Strategy of purifier selection and integration in hydrogen networks

被引:130
作者
Liu, F [1 ]
Zhang, N [1 ]
机构
[1] Univ Manchester, Dept Process Integrat, Manchester M60 1QD, Lancs, England
关键词
hydrogen network; purification; integration;
D O I
10.1205/cerd.82.10.1315.46739
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Tighter environmental regulations and more heavy-end upgrading in the petroleum industry lead to increased demand for hydrogen in oil refineries. In this paper, a systematic methodology is proposed to select appropriate purifiers from pressure swing adsorption processes, membranes or hybrid systems for recovering hydrogen from refinery off-gases. Through the understanding of the trade-offs between hydrogen saving, compression costs and capital investment, a superstructure is built to include possible purification scenarios. The shortcut models for different purification units are developed via the insights of the processes. The recovery rate of purifiers is also modelled to optimize process parameters. This method achieves the optimal design for overall hydrogen networks at a conceptual level.
引用
收藏
页码:1315 / 1330
页数:16
相关论文
共 29 条
[1]  
ADJIMAN CS, 1998, DIMACS SERIES DISCRE, V40, P429
[2]  
AITANI AM, 1995, ERDOL KOHLE ERDGAS P, V48, P19
[3]  
ALLEN P, 1999, HYDROCARBON ENG APR, P71
[4]  
ALVES J, 1999, THESIS UMIST
[5]  
Biegler L. T., 1997, SYSTEMATIC METHODS C
[6]  
Brooke A., 1996, GAMS USERS GUIDE REL
[7]   Short-cut evaluation of pressure swing adsorption systems [J].
Chung, Y ;
Na, BK ;
Song, HK .
COMPUTERS & CHEMICAL ENGINEERING, 1998, 22 :S637-S640
[8]   Integrated membrane/adsorption process for gas separation [J].
Feng, XS ;
Pan, CY ;
Ivory, J ;
Ghosh, D .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (09) :1689-1698
[9]  
Knaebel KS, 1999, CHEM ENG-NEW YORK, V106, P92
[10]   A preliminary design study of a multicomponent PSA gas separation system [J].
Kvamsdal, HM ;
Hertzberg, T .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1996, 35 (03) :213-224