Thermoeconomic analysis of a new combination of ammonia/water power generation cycle with GT-MHR cycle and LNG cryogenic exergy

被引:60
作者
Mosaffa, A. H. [1 ]
Mokarram, N. Hasani [1 ]
Farshi, L. Garousi [2 ]
机构
[1] Azarbaijan Shahid Madani Univ, Dept Mech Engn, Tabriz, Iran
[2] Univ Tabriz, Fac Mech Engn, Tabriz, Iran
关键词
Ammonia/water power generation cycle; Thermodynamic analysis; Economic analysis; Turbine-Modular Helium Reactor; LNG cryogenic exergy; LIQUEFIED NATURAL-GAS; TEMPERATURE WASTE HEAT; ORGANIC RANKINE-CYCLE; COLD ENERGY; THERMODYNAMIC ANALYSIS; ENVIRONMENTAL-ANALYSES; BINARY-MIXTURES; KALINA CYCLE; SYSTEM; OPTIMIZATION;
D O I
10.1016/j.applthermaleng.2017.06.126
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper deals with a thermoeconomic analysis of a new combination of ammonia/water power generation cycle and Turbine-Modular Helium Reactor (GT-MHR) cycle and liquefied natural gas (LNG) cryogenic exergy. In the proposed power generation system, the GT-MHR waste heat is considered as heat source as well as cryogenic exergy of LNG as thermal sink. Parametric study is performed to investigate the effects of key parameters. Also, a comparative study is conducted for proposed system with the same combined cycle without LNG cryogenic exergy. The results show that minimum temperature difference in the evaporator, Delta T-Ev, has the greatest effect on the energy and exergy efficiencies as well as total cost rate in comparison to other key parameters. For the proposed system, an increase in Delta T-Ev from 20 K to 30 K, leads to a reduction of 2.8% and 3.4%in both energy and exergy efficiencies and total cost rate, respectively. The results also show that the temperature and pressure of ammonia/water solution exiting the evaporator have the negligible effects on energy and exergy efficiencies. Also, ammonia concentration of solution entering the separator, has the greatest effect on the product cost. Moreover, a multi-objective optimization is performed to obtain optimal values of design parameters. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1343 / 1353
页数:11
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