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Local fire regulations specify that the pressure drop in a horizontal commercial steel pipe must not exceed 75 psi per 5

Posted: Mon May 16, 2022 6:13 am
by answerhappygod
Local Fire Regulations Specify That The Pressure Drop In A Horizontal Commercial Steel Pipe Must Not Exceed 75 Psi Per 5 1
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Local fire regulations specify that the pressure drop in a horizontal commercial steel pipe must not exceed 75 psi per 50 ft of pipe for flowrates up to 600 gal/min. If the water temperature is 50°F, what is the minimum allowable diameter pipe in inches? (1 ft = 7.48 gal)
Surface Tension, o (N/m) Speed of Sound", c Physical Properties of Water (SI Units)" Specific Density, Weight", Temperature Y (°C) (kg/m) (kN/m) 0 999.9 9.806 5 1000.0 9.807 10 999.7 9.804 20 998.2 9.789 30 995.7 9.765 40 992.2 9.731 50 988.1 9.690 60 983.2 9.642 70 977.8 9.589 80 971.8 9.530 90 965.3 9.467 100 958.4 9.399 Dynamic Viscosity, (N.$/m) 1.787 E-3 1.519 E-3 1.307 E-3 1.002 E-3 7.975 E-4 6.529 E-4 E-4 4.665 E-4 4.042 E-4 3.547 E-4 3.147 E - 4 2.818 E-4 Kinematic Viscosity, (m/s) 1.787 E-6 1.519 E-6 1.307 E-6 1.004 E-6 8.009 E-7 6.580 E-7 5.534 E-7 4.745 E-7 4.134 E-7 3.650 E - 7 3.260 E-7 2.940 E-7 7.56 E-2 7,49 E-2 7.42 E-2 7.28 E-2 7.12 E-2 6.96 E-2 6.79 E-2 6.62 E-2 6.44 E-2 6.26 E-2 6.08 E-2 5.89 E-2 Vapor Pressure, P. IN/m°(abs) 6.105 E + 2 8.722 E + 2 1.228 E +3 2.338 E + 3 4.243 E + 3 7.376 E + 3 1.233 E +4 1.992 E + 4 3.116 E + 4 4.734 E +4 7.010 E +4 1.013E+5 1403 1427 1447 1481 1507 1526 1541 1552 1555 1555 1550 1543 5.468
Dynamic Viscosity, Surface Tension, 6 (lb/ft) Vapor Pressure, P. [lb/in.(abs) Speed of Sound, c (ft/s) (1b/ne") Table B.1 Physical Properties of Water (BG/EE Units) Specific Density, Weight, Temperature 7 (°F) (slugs/ne) 32 1.940 62.42 40 1.940 62.43 50 1.940 62.41 60 1.938 62.37 70 1.936 62.30 80 1.934 62.22 90 1.931 62.11 100 1.927 62.00 120 1.918 61.71 140 1.908 61.38 160 1.896 61.00 180 1.883 60.58 200 1.869 60.12 212 1.860 59.83 3.732 E-5 3.228 E-5 2.730 E-5 2.344 E-5 2.037 E- 5 1.791 E- 5 1.500 E-5 1.423 E-5 1.164 E-5 9.743 E-6 8.315 E-6 7.207 E-6 6.342 E- 6 5.886 E- 6 Kinematic Viscosity, (t/s) 1.924 E-5 1.664 E-5 1.407 E-5 1.210 E-S 1.052 E-5 9.262 E-6 8.233 E-6 7.383 E-6 6.067 E-6 5.106 E-6 4.385 E-6 3.827 E-6 3.393 E- 6 3.165 E-6 5.18 E-3 5.13 E-3 5.09 E-3 5.03 E-3 4.97 E - 3 4.91 E - 3 4.86 E-3 4.79 E - 3 4.67 E-3 4.53 E- 3 4.40 E - 3 4.26 E - 3 4.12 E-3 4.04 E-3 8.854 E-2 1.217 E-1 1.781 E-1 2.563 E-1 3.631 E-1 5.069 E-1 6.979 E-1 9.493 E-1 1.692 E+O 2.888 E + 0 4.736 E+ 0 7.507 E +0 1.152 E+1 1.469E+1 4603 4672 4748 4814 4871 4819 4960 4995 5049 5091 5101 5195 5089 5062
0.1 0.00 Wholly furbow 0.08 Laminarflow QOS 00 Transition 004 03 0.0 0.03 0.015 0.04 001 OS 006 0.00 1 0.004 0.035 0.002 0.00 0001 0.000 0.0000 0.000 0.015 Table 8.1 Kvartegn for New Pipes I Mupted from Musly Reland Clerk (Ref. featluri பேதியாக, Mpe Millime R . C 0.001- Waw . 18 0.00 Calvin B.IS Call LES De . OS 0.000 Smooth 0.0001 100005 0.01 0.009! DO 0.00001 2110 2110) 2010 4 B 21101 4 5 8 2110) 10 10 10 15 Colebrook Eqn: €/D 2.51 = -2 log + 3.7 Rev