Exergoeconomic evaluation of single mixed refrigerant natural gas liquefaction processes

被引：64

作者：

Mehrpooya, Mehdi ^{[1
]}

Ansarinasab, Hojat ^{[2
]}

机构：

[1] Univ Tehran, Renewable Energies & Environm Dept, Fac New Sci & Technol, Tehran, Iran

[2] Petr Univ Technol, Fac Energy Syst Engn, Tehran, Iran

来源：

ENERGY CONVERSION AND MANAGEMENT | 2015年 / 99卷

关键词：

Natural gas; Liquefaction; Exergy; Exergoeconomic; Refrigeration; THERMOECONOMIC ANALYSIS; POWER-PLANT; PROCESS CONFIGURATION; EXERGY ANALYSIS; OPTIMIZATION; LNG; DESALINATION; ENERGY; DESIGN; NGL;

D O I：

10.1016/j.enconman.2015.04.038

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

Exergy and exergoeconomic analysis is performed for single mixed refrigerant Linde and Air Products and Chemicals Inc, processes, which are among the most important and popular natural gas liquefaction processes. Cost of exergy destruction, exergoeconomic factor, exergy destruction and exergy efficiency are calculated. Results of exergy analysis demonstrates that exergy efficiency of Linde process is around 40.2%, and its total exergy destruction rate is 93,229 kW. The exergy efficiency and exergy destruction rate for Air Products and Chemicals Inc, process are 45.0% and 72,245 kW respectively. Results of exergoeconomic analysis suggests that maximum exergy destruction cost for Linde process is related to E-2 heat exchanger which is 34,072 $/h and for Air Products and Chemicals Inc, process maximum exergy destruction cost is related to E-2 heat exchanger with the value of 4125 kW. Sensitivity of cost of exergy destruction and exergoeconomic factor to operating variables of the processes are studied and analyzed. (C) 2015 Elsevier Ltd. All rights reserved.

引用

页码：400 / 413

页数：14

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