BALANCE DE MATERIA - MP 40 ton

B%Tn/horaTORTA DE PRENSA100%10.68MIX%Tn/horaK%Tn/horaSlidos46.5%4.966100%18.101EVAPORACIN100%9.163Grasa4.5%0.481Slidos40.9%7.4Slidos0%0Hmedad49%5.234Grasa4.6%0.82Grasa0%0COCINADORPRENSAHmedad55%9.876Hmedad100%9.163

A%Tn/horaMATERIA PRIMA100%40J%Tn/horaSlidos18.5%7.4HARINA100%8.937G4.5%1.8C%Tn/horaMIXSECADORSlidos82.8%7.4Hmedad77%30.8LICOR DE PRENSA100%29.32D%Tn/horaGrasa9.2%0.822Slidos8.3%2.434SLIDOS100%3.351Hmedad8%0.715Grasa4.5%1.319Slidos30%1.005Hmedad87.2%25.566Grasa4.3%0.144Hmedad65.7%2.201

SEPARADORI%Tn/horaCONCENTRADO100%4.069Slidos35.1%1.428E%Tn/horaGrasa4.9%0.199LICOR100%25.969Hmedad60%2.441Slidos5.5%1.428G%Tn/horaGrasa4.5%1.169AGUA DE COLA100%25.06Hmedad90%23.372Slidos5.7%1.428Grasa0.8%0.200Hmedad93.5%23.429CENTRFUGAEVAPORADOR

F%Tn/horaH%Tn/horaACEITE100%0.911EVAPORACIN100%20.988Slidos0%0Slidos0%0Grasa100%0.911Grasa0%0Hmedad0%0Hmedad100%20.988

BALANCE DE ENERGA - EVAPORADORVAPOR SATURADODATOSTemperatura120CFlujo de CalorCp Agua (KJ/Kg-C)4.18393KQ = (Vapor * Hvapor + Aguadecola*Haguadecola + concentrado*Hconcentrado)Cp grasa (KJ/Kg-C)2.09Flujo msico939.42Kg/horaQ2065061.74588087KwCp slidos (KJ/Kg-C)3.4276Entalpa56013.71KJ/kgVAPOR HUMEDOQ = Vapor * (Hvapor - Hlquido) - prdidasCalor latente @ 120 C (KJ/Kg)2198.2202Cp vapor142.53KJ/Kg-kTemperatura60C939.42Kg/horaTemperatura de referencia (C)0333KPeso molecular del agua (Kg/kmol)18.01528Flujo msico939.4244243051Kg/horaEntalpa47187.80KJ/kgCp vapor141.71KJ/Kg-k%EVAPORADOR60 C%AGUA DE COLA100%25057.41Kg/horaCONCENTRADO100%4069.152Kg/horaSlidos5.7%1428.272Kg/horaSlidos35.1%1428.272Kg/horaGrasa0.8%200.459Kg/horaGrasa4.9%199.388Kg/horaAgua93.5%23428.676Kg/horaAgua60%2441.491Kg/horaTemperatura-40CTemperatura-60CEntalpa-164.816KJ/kgEntalpa-228.810KJ/Kg

VaporFlujo msico20988.256Kg/horaTemperatura60CFrmula CPCp = a + bT + cT^2 + dT^3KJ/Kmol-kEntalpa 251KJ/kga7.7b2.55E-04c7.78E-07d-1.47E-10