SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2023, Vol. 54 ›› Issue (2): 288-295.DOI: 10.1016/j.cjche.2022.04.019

• Full Length Article • 上一篇    下一篇

Reinforced temperature control of a reactive double dividing-wall distillation column

Wei Qin, Lijing Zang, Kejin Huang, Haisheng Chen, Yang Yuan, Xing Qian, Liang Zhang, Shaofeng Wang   

  1. College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, China
  • 收稿日期:2021-12-12 修回日期:2022-04-13 出版日期:2023-02-28 发布日期:2023-05-11
  • 通讯作者: Kejin Huang,E-mail:huangkj@mail.buct.edu.cn
  • 基金资助:
    We acknowledge the financial support from National Natural Science Foundation of China (21878011).

Reinforced temperature control of a reactive double dividing-wall distillation column

Wei Qin, Lijing Zang, Kejin Huang, Haisheng Chen, Yang Yuan, Xing Qian, Liang Zhang, Shaofeng Wang   

  1. College of Information Science and Technology, Beijing University of Chemical Technology, Beijing 100029, China
  • Received:2021-12-12 Revised:2022-04-13 Online:2023-02-28 Published:2023-05-11
  • Contact: Kejin Huang,E-mail:huangkj@mail.buct.edu.cn
  • Supported by:
    We acknowledge the financial support from National Natural Science Foundation of China (21878011).

摘要: The mass and thermal coupling makes the control of the reactive double dividing-wall distillation column (R-DDWDC) an especially challenging issue with a highly interactive nature. With reference to the separation of an ideal endothermic quaternary reversible reaction with the most unfavorable ranking of relative volatilities (A + B ⇋ C + D with αA > αC > αD > αB), the operation rationality of the R-DDWDC is studied in this contribution. The four-point single temperature control system leads to great steady-state discrepancies in the compositions of products C and D and the reason stems essentially from the failure in keeping strictly the stoichiometric ratio between reactants A and B. A temperature plus temperature cascade control scheme is then employed to reinforce the stoichiometric ratio control and helps to secure a substantial abatement in the steady-state discrepancies. A temperature difference plus temperature cascade control scheme is finally synthesized and leads even to better performance than the most effective double temperature difference control scheme. These outcomes reveal not only the operation feasibility of the R-DDWDC but also the general significance of the proposed temperature difference plus temperature cascade control scheme to the inferential control of any other complicated distillation columns.

关键词: Reactive double dividing-wall distillation column, Temperature control, Temperature plus temperature cascade control, Temperature difference plus temperature cascade control, Process operation

Abstract: The mass and thermal coupling makes the control of the reactive double dividing-wall distillation column (R-DDWDC) an especially challenging issue with a highly interactive nature. With reference to the separation of an ideal endothermic quaternary reversible reaction with the most unfavorable ranking of relative volatilities (A + B ⇋ C + D with αA > αC > αD > αB), the operation rationality of the R-DDWDC is studied in this contribution. The four-point single temperature control system leads to great steady-state discrepancies in the compositions of products C and D and the reason stems essentially from the failure in keeping strictly the stoichiometric ratio between reactants A and B. A temperature plus temperature cascade control scheme is then employed to reinforce the stoichiometric ratio control and helps to secure a substantial abatement in the steady-state discrepancies. A temperature difference plus temperature cascade control scheme is finally synthesized and leads even to better performance than the most effective double temperature difference control scheme. These outcomes reveal not only the operation feasibility of the R-DDWDC but also the general significance of the proposed temperature difference plus temperature cascade control scheme to the inferential control of any other complicated distillation columns.

Key words: Reactive double dividing-wall distillation column, Temperature control, Temperature plus temperature cascade control, Temperature difference plus temperature cascade control, Process operation