Energy-efficient separation design of diisopropylether/isopropanol/water system having three distillation regions and liquid-liquid envelope

被引:26
作者
Lin, Kai-Yang [1 ]
Tsai, Meng-Lin [1 ]
Chien, I-Lung [1 ]
机构
[1] Natl Taiwan Univ, Dept Chem Engn, Taipei 106, Taiwan
关键词
Ternary separation; Multiple azeotropes; Liquid-liquid separation; Pressure-swing distillation; Energy-saving scheme; Process design; PRESSURE-SWING DISTILLATION; HETEROGENEOUS AZEOTROPIC DISTILLATION; MULTI-RECYCLE STREAMS; DIVIDING WALL COLUMN; EXTRACTIVE DISTILLATION; ISOPROPYL-ALCOHOL; TERNARY MIXTURE; MIXED ENTRAINER; DIISOPROPYL ETHER; HEAT INTEGRATION;
D O I
10.1016/j.seppur.2020.117292
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work mainly focus on providing an energy-efficient design scheme for the separation of ternary mixture containing diisopropyl ether, isopropanol and water. The residue curve maps of this mixture is very complex, including: three binary azeotropes, one ternary azeotrope, three distillation regions and liquid-liquid envelope. With the preference of not adding foreign component into this separation, a new energy-efficient design flow sheet is proposed in this paper making use of natural liquid-liquid separation in a decanter together with varying operating pressure to expand the operating distillation region for the respective column. This design flowsheet can further be heat-integrated to combine a condenser of one column with partial heat input of a reboiler of another column and also add a feed-effluent heat exchanger to preheat the feed of one column. By comparing the economic performance of the proposed design flowsheet with that of a design flowsheet published in a recent paper, significant savings in total annual cost of 42.9% and in annual operating cost of 48.1% can be realized by our proposed design flowsheet.
引用
收藏
页数:13
相关论文
共 71 条
[1]   Feasibility analysis of isopropanol recovery by hybrid distillation/pervaporation process with the aid of conceptual models [J].
Angelica Sosa, Maria ;
Espinosa, Jose .
SEPARATION AND PURIFICATION TECHNOLOGY, 2011, 78 (02) :237-244
[2]  
[Anonymous], 2016, IND ENG CHEM RES, DOI DOI 10.1021/acs.iecr.6b02997
[3]   Design and control of an isopropyl alcohol dehydration process via extractive distillation using dimethyl sulfoxide as an entrainer [J].
Arifin, Saiful ;
Chien, I-Lung .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (03) :790-803
[4]   Combined preconcentrator/recovery column design for isopropyl alcohol dehydration process [J].
Arifin, Saiful ;
Chien, I-Lung .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (08) :2535-2543
[5]   Double-partitioned dividing wall column for a multicomponent azeotropic system [J].
Aurangzeb, Md. ;
Jana, Amiya K. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2019, 219 :33-46
[6]   Pressure-Swing Dividing Wall Column with Multiple Binary Azeotropes: Improving Energy Efficiency and Cost Savings through Vapor Recompression [J].
Aurangzeb, Md ;
Jana, Amiya K. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (11) :4019-4032
[7]   Energy-Saving Design and Control of a Methyl Methacrylate Separation Process [J].
Chang, Wei-Lun ;
Chien, I. -Lung .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2016, 55 (11) :3064-3074
[8]   Design and Control of a Complete Azeotropic Distillation System Incorporating Stripping Columns for Isopropyl Alcohol Dehydration [J].
Chang, Wen-Teng ;
Huang, Chi-Tsung ;
Cheng, Shueh-Hen .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (07) :2997-3006
[9]   Critical Assessment of Using an Ionic Liquid as Entrainer via Extractive Distillation [J].
Chen, Hung-Hsin ;
Chen, Meng-Kai ;
Chen, Bor-Chang ;
Chien, I-Lung .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (27) :7768-7782
[10]   Design and control of a complete heterogeneous azeotropic distillation column system [J].
Chien, IL ;
Zeng, KL ;
Chao, HY .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (09) :2160-2174