The prospect of strict equilibrium-stage distillation operating algorithm is introduced in this article.
介绍了严格的平衡级精馏模拟操作型算法的研究进展。
The non-equilibrium stage model is used to simulate catalytic distillation process for cumene synthesis using low concentration propylene and benzene.
对苯与低浓度丙烯合成异丙苯的催化精馏过程建立非平衡级模型。
ASPEN software was chosen to simulate and predict the temperature, concentration and other profiles of the catalytic distillation column by equilibrium stage mode.
以动力学模型为基础，借助A SPEN软件用平衡级模型进行了催化精馏过程的模拟与预测。
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