The coupling between the mass transfer flux and adsorption rates of all components in an adsorptive distillation process was analyzed according to non equilibrium thermodynamics.
利用非平衡热力学原理，对吸附蒸馏过程中各个热力学传输流之间的耦合进行了理论分析。
2
Therefore, this model is applicable to the phase equilibrium and distillation calculation of systems containing acetic acid.
因此，本模型可用于含醋酸物系的相平衡和精馏计算。
3
ASPEN software was chosen to simulate and predict the temperature, concentration and other profiles of the catalytic distillation column by equilibrium stage mode.