Techno-economic and environmental assessment of hydrogen production through ammonia decomposition

被引:37
作者
Devkota, Sijan [1 ]
Cha, Jin-Young [1 ]
Shin, Beom-Ju [1 ]
Mun, Ji-Hun [1 ]
Yoon, Hyung Chul [2 ]
Mazari, Shaukat Ali [1 ,3 ]
Moon, Jong-Ho [1 ]
机构
[1] Chungbuk Natl Univ, Dept Chem Engn, Cheongju, Chungbuk, South Korea
[2] Korea Inst Energy Res, Clean Fuel Lab, Daejon, South Korea
[3] Dawood Univ Engn & Technol, Dept Chem Engn, Karachi, Pakistan
基金
新加坡国家研究基金会;
关键词
Hydrogen energy; Ammonia decomposition; Hydrogen carrier; Techno-economic analysis; Global warming potential analysis; FUEL; CATALYSTS; METHANOL;
D O I
10.1016/j.apenergy.2023.122605
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
Hydrogen is one of the potential candidates to replace fossil fuels to meet net zero emissions target. This study reports a detailed techno-economic and environmental assessment of hydrogen production through ammonia decomposition. The case study is based on a multiple catalytic packed bed reactor with intermediate heating system. Aspen plus (R) and MATLAB (R) were linked to evaluate economic and environmental impact of the process. The process parameter like furnace temperature, flue gas recirculation, ammonia decomposition temperature, market ammonia supply pressure, ammonia decomposition pressure, hydrogen purification unit's pressure and equivalence ratio, and economic parameters of capital expenditure (CAPEX) and operating expenditure (OPEX) were considered. The overall thermal efficiency of the developed process is found to be 79%. The levelized cost of hydrogen (LCOH) is estimated and found to be 6.05 USD/kg of H2 based on CAPEX and OPEX. A major contribution of up to 62.2% to LCOH comes from the price of feed Ammonia. Based on 25 -year plant life with 10% discounted rate the plant is economically viable, with a return on investment of 23.7%, in a payback period of 3.58 years. Global warming potential of the process is also carried out.
引用
收藏
页数:13
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