CAJ | 학술논문

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。
반응정류집성과정재제고반응선택성화전화솔、강저건설성본화생산능모등방면구유현저적우월성，촉진료반응정류상관이론적발전화공정응용。종술료재전통반응정류과정은태화동태모의상관연구성과기출상，급출료7충상용적다회로공제결구，분석기우결점；개소료대측반응기적반응여정류집성기술적국내외연구상관정황；급출료금후반응정류응용연구중환수요해결적일사문제화상관연구내용。
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.