An optimal design methodology for large-scale gas liquefaction

被引:35
作者
Li, Yongliang [1 ]
Wang, Xiang [2 ]
Ding, Yulong [1 ,2 ]
机构
[1] Univ Leeds, Inst Particle Sci & Engn, Leeds LS2 9JT, W Yorkshire, England
[2] Chinese Acad Sci, Inst Proc Engn, State Key Lab Multiphase Complex Syst, Beijing 10090, Peoples R China
基金
英国工程与自然科学研究理事会;
关键词
Gas liquefaction system; Process modelling; Thermodynamic optimization; Pinch technology; OPTIMIZATION; HYDROGEN; PLANT;
D O I
10.1016/j.apenergy.2012.04.040
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This paper presents an optimization methodology for thermodynamic design of large scale gas liquefaction systems. Such a methodology enables configuration selection and parametric optimization to be implemented simultaneously. Exergy efficiency and genetic algorithm have been chosen as an evaluation index and an evaluation criterion, respectively. The methodology has been applied to the design of expander cycle based liquefaction processes. Liquefaction processes of hydrogen, methane and nitrogen are selected as case studies and the simulation results show that relatively high exergy efficiencies (52% for hydrogen and 58% for methane and nitrogen) are achievable based on very general consumptions. Crown Copyright (C) 2012 Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:484 / 490
页数:7
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