Comparing three configurations of the externally heat-integrated double distillation columns (EHIDDiCs)

被引:12
|
作者
Zhang, Xingxing [1 ]
Huang, Kejin [1 ]
Chen, Haisheng [1 ]
Wang, Shaofeng [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Informat Sci & Technol, Beijing 100029, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
Distillation; Heat integration; Process synthesis; Process design; Process controllability; PROCESS DESIGN; CONTROLLABILITY; EFFICIENCY; SYSTEMS; STATE;
D O I
10.1016/j.compchemeng.2010.11.008
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
In terms of separation of a binary mixture of ethylene and ethane, three configurations of externally heat-integrated double distillation columns (EHIDDiCs), including a symmetrical EHIDDiC (S-EHIDDiC), an asymmetrical EHIDDiC (A-EHIDDiC), and a simplified asymmetrical EHIDDiC (SA-EHIDDiC), are compared with respect to aspects related to process design and controllability. It has been found that the A-EHIDDiC and SA-EHIDDiC are superior to the S-EHIDDiC in terms of thermodynamic efficiency as well as in terms of process dynamics and controllability. As for the comparison between the A-EHIDDiC and SA-EHIDDiC, the latter shows somewhat comparable behaviors with the former in terms of process design and controllability. These results demonstrate that the asymmetrical configuration should generally be favored over the symmetrical one for the development of the EHIDDiC. It is feasible to approximate external heat integration using three heat exchangers between the high- and low-pressure distillation columns involved. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2017 / 2033
页数:17
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