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Home My WebLink AboutB23-2219 040-120-036 Fire Hydrant Pipe Line Calculations 062923 (2) O pip rL D U®' ^ ' r--c1 taking the pressure out of fluid flow calculations V(� Find Pressure Drop SEGMENT A - C Inoutr Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch paFE o "s+onct: Internal Diameter 8.00 inch ,� +/ Length 844.00 ft : Elevation Change -15.80 ft ,� .1689 Fluid Water I i / p, 1' • /24 Temperature 20.0 'C / ; CIO, le 411 Density 998.000000 kg/m3 �'�FOFcpa,�F Viscosity 1.002000 Centipoise 1 Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec APPL'�'S TO Pr4195 I 7fiR & za Results Flow Type Turbulent Reynolds Number 275619 Friction Factor 0.014946 Fluid Velocity 1.36 m/sec Friction Loss 2.539737 psi Fittings Loss 0.412065 psi Total Entry Loss 0.412065 psi Total Entry K 3.07 8"x 1 (K= 0.11 x 1) 1.1 8"x 3 (K= 0.84 x 3) lip 8"x2 (K= 0.22x2) Elevation Loss -6.836035 psi Pressure Drop -3.884234 psi 0 taking the pressure out of fluid flow calculations Find Flow SEGMENT A - C innut Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 844.00 ft Elevation Change -15.80 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss -3.880000 psi Flow Type Turbulent Reynolds Number 275969 Friction Factor 0.014943 Fluid Velocity 1.36 m/sec Friction Loss 2.545615 psi Fittings Loss 0.410420 psi Total Entry Loss 0.410420 psi Total Entry K 3.05 8"x2 (K= 0.21 x 2) [� 8"x 1 (K= 0.11 x 1) Lj1J 8" x 3 (K= 0.84 x 3) Elevation Loss -6.836035 psi Volume Flow 700.8886 US gpm Mass Flow 97.2917 lb/sec Pay e 2 0 c zo 0 taking the pressure out of fluid flow calculations hind Pressure Drop SEGMENT C - D 'gout- Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 285.00 ft Elevation Change 0.00 ft Fluid Water Temperature 20.0 'C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Results Flow Type Turbulent Reynolds Number 275619 Friction Factor 0.014946 Fluid Velocity 1.36 m/sec Friction Loss 0.857613 psi Fittings Loss 0.112747 psi Total Entry Loss 0.112747 psi Total Entry K 0.84 4.1 8" x1 (K= 0.84x1) Elevation Loss 0.000000 psi Pressure Drop 0.970360 psi pie, 3 I Doi® ir-c1 taking the pressure out of fluid flow calculations V V(a Find How SEGMENT C - D input Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 285.00 ft Elevation Change 0.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 0.970000 psi Results Flow Type Turbulent Reynolds Number 275564 Friction Factor 0.014947 Fluid Velocity 1.36 m/sec Friction Loss 0.857298 psi Fittings Loss 0.112702 psi Total Entry Loss 0.112702 psi Total Entry K 0.84 L1 8"x1 (K= 0.84x1) Elevation Loss 0.000000 psi Volume Flow 699.8591 US gpm Mass Flow 97.1488 lb/sec taking the pressure out of fluid flow calculations V V I rind Pressure Drop SEGMENT D - E input' Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change 2.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Hesults Flow Type Turbulent Reynolds Number 275619 Friction Factor 0.014946 Fluid Velocity 1.36 m/sec Friction Loss 0.601833 psi Fittings Loss 0.112747 psi Total Entry Loss 0.112747 psi Total Entry K 0.84 4.1 8" x1 (K= 0.84x1) Elevation Loss 0.865321 psi Pressure Drop 1.579902 psi P4ye (5a2v pip '.ODU° r-I taking the pressure out of fluid flow calculations v V I Find How SEGMENT D - E 'nputs Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change 2.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 1.570000 psi Results Flow Type Turbulent Reynolds Number 273548 Friction Factor 0.014966 Fluid Velocity 1.35 m/sec Friction Loss 0.593620 psi Fittings Loss 0.111059 psi Total Entry Loss 0.111059 psi Total Entry K 0.84 Izl 8" x1 (K= 0.84x1) Elevation Loss 0.865321 psi Volume Flow 694.7407 US gpm Mass Flow 96.4383 lb/sec > fifes DLJ° taking the pressure out of fluid flow calculations �) Find Pressure Drop SEGMENT E - F Inputs Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change 0.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Flow Type Turbulent Reynolds Number 275619 Friction Factor 0.014946 Fluid Velocity 1.36 m/sec Friction Loss 0.601833 psi Fittings Loss 0.112747 psi Total Entry Loss 0.112747 psi Total Entry K 0.84 Q 8"x1 (K= 0.84 x 1) Elevation Loss 0.000000 psi Pressure Drop 0.714581 psi (/) e- egg. zd PIED La_I taking the pressure out of fluid flow calculations V V I Find Flow SEGMENT E - F 'nnut° Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change 0.00 ft Fluid Water Temperature 20.0 'C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 0.710000 psi Results Flow Type Turbulent Reynolds Number 274663 Friction Factor 0.014955 Fluid Velocity 1.36 m/sec Friction Loss 0.598034 psi Fittings Loss 0.111966 psi Total Entry Loss 0.111966 psi Total Entry K 0.84 14 8" x1 (K= 0.84x1) Elevation Loss 0.000000 psi Volume Flow 697.5712 US gpm Mass Flow 96.8312 lb/sec 0 taking the pressure out of fluid flow calculations W I Find Pressure Drop SEGMENT F - G innluv Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change -1.00 ft Fluid Water Temperature 20.0 �C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Results Flow Type Turbulent Reynolds Number 275619 Friction Factor 0.014946 Fluid Velocity 1.36 m/sec Friction Loss 0.601833 psi Fittings Loss 0.112747 psi Total Entry Loss 0.112747 psi Total Entry K 0.84 EJ 8" x1 (K= 0.84x1) Elevation Loss -0.432660 psi Pressure Drop 0.281920 psi PeA9 e-l oC-z d taking the pressure out of fluid flow calculations V V I Find Flow SEGMENT F - G 'nnut' Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 8 inch Internal Diameter 8.00 inch Length 200.00 ft Elevation Change -1.00 ft Fluid Water Temperature 20.0 'C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 0.280000 psi Results Flow Type Turbulent Reynolds Number 275218 Friction Factor 0.014950 Fluid Velocity 1.36 m/sec Friction Loss 0.600241 psi Fittings Loss 0.112420 psi Total Entry Loss 0.112420 psi Total Entry K 0.84 4J 8" x1 (K= 0.84x1) Elevation Loss -0.432660 psi Volume Flow 698.9827 US gpm Mass Flow 97.0271 lb/sec Pam- e Zo oC o pip -EL_ it A . taking the pressure out of fluid flow calculations Find Pressure Drop SEGMENT G H Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 200.00 ft Elevation Change -1.50 ft Fluid Water Temperature 20.0 "C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Flow Type Turbulent Reynolds Number 367492 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 2.428011 psi Fittings Loss 0.050905 psi Total Entry Loss 0.050905 psi Total Entry K 0.12 E1 6"x1 (K= 0.12x1) Elevation Loss -0.648991 psi Pressure Drop 1.829926 psi taking pressure the out of fluid flow calculations Find Flow SEGMENT G - H 'nnUtr Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 200.00 ft Elevation Change -1.50 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 1.830000 psi Results Flow Type Turbulent Reynolds Number 367498 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 2.428084 psi Fittings Loss 0.050907 psi Total Entry Loss 0.050907 psi Total Entry K 0.12 [�] 6" x1 (K= 0.12x1) Elevation Loss -0.648991 psi Volume Flow 700.0114 US gpm Mass Flow 97.1699 lb/sec C taking the pressure out of fluid flow calculations Find Pressure Drop SEGMENT E - I input' Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 384.00 ft Elevation Change -7.50 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Results Flow Type Turbulent Reynolds Number 367492 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 4.661782 psi Fittings Loss 0.101811 psi Total Entry Loss 0.101811 psi Total Entry K 0.24 [1� 6"x 2 (K= 0.12 x 2) Elevation Loss -3.244954 psi Pressure Drop 1.518639 psi epc, ce__ 13er-C z6 o0 Lilj ' flowcalculationsI ��taking the pressure out of fluid SEGMENT E - I Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 384.00 ft Elevation Change -7.50 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 1.520000 psi Results Flow Type Turbulent Reynolds Number 367549 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 4.663111 psi Fittings Loss 0.101842 psi Total Entry Loss 0.101842 psi Total Entry K 0.24 [1._ 6" x 2 (K= 0.12 x 2) Elevation Loss -3.244954 psi Volume Flow 700.1088 US gpm Mass Flow 97.1834 lb/sec it nig taking the pressure out of fluid flow calculations Find Pressure Drop SEGMENT E - J !pouts Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 432.00 ft Elevation Change 5.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Hesults Flow Type Turbulent Reynolds Number 367492 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 5.244504 psi Fittings Loss 0.101811 psi Total Entry Loss 0.101811 psi Total Entry K 0.24 jJ 6"x 2 (K= 0.12x 2) Elevation Loss 2.163302 psi Pressure Drop 7.509617 psi e 15 S—ZO taking thepressure outof fluid flow calculations v V 0 rd® to ng p essu e u d Find Flow SEGMENT E - J Inn1ir- Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 432.00 ft Elevation Change 5.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 7.510000 psi Results Flow Type Turbulent Reynolds Number 367506 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 5.244879 psi Fittings Loss 0.101819 psi Total Entry Loss 0.101819 psi Total Entry K 0.24 n 6"x 2 (K= 0.12 x 2) Elevation Loss 2.163302 psi Volume Flow 700.0273 US gpm Mass Flow 97.1721 lb/sec > pipit ° • taking the pressure out of fluid flow calculations Find Pressure Drop SEGMENT G - K InnUtr Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 384.00 ft Elevation Change -8.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Results Flow Type Turbulent Reynolds Number 367492 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 4.661782 psi Fittings Loss 0.101811 psi Total Entry Loss 0.101811 Total Entry K 0.24 [�] 6" x 2 (K= 0.12 x 2) Elevation Loss -3.461284 psi Pressure Drop 1.302309 psi > . taking the pressure out of fluid flow calculations Find Flow SEGMENT G - K Inout� Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 384.00 ft Elevation Change -8.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 1.300000 psi Results Flow Type Turbulent Reynolds Number 367395 Friction Factor 0.014310 Fluid Velocity 2.42 m/sec Friction Loss 4.659527 psi Fittings Loss 0.101757 psi Total Entry Loss 0.101757 psi Total Entry K 0.24 ['1� 6" x2 (K= 0.12x2) Elevation Loss -3.461284 psi Volume Flow 699.8155 US gpm Mass Flow 97.1427 lb/sec Pc4,e l6n - ao o pipB --nuti® taking the pressure out of fluid flow calculations W I Find Pressure Drop SEGMENT G - L 'nput� Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 342.00 ft Elevation Change 3.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Volume Flow 700.0000 US gpm Mass Flow 44.0748 kg/sec Hesults Flow Type Turbulent Reynolds Number 367492 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 4.151899 psi Fittings Loss 0.101811 psi Total Entry Loss 0.101811 psi Total Entry K 0.24 jJ 6"x 2 (K= 0.12 x 2) Elevation Loss 1.297981 psi Pressure Drop 5.551691 psi taking the pressure out of fluid flow calculations W(�Find Flow SEGMENT G - L 'nnUtp Method of Calculation Darcy-Weisbach Material PVC (ANSI) Schedule Sch. 40 Internal Roughness 0.000197 inch Nominal Size 6 inch Internal Diameter 6.00 inch Length 342.00 ft Elevation Change 3.00 ft Fluid Water Temperature 20.0 °C Density 998.000000 kg/m3 Viscosity 1.002000 Centipoise Pressure Loss 5.550000 psi Results Flow Type Turbulent Reynolds Number 367413 Friction Factor 0.014309 Fluid Velocity 2.42 m/sec Friction Loss 4.150252 psi Fittings Loss 0.101767 psi Total Entry Loss 0.101767 psi Total Entry K 0.24 [ti� 6" x 2 (K= 0.12 x 2) Elevation Loss 1.297981 psi Volume Flow 699.8486 US gpm Mass Flow 97.1473 lb/sec p� e zo 0,C z d y