Novel hybrid reactive-extractive distillation for separation of tetrahydrofuran, ethanol, and water azeotropic system with rigorous side reactions consideration

被引:5
|
作者
Tsai, Chen-Cheng [1 ]
Kong, Zong Yang [2 ]
Yang, Ao [3 ]
Sunarso, Jaka [4 ]
Adi, Vincentius Surya Kurnia [1 ]
机构
[1] Natl Chung Hsing Univ, Dept Chem Engn, Taichung 40227, Taiwan
[2] Sunway Univ, Sch Engn & Technol, Dept Engn, Subang Jaya 47500, Selangor, Malaysia
[3] Chongqing Changyuan Grp Ltd, Chongqing 402460, Peoples R China
[4] Swinburne Univ Technol, Fac Engn Comp & Sci, Res Ctr Sustainable Technol, Kuching 93350, Sarawak, Malaysia
关键词
Reactive-extractive distillation; Ternary azeotropic mixture; Auxiliary reactions; Resource conservation; ETHYLENE-OXIDE; HEAT INTEGRATION; TERNARY MIXTURE; DESIGN; INTENSIFICATION; ENTRAINER;
D O I
10.1016/j.jwpe.2023.104478
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study builds upon our previous research work (Ind. Eng. Chem. Res. 2023, 62, 27, 10,601-10,610), which investigated the impact of considering the side reactions in the hybrid reactive-extractive distillation (RED). Our prior investigation revealed a significant challenge, as the inclusion of side reactions led to staggering spikes in energy consumption and total annual cost (TAC), seemingly rendering the performance of RED impractical. In this study, we present another possible scenario for considering side reactions in RED and highlight that RED with side reactions can still be a superior alternative to conventional distillation methods, even when side reactions are considered. This work was exemplified by using the recovering tetrahydrofuran (THF) and ethanol (EtOH) from waste effluent. We explore two different cases: Case 1 involves a side-reaction-free RED configuration reproduced as the base case, while the introduction of side reactions resulted in an increase in TAC by about 79.2% and a rise in total energy consumption by about 69%. Implementing a vacuum system (Case 2) substantially reduced the TAC by about 39% and energy consumption by about 20.5%. Although Case 2 outperformed Case 1 economically, it fell short of the base case due to additional capital costs. In contrast, Case 2 exhibited a lower TAC by 58% relative to the conventional pressure swing distillation.
引用
收藏
页数:9
相关论文
共 41 条
  • [31] Techno-economic comparison of energy usage between azeotropic distillation and hybrid system for water-ethanol separation
    Kunnakorn, D.
    Rirksomboon, T.
    Siemanond, K.
    Aungkavattana, R.
    Kuanchertchoo, N.
    Chuntanalerg, R.
    Hemra, K.
    Kulprathipanja, S.
    James, R. B.
    Wongkasemjit, S.
    RENEWABLE ENERGY, 2013, 51 : 310 - 316
  • [32] Heat integration and dynamic control of reactive pressure-swing distillation for separation of tetrahydrofuran/ethanol/water
    Xu, Qilei
    Liu, Xiaojing
    Sun, Defeng
    Shan, Baoming
    Cui, Peizhe
    Wang, Yinglong
    Zhang, Fangkun
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2023, 191
  • [33] Optimization of the composition of mixed entrainer for economic extractive distillation process in view of the separation of tetrahydrofuran/ethanol/water ternary azeotrope
    Zhao, Yongteng
    Zhao, Tingran
    Jia, Hui
    Li, Xin
    Zhu, Zhaoyou
    Wang, Yinglong
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2017, 92 (09) : 2433 - 2444
  • [34] Design and multi-objective optimization of novel side-stream reactive-extractive distillation process with intermediate reboiler for recovering ethanol and 1,4-dioxane from wastewater
    Rui, Qingqing
    Ye, Qing
    Li, Jinlong
    Wang, Yao
    Yu, Azhi
    SEPARATION AND PURIFICATION TECHNOLOGY, 2024, 334
  • [35] A vapor phase side stream intensified extractive distillation process for separation of azeotropic mixture 2, 2, 2-trifluoroethanol and water
    Xu, Dongmei
    Mu, Jinxing
    Sun, Hailin
    Tao, Sixuan
    Gao, Jun
    Zhang, Zhishan
    Zhang, Lianzheng
    Ma, Yixin
    Wang, Yinglong
    PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2024, 190 : 1164 - 1174
  • [36] Development of novel hybrid pre-separation/extractive reactive distillation processes for the separation of methanol/methyl acetate/ethyl acetate
    Zhu, Jiaxing
    Hao, Lin
    Zhu, Zhenxing
    Wei, Hongyuan
    SEPARATION AND PURIFICATION TECHNOLOGY, 2024, 348
  • [37] Control of extractive distillation processes with preconcentration for the separation of ternary azeotropic mixture ethyl acetate-ethanol-water in the face of multiple feed disturbances
    Wu, Tingyu
    Wang, Chao
    Zhuang, Yu
    Xu, Haohan
    Du, Jian
    SEPARATION AND PURIFICATION TECHNOLOGY, 2025, 354
  • [38] Design and eco-efficiency analysis of sustainable extractive distillation process combining preconcentration and solvent recovery functions for separating the tetrahydrofuran/ethanol/water ternary multi-azeotropic mixture
    Wang, Chao
    Zhuang, Yu
    Qin, Yutao
    Dong, Yachao
    Liu, Linlin
    Zhang, Lei
    Du, Jian
    PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2022, 159 : 795 - 808
  • [39] Multi-objective optimisation and energy-saving design of pressure-swing extractive distillation for separating ethanol/acetonitrile/water azeotropic system
    Sun, Qingbo
    Zhai, Jian
    Peng, Zekong
    Li, Jinwen
    Xie, Hongfei
    Liang, Hao
    Xu, Wendi
    Zhang, Jinqiang
    CHEMICAL ENGINEERING SCIENCE, 2025, 305
  • [40] Sustainable and efficient separation of ternary multi-azeotropic mixture butanone/ethanol/water based on the intensified reactive extractive distillation: process design, multi-objective optimization, and multi-criteria decision-making
    Li, Zongyao
    Huang, Xun
    Wang, Lanchi
    Chen, Yong
    Shi, Tao
    Shen, Weifeng
    SEPARATION AND PURIFICATION TECHNOLOGY, 2025, 355