Numerical Studies on Hydrogen Production from Ammonia Thermal Cracking with Catalysts

Peikai Yuan, Longwei Chen (), Chengzhou Liu and Zhiwei Wang
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Peikai Yuan: School of Mechanical Engineering, Anhui University of Science and Technology, Huainan 232000, China
Longwei Chen: Institute of Energy, Hefei Comprehensive National Science Center, Hefei 230000, China
Chengzhou Liu: Institute of Energy, Hefei Comprehensive National Science Center, Hefei 230000, China
Zhiwei Wang: Institute of Energy, Hefei Comprehensive National Science Center, Hefei 230000, China

Energies, 2023, vol. 16, issue 13, 1-18

Abstract: To explore and optimize the process of hydrogen production from plasma-assisted ammonia-cracking, a tubular ammonia-cracking on-site hydrogen production device with plasma-assisted ammonia combustion flue gas as the heat source was developed. Using the Temkin–Pyzhev kinetic model and the local thermal equilibrium (LTE) hypothesis, the effects of operating conditions, such as combustion flue gas temperature and ammonia flow rates, on ammonia-cracking efficiency were investigated. The numerical results are quantitatively consistent with the experiment. Ammonia cracking efficiency is notably influenced by the initial combustion gas temperature. When the gas velocity of the cracking system is less than or equal to 0.03 m/s, the cracking rate increases by 63% when the inlet temperature of the heat pipe changes from 700 K to 800 K. The cracking rate of ammonia decreased with the increase of ammonia flow rate, and this trend reached the maximum and began to weaken when the flow rate was 0.3 m/s. Longer catalyst bed length does not always mean higher cracking efficiency; the length of the cracking tube over 0.6 m shows little effect on cracking efficiency. Response surface methodology was used to conduct multi-factor analysis of the three main factors affecting the cracking rate of the cracker, namely, the temperature of the heating tube, the flow rate of flue gas in the heating process, and the inlet flow rate of the catalytic bed. It was found that the flow rate of the catalytic bed was the most significant factor affecting the cracking rate, which could be used as the main control method. The numerical results would provide technical guidance for industrial applications of on-site hydrogen production devices from ammonia decomposition.

Keywords: ammonia-cracking; Temkin–Pyzhev kinetic model; plasma-assisted ammonia combustion; on-site hydrogen production (search for similar items in EconPapers)
JEL-codes: Q Q0 Q4 Q40 Q41 Q42 Q43 Q47 Q48 Q49 (search for similar items in EconPapers)
Date: 2023
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