datos equilibrioa cetona agua t=307.8ºc y p=0.71 atm

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

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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

INTOXICACION POR CETONA

ARTROPLASTIA ATM