead Sprinkler 5.6 25.4 225 20.6 16.1 30 HEAD Open 2.9 0.113 -14.3 22.5 A2 Overhead Sprinkler 5.6 22.8 225 16.6 16.1 30 HEAD Open 0.3 0.101 -14.3 22.5 A3 Overhead Sprinkler 5.6 23.3 225 17.3 16.1 30 HEAD Open 0.8 0.104 -14.3 22.5 A4 Overhead Sprinkler 5.6 22.6 225 16.3 16.1 30 HEAD Open 0.1 0.101 -14.3 22.5 A5 Overhead Sprinkler 5.6 23 225 16.8 16.1 30 HEAD Open 0.5 0.102 -14.3 22.5 A6 Overhead Sprinkler 5.6 23.5 225 17.5 16.1 30 HEAD Open 1 0.104 -14.3 22.5 A7 Overhead Sprinkler 5.6 23 225 16.9 16.1 30 HEAD Open 0.5 0.102 -14.3 22.5 A8 Overhead Sprinkler 5.6 23.4 225 17.4 16.1 30 HEAD Open 0.9 0.104 -14.3 22.5 A9 Overhead Sprinkler 5.6 23.9 225 18.1 16.1 30 HEAD Open 1.4 0.106 -14.3 22.5 W1 Supply 87.5 -233.4 -3 SUPPLY 0 File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 7 Job:DURHAM EDUCATION CENTER Hydraulic Calculations 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/2) (gpm) (in) (ft) (ft) (psi) (psi) Path No: 1 Al 30 5.6 22.5 1.25 14 120 16.1 A2 30 5.6 22.5 1.442 0 0.0342 0 14 0.5 A2 30 5.6 22.8 1.25 lx(us.Tee-Br)=7.43 3.48 120 16.6 002 30 45.3 1.442 7.43 0.1253 0 10.91 1.4 002 30 23.3 2.5 15 120 18 006 30 68.6 2.635 0 0.0143 0 15 0.2 006 30 69.1 2.5 12 120 18.2 007 30 137.7 2.635 0 0.0521 0 12 0.6 007 30 70.2 2.5 lx(us.Tee-Br)=16.47 9.14 120 18.8 008 30 207.9 2.635 16.47 0.1117 0 25.62 2.9 008 30 25.4 2.5 9x(us.90)=74.13 215.25 120 21.7 185 -3 233.4 2.635 3x(us.Tee-Br)=49.42 123.56 0.1383 14.3 338.81 46.9 185 -3 0 4 lx(coupling)=1.83 14.38 140 82.9 186-0 -3 233.4 4.3 1.83 0.0096 0 16.21 0.2 186-0 -3 0 4 0.17 0 83 BFV-N 186-I -3 233.4 0 0 0.8902 0 *** 0.17 0.2 186-I -3 0 4 lx(coupling)=1.83 24.46 140 83.2 188-0 -3 233.4 4.3 lx(us.90)=18.33 20.16 0.0096 0 44.62 0.4 188-0 -3 0 4 2.81 0 83.6 AmesC300H 188-I -3 233.4 0 0 1.3363 0 *** 2.81 3.8 188-I -3 0 4 18.18 140 87.3 W1 -3 233.4 4.3 0 0.0096 0 18.18 0.2 W1 87.5 Path No: 2 A4 30 5.6 22.6 1.25 14 120 16.3 A5 30 5.6 22.6 1.442 0 0.0346 0 14 0.5 A5 30 5.6 23 1.25 1x(us.Tee-Br)=7.43 3.48 120 16.8 006 30 45.6 1.442 7.43 0.1267 0 10.91 1.4 006 18.2 File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 8 Job:DURHAM EDUCATION CENTER Hydraulic Calculations PIPE INFORMATION Path No: 3 A7 30 5.6 23 1.25 14 120 16.9 A8 30 5.6 23 1.442 0 0.0357 0 14 0.5 A8 30 5.6 23.4 1.25 1x(us.Tee-Br)=7.43 3.48 120 17.4 007 30 46.4 1.442 7.43 0.1308 0 10.91 1.4 007 18.8 Path No: 4 A3 30 5.6 231 1.25 lx(us.Tee-Br)=7.43 10.52 120 17.3 002 30 23 1.442 7.43 0.0366 0 17.95 0.7 002 18 Path No: 5 • A6 30 5.6 23.5 1.25 lx(us.Tee-Br)=7.43 . 10.52 120 17.5 006 30 23.5 1.442 7.43 0.037 0 17.95 0.7 006 - 18.2 Path No: 6 A9 30 5.6 23.9 1.25 lx(us.Tee-Br)=7.43 10.52 120 18.1 007 30 23.9 1.442 7.43 0.0382 0 17.95 0.7 007 18.8 Path No: 7 A10 30• 5.6 25.4E 1.25 lx(us.Tee-Br)=7.43 17.48 120 20.6 009 30 25.4 1.442 7.43 0.0429 0 24.91 1.1 009 30 0 2.5 1x(us.Tee-Br)=16.47 0.86 120 21.7 008 30 25.4 2.635 16.47 0.0023 0 17.33 0.0 008 21.7 * Pressures are balanced to a high degree of accuracy. Values may vary by 0.1 psi due to display rounding. * Maximum Velocity of 13.73 ft/s occurs in the following pipe(s): (185-008) *** Device pressure loss (gain in the case of pumps) is calculated from the device's curve. If the device curve is printed with this report, it will appear below. The length of the device as shown in the table above comes from the CAD drawing.The friction loss per unit of length is calculated based upon the length and the curve-based loss/gain value. Internal ID and C Factor values are irrelevant as the device is not represented as an addition to any pipe, but is an individual item whose loss/gain is based solely on the curve data. File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 9 Job:DURHAM EDUCATION CENTER Device Graphs Pressure vs. Flow Function Design Arm 1; Supply Ref.:WI; Supply N ne: }._.— 1 Y13t !— 105 € t a z �......_.. .. c 1 i Ars Ey5_ 3 44t .. j I W G 1 __ . ..�_____ _. __ , i 4 4 4 0 4 4 0 4 4 0 0 0 4. 4 4 4 "IR 4 al a 4 CD 0VI 4 4 CI VI, 4 0- CO WI IC FlugPm Pressure Loss Function Design Area: 1; BFP Ref.: 396 (Am C H,'Size = 41Inlet Node: 1: l; Outlet Node: 1.*: 0 18:8 Ilam. e,n w . �®�. ,. ._.. _ I .� .._s : _...._. .�. j 13_F a_ ' 1 .. . . .W._. { ... 118 .... a I t. 14.8 _. . I 1.ew ?8 __.._____ I _s I I 3.8 psi Q 233.4 goal 1 8 - .0 4 4 4 4 4 4 4 4- 4 4' AC 4- .. Ct4. 4 4: 4 4 4 rr m kn cc 1 gPin File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright 0 2002-2012 Tyco Fire Protection Products Page 10 Job:DURHAM EDUCATION CENTER Device Graphs Pressure Loss Function Design unct onign Area: 1; Valve Ret: (BFV-N Size- Inlet Node: 186-1; Outlet Node: 186-C y i 4.428- _ __ .. ... m_. . l 1423-.._ i 0.2 psi qt 233.4 gpm i I 1 , - r - o 4 a, ppm File:C:\Users'Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 11 HYDRAULIC CALCULATIONS for Job Information Project Name:DURHAM EDUCATION CENTER Contract No. : City: TIGARD, OR 97224 Project Location: 8040 SW DURHAM RD Date:4/30/2018 Contractor Information Name of Contractor: FIRESTOP COMPANY Address: 3203 NORTHEAST 65TH ST,SPACE 2 City: VANCOUVER, WA 98663 Phone Number: E-mail:RYAN.BROYLES@BROWNINGFIRE.NET Name of Designer: R.BROYLES Authority Having Jurisdiction: CITY OF TIGARD Design Remote Area Name 2 Remote Area Location MAKER SPACE Occupancy Classification LIGHT HAZ Density(gpm/ft2) 0.1 Area of Application(ft2) 1500 , r Coverage per Sprinkler(ft2) 2257 '' �� ► Number of Calculated Sprinklers 9 Or�G yl In-Rack Demand(gpm) 0 77506 PE 5-3-2018 Special Heads OREGON �o Hose Streams(gpm) 100 v<�R 0 ��P� Total Water Required(incl.Hose Streams)(gpm) 308 Y L 0' Required Pressure at Source(psi) 99.5 EXPIRATION DATE:12/31/18 Type of System Wet Volume-Entire System (gal) 157 gal Water Supply Information Date 5/18/17 Location 7980 SW DURHAM Source W1 Notes File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 12 Job:DURHAM EDUCATION CENTER • Hydraulic Analysis for : 2 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 :W1 Flow(qpm) Pressure(psi) 0 102 1475 97 6680 20 Supply Analysis Residual Available Static Pressure Flow Total Demand Required Pressure Node at Source Pressure Pressure (psi) (psi) (gpm) (psi) (gpm) (psi) W1 102 97 1475 101.9 308 99.5 Hoses Inside Hose Flow/Standpipe Demand(gpm) Outside Hose Flow(gpm) Additional Outside Hose Flow(gpm) 100 Other(custom defined) Hose Flow(gpm) Total Hose Flow(gpm) 100 Sprinklers Ovehead Sprinkler Flow(gpm) 208 InRack Sprinkler Flow(gpm) 0 Other(custom defined)Sprinkler Flow(gpm) 0 Total Sprinkler Flow(gpm) 208 Other Required Margin of Safety(psi) 0 W1 -Pressure(psi) 99.5 W1 -Flow(gpm) 208 Demand w/o System Pump(s) N/A File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 14 • Job:DURHAM EDUCATION CENTER Hydraulic Analysis for : 2 in Vostem ParAwi.d f .0,4.Hoag, i 95r- E , i in , i t .t ..... ... i _ t 1. 1 ' , , I— i 1 1 i I t_L , 1 1 G01 ..G01 E._ t , . y .. ___.....m air- _ w....�._........__._ 0 2000 MCC 3030 :MCC 44M0 40)0 5E0) 5500 ED:0 5500 7000 rstx) Flaw,upon File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 15 Job:DURHAM EDUCATION CENTER Hydraulic Analysis for : 2 Graph Labels Label Description Values Flow (gpm) Pressure (psi) S1 Supply point#1 -Static 0 102 S2 Supply point#2 1475 97 S3 Supply point#3 _ 6680 20 D1 Elevation Pressure 0 6.5 D2 System Demand 208 99.5 D3 System Demand+Add.Out.Hose 308 99.5 Curve Intersections &Safety Margins Curve Name Intersection Safety Margin Pressure (psi) Flow (gpm) Pressure (psi) @ Flow (gpm) Supply 101.9 210.9 2.3 308 Open Heads Required Calculated Head Ref. Head Type Coverage K-Factor ---. • Density Flow Pressure Density Flow Pressure (ft2) (gpm/psiY) (gpm/ft2) (gpm) (psi) (gpm/ft2) (gpm) (psi) B1 Overhead 225 5.6 0.1 22.5 16.1 0.1 22.5 16.1 Sprinkler B2 Overhead 225 5.6 0.1 22.5 16.1 0.1 22.5 16.1 Sprinkler B3 Overhead 225 5.6 0.1 22.5 16.1 0.1 22.5 16.2 Sprinkler B4 Overhead 225 5.6 0.1 22.5 16.1 0.101 22.8 16.6 Sprinkler B5 Overhead 225 5.6 0.1 22.5 16.1 0.101 22.8 16.5 Sprinkler B6 Overhead 225 5.6 0.1 22.5 16.1 0.102 22.9 16.7 Sprinkler B7 Overhead 225 5.6 0.1 22.5 16.1 0.107 24 18.3 Sprinkler B8 Overhead 225 5.6 0.1 22.5 16.1 0.106 23.9 18.3 Sprinkler B9 Overhead 225 5.6 0.1 22.5 16.1 0.107 24.2 18.6 Sprinkler File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 16 Job:DURHAM EDUCATION CENTER Hydraulic Calculations/Fluid Delivery Time Analysis Node Data Node# Type K-Fact. Discharge Coverage Tot. Pres. Req. Pres. Elev Hgroup Open/Closed Overdischarge Density Elev. Pres. Req. Discharge sig/z gpm ft2 psi psi ft gpm/p gpm gpm/ft2 psi gpm B2 Overhead Sprinkler 5.6 22.5 225 16.1 16.1 12 HEAD Open 0 0.1 -6.5 22.5 B1 Overhead Sprinkler 5.6 22.5 225 16.1 16.1 12 HEAD Open 0 0.1 -6.5 22.5 B3 Overhead Sprinkler 5.6 22.5 225 16.2 16.1 12 HEAD Open 0 0.1 -6.5 22.5 B5 Overhead Sprinkler 5.6 22.8 225 16.5 16.1 12 HEAD Open 0.3 0.101 -6.5 22.5 • Overhead Sprinkler 5.6 22.8 225 16.6 16.1 12 HEAD Open 0.3 0.101 22.5 • Overhead Sprinkler 5.6 22.9 225 16.7 16.1 12 HEAD Open 0.4 0.102 22.5 • Overhead Sprinkler 5.6 23.9 225 18.3 16.1 12 HEAD Open 1.4 0.106 22.5 B7 Overhead Sprinkler 5.6 24 225 18.3 16.1 12 HEAD Open 1.5 0.107 -6.5 22.5 • B9 Overhead Sprinkler 5.618.6 16.1 12 HEAD Open I I -6.5 22.5 003 Node 16.1 12 NODE -6.5 016 Node 33.7 12 NODE -6.5 015 Node 33.9 12 NODE -6.5 011 Node 113 5 -6.5 12NODE 185 Node 94.9 -3 NODE 0 186-0 Node 95 -3 NODE 0 186-I Node 95.1 -3 NODE 0 188-0 Node 95.4 NODE 188-1 Node 99.3 - NODE W1 Supply -208 99.5 -3 SUPPLY 0 File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 17 Job:DURHAM EDUCATION CENTER Hydraulic Calculations 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/psi1/2) (gpm) (in) (ft) (ft) (psi) (psi) Path No: 1 B2 12 5.6 22.5 1.25 13 120 16.1 B5 12 5.6 21.3 1.442 0 0.031 0 13 0.4 B5 12 5.6 22.8 1.25 14.5 120 16.5 B8 12 5.6 44.1 1.442 0 0.1191 0 • 14.5 1.7 B8 12 5.6 23.9 1.25 lx(us.Tee-Br)=7.43 43.87 120 18.3 015 12 68 1.442 2x(us.90)=7.43 14.86 0.2658 0 58.74 15.6 015 12 68.7 2.5 22.52 120 33.9 011 12 136.8 2.635 0 0.0514 0 22.52 1.2 011 12 71.2 2.5 12x(us.90)=98.85 295.66 120 35 185 -3 208 2.635 5x(us.Tee-Br)=82.37 181.22 0.1118 6.5 476.87 53.3 185 -3 0 4 lx(coupling)=1.83 14.38 140 94.9 186-0 -3 208 4.3 1.83 0.0077 0 16.21 0.1 186-0 -3 0 4 0.17 0 95 BFV-N 186-I -3 208 0 0 0.7138 0 *** 0.17 0.1 186-I -3 0 4 lx(coupling)=1.83 24.46 140 95.1 188-0 -3 208 4.3 lx(us.90)=18.33 20.16 0.0077 0 44.62 0.3 188-0 -3 0 4 2.81 0 95.4 AmesC300H 188-I -3 208 0 0 1.3799 0 *** 2.81 3.9 188-I -3 0 4 18.18 140 99.3 W1 -3 208 4.3 0 0.0077 0 18.18 0.1 W1 99.5 Path No: 2 B2 12 5.6 22.5 1.25 1x(us.Tee-Br)=7.43 1 120 16.1 003 12 1.2 1.442 7.43 0.0001 0 8.43 0 ! _ 003 12 0.5 1.25 lx(us.Tee-Br)=7.43 15 120 16.1 B3 12 5.6 1.7 1.442 7.43 0.0003 0 22.43 0 B3 12 5.6 22.5 1.25 13 120 16.2 B6 12 5.6 24.2 1.442 0 0.0393 0 13 0.5 __ B6 12 5.6 22.9 1.25 14.5 120 16.7 B9 12 5.6 47.1 1.442 0 0.1344 0 14.5 1.9 _ B9 12 5.6 24.2 1.25 1x(us.Tee-Br)=7.43 41.91 120 18.6 011 12 71.2 1.442 2x(us.90)=7.43 14.86 0.2894 0 56.78 16.4 011 35 File:C:\Users\Admin\DesktopUobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 18 Job:DURHAM EDUCATION CENTER Hydraulic Calculations 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/psi1/2) (gpm) (in) (ft) (ft) (psi) (Psi) Path No: 3 B1 12 5.6 22.5 1.25 13 120 16.1 B4 12 5.6 22 1.442 0 0.0327 0 13 0.4 B4 12 5.6 22.8 1.25 14.5 120 16.6 B7 12 5.6 44.8 1.442 0 0.1224 0 14.5 1.8 B7 12 5.6 24 1.25 lx(us.Tee-Br)=7.43 41.87 120 18.3 016 12 68.7 1.442 2x(us.90)=7.43 14.86 0.2709 0 56.74 15.4 016 12 0 2.5 12 120 33.7 015 12 68.7 2.635 0 0.0144 0 12 0.2 015 33.9 Path No: 4 B1 12 5.6 22.5 1.25 lx(us.Tee-Br)=7.43 15 120 16.1 003 12 0.5 1.442 7.43 0.0000 0 22.43 0 003 16.1 * Pressures are balanced to a high degree of accuracy. Values may vary by 0.1 psi due to display rounding. * Maximum Velocity of 14 ft/s occurs in the following pipe(s): (011-B9) *** Device pressure loss (gain in the case of pumps) is calculated from the device's curve. If the device curve is printed with this report, it will appear below. The length of the device as shown in the table above comes from the CAD drawing. The friction loss per unit of length is calculated based upon the length and the curve-based loss/gain value. Internal ID and C Factor values are irrelevant as the device is not represented as an addition to any pipe, but is an individual item whose loss/gain is based solely on the curve data. File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 19 L Job:DURHAM EDUCATION CENTER Device Graphs Pressure vs. Flow Function Design Area: 2 Supply Ref.: ; Supply N .Wl I1 i a - 1 _._ _ I 90-E i I I I. i „ , ., , , ,, „„ _,,, ,,,,, , , 1 , , -.,• ' 1..5. - II. - -F.-- ' I ' _ : ..__ _4 til 1 ! E ;. 7C 7 3 E __... _....._. ...,...m..._.� �. _.. .� .......__.. a ..� _.,,, ..{ ............�................_.... .._,w _ .. 1t1L t 7 ice+ O Q Q. C. O L1^ G 4 G O Q o co py 75 O 't Q 4n O 4^o- 0 vl k !5 N.. rn ?+Y ,t, ,�'n.. 4�5 try' 40 IOW, gPm Pressure Loss Function Design Area: 2; BFP Rif.: 3% (Ames ,�H, Size=4); inlet Node: 1$*+ I;Outlet Node: 188-0 1 —: a. i. g 1.13.::: i f. f 115_37: -.I-.. ..... _ _.,_ . __ ,_ __._ __, I ISS=—. 13_R 121.:, „.._._ .._ �. ... ____........_.:.1 ..�' M. 111: 4 <. I. 10j t - i i 3.9 psi gp 3..8.;_ _......__._...... .. .. _....., w- .. _ s 3 .___._.......-A- -_.. l i , , I— f 3 E 4 Mt CrS 4 mr 4: 4: 4.: 4 4. 4. 4: Flow,awn File:C:\Users'Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 20 A Jbb:DURHAM EDUCATION CENTER Device Graphs Pressure Leas Function Design Area2; Valve Ref.: 395(BFV N, Size- 4); Inlet Node: 186-I; Outlet Node: 1: 4428 3.42 -____ �_ .. . ____ �___ w .. ,_ ra - as 422- --- — _ f i _� �_m_, __ _ L__ _�. 2 z 4 I i 1- 042s- 0.1 psi gpm 1 t _. - . 4., cu. rte, :0.. re, a F ows aPni File:C:\Users\Admin\Desktop\Jobs\Durham Educ.Center\Calc's\Hydraulic\CALC.dwg Date 4/30/2018 Copyright©2002-2012 Tyco Fire Protection Products Page 21