Evaluation of an optimal integrated design multi-fuel multi-product electrical power plant by energy and exergy analyses

被引:33
|
作者
Mehrpooya, Mehdi [1 ]
Sharifzadeh, Mohammad Mehdi Moftakhari [2 ]
Mousavi, Seyed Ali [1 ]
机构
[1] Univ Tehran, Dept Renewable Energies & Environm, Fac New Sci & Technol, Tehran, Iran
[2] Islamic Azad Univ, Dept Chem Engn, Sci & Res Branch, Tehran, Iran
关键词
SOFC cycle; Heat integration; Energy and exergy analyses; CO2; capture; Electrical power plant; LIQUEFIED NATURAL-GAS; OXIDE FUEL-CELL; AIR SEPARATION PROCESS; THERMODYNAMIC ANALYSIS; COAL-GASIFICATION; HYDROGEN-PRODUCTION; CO2; CAPTURE; LNG COLD; THERMOECONOMIC OPTIMIZATION; SUPERCRITICAL WATER;
D O I
10.1016/j.energy.2018.12.018
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel integrated multi-fuel multi-product electrical power plant with a net electrical power output of 5.97 x 10(5) kW is developed and investigated by energy and exergy analyses. The electrical power plant including coal gasification, natural gas solid oxide fuel cell, cryogenic air separation unit, carbon dioxide transcritical and steam cycles, and liquefied natural gas regasification sub-systems. The potential of operating performance improvement by conducted energy and exergy analyses is assessed. Also, the thermal design and heat integration analyses are performed for studying the system sustainability and emphasizing on no requirement for external hot and cold utilities. Effects of the main design parameters such as fuel cell operating parameters, ambient temperature and liquefied natural gas thermodynamic specifications on the system operating performance are examined. The obtained results indicate that the overall energy and exergy efficiencies reach to a maximum value of about 56.4% and 57.9%, respectively; in the case of fuel utilization of solid oxide fuel cell is about 80.0%. Furthermore, increasing the ambient temperature and current density decrease the system operating performance. In contrast, the system performance increases with the liquefied natural gas vapor pressure. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:61 / 78
页数:18
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