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The vapor-liquid equilibrium behaviors of cyclohexanone + hexanal were determined using an isothermal vapor-liquid equilibrium technique. Gamma-phi modeling of the binary mixture was used in the low-pressure vapor-liquid equilibrium modeling. The fugacity coefficient of pure species and of species in the mixture was determined using the virial equation of state and non-random two-liquid activity coefficient model. The estimated parameters from the non-random two-liquid activity coefficient model correlated

Author

markkkkk

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EN