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

Datos Equilibrioa Cetona Agua T=307.8ºC y P=0.71 atm

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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

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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