Useful FormulasNPSH Net Positive Suction Head available (NPSHa) is the total suction head minus the vapor pressure (both expressed in feet absolute) at the pump suction flange. NPSHa = 2.309(Pa - Pvp)/S.G. + or - He - Hf Pa is the atmospheric or tank pressure (psi absolute), Pvp is the vapor pressure (psi absolute), He is the elevation head (negative if suction lift) expressed in feet and Hf is the friction loss through the suction piping expressed in feet. HEAD psi = (14.50)(bar) psi = (.4912)(in. Hg) psi = (.4331)(ft)(S.G) in. Hg = (2.036)(psi) in. Hg = (.8819)(ft)(S.G.) 1 atm = 760 mm Hg 1 atm = 29.92 in. Hg ft = 2.309(psi)/S.G. ft = (1.134)(in. Hg)/S.G. CAPACITY GPM = (7.481)(Cu. ft./min.) GPM = (.2642)(Liter/min.) GPM = (264.2)(Cu. meter/min.) GPM = (4.403)(Cu. meter/hr.) HPM BHP = (GPM)(ft)(S.G.)/(3960)(E) KWinput = (GPM)(ft)(S.G.)/(5308)(E)(M.E.) E = pump efficiency M.E. = motor efficiency. HP = (1.341)(KW) KW = (.7457)(HP) HP = (lb. ft.)(RPM)/5250 TEMPERATURE deg. F = 9/5 (deg. C) + 32 deg. C = 5/9 (deg. F - 32) Heat added to fluid due to pump inefficiency. Total heat added per pass through pump LENGTH (mm) = (25.40)(inches)
meters = (.3048)(ft.) SPECIFIC GRAVITY Water = 1.0 S.G. = 62.43 lb./cu. ft. 1 gallon water = 8.3453 lb. 1 cu. ft. water = 7.48052 gal. VISCOSITY Centistokes = (centipoise)/Specific Gravity Above 50 centistokes, SSU = 4.55 (centistokes) If over 2500 SSU, a centrifugal pump smaller than 2-1/2" is impractical. If over 5000 SSU, any centrifugal pump is impractical. |