高等学校化学学报 ›› 2004, Vol. 25 ›› Issue (5): 938.

• 研究论文 • 上一篇    下一篇

萃取精馏过程的非平衡态热力学分析

雷志刚, 李成岳, 陈标华   

  1. 北京化工大学可控化学反应科学与技术基础教育部重点实验室, 北京 100029
  • 收稿日期:2003-02-18 出版日期:2004-05-24 发布日期:2004-05-24
  • 通讯作者: 雷志刚(1973年生),男,博士,副教授,主要从事分离与反应工程研究.E-mail:leizhg@mail.buct.edu.cn E-mail:leizhg@mail.buct.edu.cn
  • 基金资助:

    中国石油化工集团公司科学技术研究开发项目(批准号:X501020)资助

Nonequilibrium Thermodynamic Analysis for Extractive Distillation Process

LEI Zhi-Gang, LI Cheng-Yue, CHEN Biao-Hua   

  1. The Key Laboratory of Science and Technology of Controllable Chemical Reactions, Ministry of Education, Beijing University of Chemical Technology, Beijing 100029
  • Received:2003-02-18 Online:2004-05-24 Published:2004-05-24

摘要: 对萃取精馏过程进行了非平衡热力学分析,提出了分离过程得以进行的判据.推导出了熵产生的数学表达式,并可将其用于萃取精馏过程的节能分析.此项研究结果只适用于萃取精馏板式塔,且在非平衡热力学的线性区域内

关键词: 萃取精馏, 非平衡热力学, 分离, 熵产生

Abstract: Nonequilibrium thermodynamic analysis for extractive distillation process was made. The separation criteria for implementing extractive distillation process were proposed, which will be theoretically helpful to the design of extractive distillation process. The mathematical equation of entropy generation, which can be used for energy-saving analysis, was deduced and verified to be reliable. The results presented in this work can only be applied to the tray distillation column and are in the linear range of nonequilibrium thermodynamics. Moreover, it is valuable for other special distillations with separating agent about why the process can be carried out.

Key words: Extractive distillation, Nonequilibrium thermodynamics, Separation, Entropy generation

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