Dehydration of Isopropanol: A Comparative Review of Distillation Processes, Heat Integration, and Intensification Techniques

被引:6
作者
Nhien, Le Cao [1 ]
Agarwal, Neha [1 ]
Lee, Moonyong [1 ]
机构
[1] Yeungnam Univ, Sch Chem Engn, Gyeongbuk 38541, South Korea
关键词
isopropyl alcohol; heat integration; process intensification; heterogeneous azeotrope distillation; extractive distillation; pressure swing distillation; LIQUID-LIQUID EQUILIBRIA; ALCOHOL PLUS WATER; EXTRACTIVE DISTILLATION; AZEOTROPIC DISTILLATION; VAPOR-LIQUID; DIMETHYL-SULFOXIDE; DESIGN; COLUMN; SYSTEMS; OPTIMIZATION;
D O I
10.3390/en16165934
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The dehydration of isopropanol (IPA) is a crucial process in numerous industries, and the optimization of its efficiency and economic viability is essential. This review provides a comprehensive analysis and comparison of various distillation processes, heat integration (HI) strategies, and process intensification (PI) techniques employed for IPA dehydration. The advantages, limitations, and applicability of distillation processes, such as extractive distillation, heterogeneous azeotropic distillation, and pressure swing distillation, are discussed. In addition, this review explores the potential of HI techniques to optimize energy consumption and reduce operating costs of IPA dehydration processes. PI techniques, including thermally coupled arrangements and dividing wall columns, are examined for their ability to improve the process efficiency and sustainability. It is crucial to conduct thorough evaluations, as well as energy and economic analyses, when choosing the appropriate distillation process, HI approach, and PI technique for specific IPA dehydration applications. This review emphasizes the potential for improving the energy efficiency, product purity, and cost-effectiveness of IPA dehydration through the integration of advanced distillation processes and PI techniques.
引用
收藏
页数:25
相关论文
共 55 条
  • [51] Optimal design of mixed acid esterification and isopropanol dehydration systems via incorporation of dividing-wall columns
    Wang, San-Jang
    Chen, Wun-Yu
    Chang, Wen-Teng
    Hu, Chi-Chih
    Cheng, Shueh-Hen
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 85 : 108 - 124
  • [52] Azeotropic distillation
    Widagdo, S
    Seider, WD
    [J]. AICHE JOURNAL, 1996, 42 (01) : 96 - 130
  • [53] Comparison of Energy Consumption of Two-Column Configuration and Three-Column Configuration in the Extractive Distillation Process for High Purity Refinement of Isopropyl Alcohol
    Wu, Xuefei
    Nho, Jaehyun
    Kim, Dong Sun
    Cho, Jungho
    [J]. ASIAN JOURNAL OF CHEMISTRY, 2014, 26 (16) : 5223 - 5229
  • [54] Critical Assessment of the Energy-Saving Potential of an Extractive Dividing-Wall Column
    Wu, Yi Chang
    Hsu, Paul Hen-Chia
    Chien, I-Lung
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (15) : 5384 - 5399
  • [55] Economically and thermodynamically efficient pressure-swing distillation with heat integration and heat pump techniques
    Zhai, Jian
    Chen, Xin
    Sun, Xiaoqing
    Xie, Hongfei
    [J]. APPLIED THERMAL ENGINEERING, 2023, 218