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• <br />N <br />NU MBER SETS = ML +1 = ( ) +l = sets per field <br />Sin ( 60 ) <br />Use multiples of 60ft. Note this lenght may be shorter if 60 ft swing lines are used. <br />MAINLINE CAPACITY <br />(Manifold) <br />MAINLINE CAP.= ( #HEAD REQ'D (15)) X (NOZZLE FLOW (GPM) {l61) <br />X ( #SIDEROLLS {15al) <br />_ ( )X( )X( ) <br />GPM = GPM = CFS <br />TOTAL SIDEROLL PRESSURE REQURIED: <br />• TOTAL PRESSURE REQUIRED = MPS + (SWING LINE LOSS + RISER, <br />HYDRANT AND STUB VALVE <br />LOSS) <br />_( ) +( 2psi } <br />Total = ( ) psi req. at beginning of sideroll riser (22) <br />.Main Line Head Loss per 100ft. <br />;+ siderolls (15a)= <br />gpm per sideroll (20a) = gpm <br />Mainline material & Diameter <br />Length of Mainline Pipe <br />Elazen Williams "C" factor <br />Friction Loss ft; 100 (chart) <br />(21) <br />(L) <br />(2`I) <br />