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。
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 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。
应用推荐