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Rational Method <br /> PipeNl T1 L1 V1 KS sol T2 L2 V2 K2 so2 Tc <br /> min eet eeUsec uniUess /h min eet eet/sec unidess Jt/h min <br /> 0.496904 lOD 33541G2 15 0.05 0.161421 44 4.542995 42 0.0117 0.658325 <br /> m n i A1 Cl A2 Q C avg A total Q <br /> uniNess uniUess in/hr acres unitless acres unitless unitless acres cJs <br /> 7.83 0.582 9.986875 013 0.9 017 0.25 0.549 0.5 2.741397 <br /> Pipe y2 T1 L1 V1 KS sol T2 L2 V2 K2 so2 Tc <br /> min eet eet/sec unidess /Jt min eet eet/sec unitless /h min <br /> 0.165635 60 6.037384 27 0.05 0.719151 209 4.843676 42 0.0133 0.884785 <br /> m n i AS Cl A2 C2 C avg A total Q <br /> unitless uniUess in/hr acres unitless acres unitless unitless oaes c/s <br /> 7.83 0.582 8.408182 034 0.9 0.05 0.25 0.816661 0.39 2.678006 <br /> Pipe"3 TS LI VS KS zo1 T2 L2 V2 K2 so2 Tc <br /> min feet feet/sec unitless ft/ft min feet feet/sec unitless h/h min <br /> 0.496904 100 3.354102 15 0.05 0.209055 a05 32.?8814 42 0.591 0.705959 <br /> m n i A1 CI A2 C2 Cavg Atotal Q <br /> unitless unitless in/hr acres unitl?ss acres unitless unitless acres cfs <br /> 7.83 0.562 9.588973 112 0.9 0.6 0.25 0.685711 1.82 11.96704 <br /> Pipe H4 Detention Outfall <br /> Q25= 0.22 Cf5 <br /> L= 65 h <br /> 5= 0.005 ft/h <br /> Pipe tt5 Detention Outfall <br /> 425= 0.156 cB i <br /> L= 57 (t <br /> S= 0.0175 ft/ft <br /> (LC•:FtR TO �aN�3�7 A - U Foz PIPC LOCArioaS • <br /> 2AT�o�n � Me'cri�o �X,eO TO pCTcer^�aE �s • ���c Coa.,�Yq.�cE <br /> �J(?AI.0 Fl-OW R. `�TE . G�E (=0��-OW�'JC-'� FIO�NAc�TE2 O��TPuT <br /> GuR capAc� *��' ,d--'� vC�oc.�Z-k CNEC.I.L . <br /> ('�-l 2 <br />