Numerical study on hydrogen recovery performance of a novel industrial scale hydride-based flow-through hydrogen purification reactor with distributed gas inlet tubes

被引:0
作者
Li, Ruiqing [1 ]
Wan, Guangze [1 ]
Guo, Leilei [1 ]
Yang, Fusheng [1 ]
Wu, Zhen [1 ]
Zhang, Zaoxiao [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Metal hydride; Hydrogen recovery; Poisoning effect; Optimal design; MASS-TRANSFER; METAL; SEPARATION; HEAT; STORAGE; SIMULATION; OPTIMIZATION; ABSORPTION; MEMBRANES; ENERGY;
D O I
10.1016/j.ijhydene.2025.150496
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
In this study, an industrial-scale, flow-through metal hydride hydrogen purification (MHHP) reactor with distributed gas inlet tubes loaded with 160 kg of LaNi4.3Al0.7 material was designed. Numerical simulations were employed to analyze the impact of reactor structure parameters, such as bed thickness and gas inlet tube length. Further, we investigated how operational parameters, including heat transfer fluid temperature, hydrogen partial pressure, and raw gas composition, influence the absorption efficiency of the reactor. Moreover, an annular finned MHHP reactor was designed, which increased the hydrogen absorption efficiency from 70 % to 77.7 % under low pressure (0.67 MPa). This research contributes to the development of high-performance industrial scale MHHP reactor, provides valuable insights into the application of large MHHP reactors in the recovery of industrial by-product hydrogen.
引用
收藏
页数:19
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