Thermodynamic and Economic Analysis of the Green Ammonia Synthesis System Driven by Synergistic Hydrogen Production Using Alkaline Water Electrolyzers and Proton Exchange Membrane Electrolyzers

被引:0
|
作者
Yu, Jianyu [1 ]
Liu, Luyao [2 ]
Du, Yiyun [3 ]
Li, Yanchao [1 ]
Zhang, Dongshun [3 ]
Li, Biao [3 ]
Liu, Xianhai [4 ]
Cheng, Linsheng [3 ]
Zhang, Xinyi [3 ]
Zhang, Yumeng [2 ]
机构
[1] Jilin Elect Power CO LTD, Changchun 130022, Peoples R China
[2] North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China
[3] State Nucl Elect Power Planning Design & Res Inst, Beijing 100095, Peoples R China
[4] Daan Jilin Elect Power Green Hydrogen Energy CO LT, Baicheng, Peoples R China
关键词
alkaline water electrolyzer; ammonia; multi-objective optimization; proton exchange membrane electrolyzer; POWER; PERFORMANCE; INTEGRATION; SOLAR;
D O I
10.1002/ente.202401169
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Green ammonia and hydrogen from renewable energy sources have emerged as crucial players during the transition of the chemical industry from a fossil energy-dominated economy to one that is environmentally friendly. This work proposes a green ammonia synthesis system driven by synergistic hydrogen generation using alkaline water electrolyzers (AWE) and proton exchange membrane electrolyzers (PEMEC). The effects of hydrogen-production ratios of PEMEC and AWE on the thermodynamic and economic performance of the system are compared and analyzed via multi-objective optimization. The findings showed that an increase in the amount of hydrogen produced by PEMEC improves the system's energy efficiency, but the payback period is delayed because of the PEMEC high initial investment cost. The techno-economic performance of the system at a 1:1 ratio of PEMEC to AWE hydrogen production are investigated considering the system level heat integration based on the pinch point analysis method to maximize the heat recovery. The results show that increasing the operational temperature, the pressure of the electrolyzer, and the ammonia synthesis pressure will enhance the system's thermal performance. Economic analysis shows that reducing electricity prices and electrolyzer investment costs will be the key to achieving the economic feasibility of the green ammonia system. A novel ammonia synthesis system is proposed, which combines alkaline water electrolyzers (AWE) and proton exchange membrane electrolyzers (PEMEC) to produce hydrogen in a synergistic manner. A comparative analysis is performed to assess the influence of hydrogen-production ratios of PEMEC and AWE on the thermodynamic and economic performance of the system via multi-objective optimization.image (c) 2024 WILEY-VCH GmbH
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页数:13
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