反应精馏模拟与控制研究进展  

Research Development on Reactive Distillation Simulation and Control

作　　者：薄翠梅[1,2] 柏杨进[1] 李芳芳[1] 丁良辉[2] 乔旭[2] 

机构地区：[1]南京工业大学自动化与电气工程学院,南京211816 [2]南京工业大学化学与化工学院,南京211816

出　　处：《石油化工自动化》2012年第2期1-6,共6页Automation in Petro-chemical Industry

基　　金：中国博士后科学基金项目(20100471325);江苏省博士后基金项目(0901011B);江苏省自然科学基金(BK2011795);江苏省六大人才高峰计划

摘　　要：反应精馏集成过程在提高反应选择性和转化率、降低建设成本和生产能耗等方面具有显著的优越性,促进了反应精馏相关理论的发展和工程应用。综述了在传统反应精馏过程稳态和动态模拟相关研究成果基础上,给出了7种常用的多回路控制结构,分析其优缺点;介绍了带侧反应器的反应与精馏集成技术的国内外研究相关情况;给出了今后反应精馏应用研究中还需要解决的一些问题和相关研究内容。Integration process of reactive distillation technologies have notable advantages on increasing reaction selectivity and conversion, reducing construction cost and energy consumption production, etc. , and have promoted the development of theory and engineering application. The research progress of static and dynamic simulation for the traditional reactive distillation process is firstly summarized, seven kinds of common multi-loop control structure are described, and their advantages and disadvantages are evaluated. The latest research situation at domestic and off-shore integrated reactive distillation technologies with side reactor is introduced. Some issues to be solved and related research contents for the application are put forward.

关 键 词：反应精馏 数学模型 动态模拟 自动控制 侧反应精馏 

分 类 号：TQ018[化学工程] TP273[自动化与计算机技术—检测技术与自动化装置]