Ma Hongliao *, Chen Shaozhou and Bai Zilong. Simulation of Multicomponent Batch Distillation[J]. Journal of East China University of Science and Technology, 1999, (2): 205-208.
Citation:
Ma Hongliao *, Chen Shaozhou and Bai Zilong. Simulation of Multicomponent Batch Distillation[J]. Journal of East China University of Science and Technology, 1999, (2): 205-208.
Ma Hongliao *, Chen Shaozhou and Bai Zilong. Simulation of Multicomponent Batch Distillation[J]. Journal of East China University of Science and Technology, 1999, (2): 205-208.
Citation:
Ma Hongliao *, Chen Shaozhou and Bai Zilong. Simulation of Multicomponent Batch Distillation[J]. Journal of East China University of Science and Technology, 1999, (2): 205-208.
In this thesis,comparison among several equation of state has been carried out.Considering precision,time and universality,PR or SRK is selected to calculate the phase equilibrium constant of the mixture.A model has been developed to simulate the operation of multicomponent batch distillation with holdup by a plate to plate method,and has been programmed with FORTRAN.
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