Optimization of a novel liquefaction process based on Joule-Thomson cycle utilizing high-pressure natural gas exergy by genetic algorithm

被引:13
作者
Guo, Hao [1 ]
Tang, Qixiong [1 ,2 ]
Gong, Maoqiong [1 ]
Cheng, Kuiwei [1 ]
机构
[1] Chinese Acad Sci, Tech Inst Phys & Chem, Key Lab Cryogen, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 101408, Peoples R China
基金
中国国家自然科学基金;
关键词
High-pressure natural gas; Liquefaction process; Joule-Thomson cycle; Thermodynamic and economic optimization; Exergy analysis; NITROGEN EXPANSION; LNG;
D O I
10.1016/j.energy.2018.02.148
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel liquefaction process based on Joule Thomson cycle utilizing high-pressure natural gas exergy is specifically proposed and presented in this paper. Thermodynamic and economic optimization of the novel process are performed with the genetic algorithm (GA) in Microsoft Excel VBA connecting Aspen HYSYS. Five different objective functions are selected: minimization of specific energy consumption (SEC), total cost investment (TCI), specific operation cost (SOPEX), total annualized cost (TAC) and maximization of exergy efficiency. The specific energy consumption objective function is equivalent to exergy efficiency, SOPEX, TAC objective functions. Compared to T CI objective function, the other four objective functions can result in an about 49% reduction of SEC, an about 99% increase of exergy efficiency, an about 2% reduction of SOPEX and an about 2.8% reduction of TAC, but an about 95% increase of TCI. The results show that any of SEC, exergy efficiency, SOPEX and TCI objective functions is more suitable for the optimization of this process. Finally, the exergy analysis of each component is given. It can be found that compressors and water coolers produce the highest exergy losses for the equivalent objective functions. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:696 / 706
页数:11
相关论文
共 22 条
[1]   A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 3: The combined carrier and onshore storage [J].
Aspelund, Audun ;
Tveit, Steinar P. ;
Gundersen, Truls .
APPLIED ENERGY, 2009, 86 (06) :805-814
[2]   A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 4: Sensitivity analysis of transport pressures and benchmarking with conventional technology for gas transport [J].
Aspelund, Audun ;
Gundersen, Truls .
APPLIED ENERGY, 2009, 86 (06) :815-825
[3]   A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 2: The offshore and the onshore processes [J].
Aspelund, Audun ;
Gundersen, Truls .
APPLIED ENERGY, 2009, 86 (06) :793-804
[4]   A liquefied energy chain for transport and utilization of natural gas for power production with CO2 capture and storage - Part 1 [J].
Aspelund, Audun ;
Gundersen, Truls .
APPLIED ENERGY, 2009, 86 (06) :781-792
[5]  
AspenTech, 2011, ASO HYGYS US GUID V7
[6]   Full load synthesis/desigin optimization of a hybrid SOFC-GT power plant [J].
Calise, F. ;
d'Accadia, M. Dentice ;
Vanoli, L. ;
von Spakovsky, Michael R. .
ENERGY, 2007, 32 (04) :446-458
[7]  
Cranmore RG, 2000, MODERN PETROLEUM TEC, P383
[8]   Coalbed methane liquefaction adopting a nitrogen expansion process with propane pre-cooling [J].
Gao, Ting ;
Lin, Wensheng ;
Gu, Anzhong ;
Gu, Min .
APPLIED ENERGY, 2010, 87 (07) :2142-2147
[9]   Development and performance test of a small trailer-mounted moveable natural gas liquefier [J].
Gong, Maoqiong ;
Wu, Jianfeng ;
Sun, Zhaohu ;
Liu, Jiayong ;
Hu, Qinguo .
ENERGY CONVERSION AND MANAGEMENT, 2012, 57 :148-153
[10]   A novel process for small-scale pipeline natural gas liquefaction [J].
He, T. B. ;
Ju, Y. L. .
APPLIED ENERGY, 2014, 115 :17-24