催化精馏过程模拟稳态模型的研究进展  

Progress in steady-state models for simulation of catalytic distillation process

作　　者：齐永君[1] 翁惠新[1] 

机构地区：[1]华东理工大学石油加工研究所,上海200237

出　　处：《化工进展》2010年第4期600-605,共6页Chemical Industry and Engineering Progress

摘　　要：对催化精馏过程模拟的平衡级模型、非平衡级模型和非平衡池模型3个常用的稳态模型及其求解方法进行了综述,并简要分析了各模型和求解方法的优缺点,讨论了催化精馏过程模拟的稳态模型及其求解方法未来的发展方向。Three commonly used steady-state models for catalytic distillation process and their algorithms are reviewed,including the equilibrium stage model,the non-equilibrium stage model and the non-equilibrium cell model.Advantages and disadvantages of each model and algorithm are summarized.Prospects for future development of steady-state models and their algorithms of catalytic distillation are also discussed.

关 键 词：催化精馏 模拟 平衡级模型 非平衡级模型 非平衡池模型 

分 类 号：TQ018[化学工程]