A new metric for the evaluation and selection of energy-intensified extractive distillation sequences

被引:8
作者
Chien, Chih-Kuan [1 ]
Ward, Jeffrey D. [1 ]
机构
[1] Natl Taiwan Univ, Dept Chem Engn, Taipei 10607, Taiwan
关键词
Extractive distillation; Heat integration; Side streams; Thermal coupling; Dividing -wall column; PRESSURE-SWING DISTILLATION; DIVIDING-WALL COLUMN; DESIGN; EFFICIENT; OPTIMIZATION; SEPARATION; EQUILIBRIA; SIMULATION; SOLVENT; SYSTEM;
D O I
10.1016/j.seppur.2023.124165
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Extractive distillation is a widely-used but energy-intensive method for separating homogeneous azeotropic mixtures into pure components. Numerous design alternatives have been proposed for reducing energy consumption in such processes, including alternatives with side-streams, column stacking and thermally coupled sequences. However, there is very little guidance in the literature about which alternative is likely to work the best in a given situation.To address this deficiency, in this work, seventeen industrially-relevant chemical systems comprising two species that form a minimum boiling azeotrope and a heavy entrainer are selected for study. Two ordinary and six energy-saving flowsheet alternatives for extractive distillation processes were also selected. Each of the eight flowsheet alternatives was optimized for each of the 17 chemical systems. A novel metric RCB (the ratio of the entrainer flow rate to the heavy key flow rate) is proposed to facilitate interpretation of the results. General trends in the relative attractiveness of the three energy-saving strategies (side streams, thermal coupling, column stacking heat integration) were found as RCB changes. An understanding of these trends can help engineers to understand the conditions for which various energy-savings strategies are most likely to be effective.
引用
收藏
页数:15
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共 56 条
[1]   The effect of solvent selection on energy-integrated extractive distillation for aromatics recovery from pyrolysis gasoline: simulation and optimization [J].
Abushwireb, F. ;
Elakrami, H. ;
Emtir, M. .
PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 :243-+
[2]   Are thermally coupled distillation columns always thermodynamically more efficient for ternary distillations? [J].
Agrawal, R ;
Fidkowski, ZT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (08) :3444-3454
[3]   Criterion of the energy effectiveness of extractive distillation in the partially thermally coupled columns [J].
Anokhina, Elena ;
Timoshenko, Andrey .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 99 :165-175
[4]   Extractive distillation of 2-methoxy-2-methylpropane plus ethanol using 1-butanol as entrainer: Equilibria and simulation [J].
Arce, A ;
Rodil, E ;
Soto, A .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (06) :1135-1140
[5]   Comparison of pressure-swing distillation and extractive distillation with varied-diameter column in economics and dynamic control [J].
Cao, Yujuan ;
Hu, Jiajing ;
Jia, Hui ;
Bu, Guangle ;
Zhu, Zhaoyou ;
Wang, Yinglong .
JOURNAL OF PROCESS CONTROL, 2017, 49 :9-25
[6]   Design and control of an energy intensified side-stream extractive distillation for binary azeotropic separation of n-hexane and ethyl acetate [J].
Chen, Yu-Ying ;
Kong, Zong Yang ;
Yang, Ao ;
Lee, Hao-Yeh ;
Sunarso, Jaka .
SEPARATION AND PURIFICATION TECHNOLOGY, 2022, 294
[7]   Systematic Strategy for Obtaining a Dividing-Wall Column Applied to an Extractive Distillation Process [J].
Cordeiro, Gardenia M. ;
de Figueiredo, Marcella F. ;
Ramos, Wagner B. ;
Sales, Fabricia A. ;
Brito, Karoline D. ;
Brito, Romildo P. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (14) :4083-4094
[8]   Process synthesis and plantwide control of intensified extractive distillation with preconcentration for separating the minimum-boiling azeotropes: A case study of acetonitrile dehydration [J].
Cui, Chengtian ;
Zhang, Qingjun ;
Zhang, Xiaodong ;
Sun, Jinsheng ;
Chien, I-Lung .
SEPARATION AND PURIFICATION TECHNOLOGY, 2022, 285
[9]   Design and optimization of energy-efficient liquid-only side-stream distillation configurations using a stochastic algorithm [J].
Cui, Chengtian ;
Zhang, Xiaodong ;
Sun, Jinsheng .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2019, 145 (48-52) :48-52
[10]   Phase equilibria behaviour of n-heptane with o-xylene, m-xylene, p-xylene and ethylbenzene at 101.3kPa [J].
Díaz, C ;
Tojo, J .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2002, 34 (12) :1975-1984