Datos Equilibrioa Cetona Agua T=307.8ºC y P=0.71 atm
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VAPOR LIQUID Datos obtenidos utilizando Aspe MOLEFRAC MOLEFRAC ACETO-01 ACETO-01 gas liq 1 1 salida 0.00326666 0.140625 0.9877855 0.975 entrada 0.00335427 0 0.9766856 0.95 0.9665865 0.925 0.9573884 0.9 0.9490042 0.875 0.9413565 0.85 0.9343769 0.825 0.9280041 0.8 0.9221831 0.775 0.916864 0.75 0.9120014 0.725 0.9075534 0.7 0.9034814 0.675 0.899749 0.65 0.8963217 0.625 0.8931663 0.6 0.8902505 0.575 0.887542 0.55 0.8850082 0.525 0.8826154 0.5 0.8803279 0.475 0.8781068 0.45 0.8759093 0.425 0.8736862 0.4 0.87138 0.375 0.8689219 0.35 0.8662269 0.325 0.8631872 0.3 0.8596623 0.275 0.8554637 0.25 0.8503292 0.225 0.843881 0.2 0.83555 0.175 0.824433 0.15 0.8089986 0.125 0.786419 0.1 0.7508141 0.075 0.6875895 0.05 0.547724 0.025 0 0
description
en el presente documento se muestran las concentraciones de equilibrio (curva de equilibrio)para el sistema acetona agua a T=307.8ºC ,P=0.71 atm, obtenidos usando software de simulacion
Transcript of Datos Equilibrioa Cetona Agua T=307.8ºC y P=0.71 atm
Hoja1VAPORLIQUIDDatos obtenidos utilizando Aspen, y el modelo termodinamico NTRL a T=307,8 y P =0,71 atmMOLEFRACMOLEFRACACETO-01ACETO-01 gasliq11salida0.00326666020.1406250.98778550.975entrada0.003354265400.97668560.950.96658650.9250.95738840.90.94900420.8750.94135650.850.93437690.8250.92800410.80.92218310.7750.9168640.750.91200140.7250.90755340.70.90348140.6750.8997490.650.89632170.6250.89316630.60.89025050.5750.8875420.550.88500820.5250.88261540.50.88032790.4750.87810680.450.87590930.4250.87368620.40.871380.3750.86892190.350.86622690.3250.86318720.30.85966230.2750.85546370.250.85032920.2250.8438810.20.835550.1750.8244330.150.80899860.1250.7864190.10.75081410.0750.68758950.050.5477240.02500
