Application of exergy analysis for improving energy efficiency of natural gas liquids recovery processes

被引:30
作者
Shin, Jihoon [1 ]
Yoon, Sekwang [1 ]
Kim, Jin-Kuk [1 ]
机构
[1] Hanyang Univ, Dept Chem Engn, Seoul 133791, South Korea
关键词
Energy efficiency; Natural gas liquids; Exergy analysis; Simulation; Optimization; DISTILLATION-COLUMNS; THERMODYNAMIC ANALYSIS; PROCESS DESIGN; OPTIMIZATION;
D O I
10.1016/j.applthermaleng.2014.10.042
中图分类号
O414.1 [热力学];
学科分类号
摘要
Thermodynamic analysis and optimization method is applied to provide design guidelines for improving energy efficiency and cost-effectiveness of natural gas liquids recovery processes. Exergy analysis is adopted in this study as a thermodynamic tool to evaluate the loss of exergy associated with irreversibility in natural gas liquids recovery processes, with which conceptual understanding on inefficient design feature or equipment can be obtained. Natural gas liquids processes are modeled and simulated within UniSim (R) simulator, with which detailed thermodynamic information are obtained for calculating exergy loss. The optimization framework is developed by minimizing overall exergy loss, as an objective function, subject to product specifications and engineering constraints. The optimization is carried out within MATLAB (R) with the aid of a stochastic solver based on genetic algorithms. The process simulator is linked and interacted with the optimization solver, in which optimal operating conditions can be determined. A case study is presented to illustrate the benefit of using exergy analysis for the design and optimization of natural gas liquids processes and to demonstrate the applicability of design method proposed in this paper. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:967 / 977
页数:11
相关论文
共 18 条
[1]  
[Anonymous], 1989, AVAILABILITY ANAL GU
[2]  
[Anonymous], 77 ANN GPA CONV DALL
[3]   Thermal integration of a distillation column through side-exchangers [J].
Bandyopadhyay, S. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2007, 85 (A1) :155-166
[4]   Temperature-enthalpy curve for energy targeting of distillation columns [J].
Bandyopadhyay, S ;
Malik, RK ;
Shenoy, UV .
COMPUTERS & CHEMICAL ENGINEERING, 1998, 22 (12) :1733-1744
[5]  
Bejan A., 1982, Entropy Generation through heat and fluid flow
[6]   Optimum ethane recovery in conventional turboexpander process [J].
Chebbi, R. ;
Al-Amoodi, N. S. ;
Jabbar, N. M. Abdel ;
Husseini, G. A. ;
Al Mazroui, K. A. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (5-6A) :779-787
[7]   Retrofit of distillation columns using thermodynamic analysis [J].
Demirel, Y .
SEPARATION SCIENCE AND TECHNOLOGY, 2006, 41 (05) :791-817
[8]  
Dincer I., 2001, Entropy, V3, DOI 10.3390/e3030116
[9]  
Feng X., 1997, THERM ENG, V17, P249
[10]   Design and Optimization of a Novel Mixed Refrigerant Cycle Integrated with NGL Recovery Process for Small-Scale LNG Plant [J].
He, Tianbiao ;
Ju, Yonglin .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (13) :5545-5553