An improvement scheme for pressure-swing distillation with and without heat integration through an intermediate connection to achieve energy savings

被引:57
作者
Wang, Yinglong [1 ]
Ma, Kang [1 ]
Yu, Mengxiao [1 ]
Dai, Yao [1 ]
Yuan, Rujia [2 ]
Zhu, Zhaoyou [1 ]
Gao, Jun [3 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
[2] Qingdao 2 Middle Sch Shandong Prov, Qingdao 266042, Peoples R China
[3] Shandong Univ Sci & Technol, Coll Chem & Environm Engn, Qingdao 266590, Peoples R China
基金
中国国家自然科学基金;
关键词
Pressure-swing distillation; Heat integration; Intermediate connection; TAC; Energy consumption; HETEROGENEOUS AZEOTROPIC DISTILLATION; EXTRACTIVE DISTILLATION; BIOETHANOL SEPARATION; DEHYDRATION SYSTEM; BOILING AZEOTROPE; TERNARY AZEOTROPE; MIXED ENTRAINER; DYNAMIC CONTROL; ETHYL-ACETATE; DESIGN;
D O I
10.1016/j.compchemeng.2018.09.012
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
Pressure-swing distillation is widely studied in academia and industry. Energy consumption is a key criterion for judging whether a pressure-swing distillation is better than other distillation methods. An improved process with an intermediate connection was developed based on the two-column pressure-swing distillation for separating a binary azeotropic mixture to save energy and reduce the total annual cost. The proposed pressure-swing distillation was applied to three case systems, two minimum-boiling azeotropic mixtures of ethyl acetate/ethanol and methanol/chloroform and one maximum-boiling azeotropic mixture of ethylenediamine/water. According to our analysis, the proposed pressure-swing distillation and heat integrated scheme can reduce energy consumption and total annual cost. The pressure-swing distillation with the intermediate connection is promising for saving energy. This advantage assists in promoting the application of pressure-swing distillation and overall energy savings in the chemical process industry. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:439 / 449
页数:11
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