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• <br />• • <br />Full Pipe Flow Under Gravity Worksheet <br />Tertlary Pipes <br />Project: CC3V (Section C) <br />Date: January 2008 <br />~': Dolezal 1.49 ~~~~ '/ <br />Project #: 1125 Q - _ ~ 73 S' JZ <br />n <br />(ftfft): 0.27 <br />ngs "n": 0.015 <br />ar P/pe Flow <br />Q = 9Pm <br />n = Mannings CoetT. <br />A =Flow Area <br />R = Hyd. Radius <br />S = Pi Slo <br />SMITH wilLtAMS CONSUITANTi, INC. <br />--Zubic <br />Inside Diameter inches Ares Ft"2 d. iZad us R. Q m Cr cfs s Q ems meterlhr ~ <br />2.00 0.02 0.04 61 0.14 3.8 0.00 13.8 <br />4.00 0.09 0.08 386 0.86 24.3 0.02 87.6 <br />8.00 0.20 0.13 1137 2.53 71.7 0.07 258.2 <br />8.00 0.35 0.17 2,449 5.48 154.5 0.15 556.1 <br />10.00 0.55 0.21 4,440 9.89 280.1 0.28 1008.4 <br />12.00 0.79 0.25 7,220 16.09 455.5 0.46 1639.7 <br />14.00 1.07 0.29 10,891 24.27 687.0 0.69 2473.4 <br />16.00 1.40 0.33 15549 34.65 980.9 0.98 3531.3 <br />18.00 1.77 0.38 21287 47.43 1342.9 1.34 4834.4 <br />20.00 2.18 0.42 28193 62.82 1778.5 1.78 6402.7 <br />22.00 2.84 0.46 38,352 81.00 2293.2 2.29 8255.4 <br />Horizontal Deflection <br />ihape Plpe Flow • •"~ ~~~~~~~~~~~' <br />Pfpe Deflection (%): 0 --~ <br />Vertical Deflection <br />tel Deflection (%): 0 <br />orizon _ e~'ir meter _-_. <br />Clcular Pi LD. inches VerHeat Axis In. In. Area Ft"2 full flow d. Radius D cfs <br />2.00 2.0 2.0 0.02 0.52 0.04 0.14 60.7 <br />4.00 4.0 4.0 0.09 1.05 0.08 0.86 385.7 <br />8.00 6.0 6.0 0.20 1.57 0.13 2.53 1137.1 <br />6.00 8.D 8.0 0.35 2.09 0.17 5.48 2448.9 <br />10.00 10.0 10.0 0.55 2.82 0.21 9.89 4440.1 <br />12.00 t 2.0 12.0 0.79 3.14 0.25 16.09 7220.2 <br />14.00 14.0 14.0 1.07 3.67 0.29 24.27 10891.1 <br />16.00 16.0 16.0 1.40 4.19 0.33 34.65 15549.5 <br />18.00 18.0 16.0 1.77 4.71 0.38 47.43 21287.4 <br />20.00 20.0 20.0 2.18 5.24 0.42 82.82 28193.1 <br />