共 38 条
Energy, exergy, and exergoeconomic evaluations of a novel power, steam, and hydrogen system based of molten carbonate fuel cell driver
被引:2
作者:
Balakheli, Mohammad Mahdi
[1
]
Mehregan, Mahmood
[1
]
Hashemian, Seyed Majid
[1
]
机构:
[1] Shahrood Univ Technol, Fac Mech Engn, POB 3619995161, Shahrood, Iran
关键词:
Simultaneous production of power;
Steam;
And hydrogen;
Molten carbonate fuel cell;
Proton exchange membrane electrolyzer;
Organic fluids;
GAS-TURBINE;
PERFORMANCE ASSESSMENT;
STIRLING ENGINE;
CYCLE SYSTEM;
CCHP SYSTEM;
PLANT;
OPTIMIZATION;
ELECTROLYZER;
COLLECTOR;
CAPTURE;
D O I:
10.1016/j.ijhydene.2024.09.276
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
Considering the importance of using systems with high productivity, in order to reduce fuel consumption and economic savings, multiple production systems can be an attractive option. In this study, a simultaneous production system of power, steam and hydrogen based on molten carbonate fuel cell with methane fuel source is presented. The proposed system consists of four main parts, molten carbonate fuel cell, heat recovery steam generator, proton exchange membrane electrolyzer, and organic Rankine cycle. The system is evaluated from viewpoints of energy, exergy and exergeoeconomics. In the organic Rankine cycle, R141b has the best performance in terms of electricity production, organic fluid consumption, and efficiency among the proposed organic fluids, so that with R141b the efficiency reaches to 18.31%. Also, 68.85% of heat recovery is done by the heat recovery steam generator and the rest is done by the heat recovery vapor generator. The energy, exergy, and electrical efficiencies of the proposed system are 64.29, 63.53, and 39.69%, respectively, which shows a good performance compared to many power plants. The highest exergy destruction occurs in the air heat exchanger with 45673 kW. The operating cost rate of the system is 2.38 $/s and the hydrogen production rate is 3.67 kg/h.
引用
收藏
页码:1436 / 1450
页数:15
相关论文