Multi-objective optimization of hydrogen production process and steam reforming reactor design

被引:6
|
作者
Han, Ja-Ryoung [1 ]
Lee, Jong Min [2 ]
机构
[1] Korea Gas Corp, KOGAS Res Inst, 1248 Suin Ro, Ansan 15328, Gyeonggi Do, South Korea
[2] Seoul Natl Univ, Inst Chem Proc, Sch Chem & Biol Engn, Gwanak Ro 1, Seoul 08826, South Korea
关键词
Hydrogen energy; Computational fluid dynamics; Process modeling; Optimization; Process efficiency; Reactor design; BAYESIAN OPTIMIZATION; EXERGY ANALYSIS; H-2; PRODUCTION; METHANE; GAS;
D O I
10.1016/j.ijhydene.2023.04.002
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
This study proposes a multi-objective optimization approach to design a steam methane reforming (SMR) reactor and maximize the efficiency of the hydrogen production process. Out of 1782 possible variable combinations, only 50 iterations were performed, identifying three Pareto optimal that resulted in reactor size reductions of 50.53%, 35.56%, and 20.69%, respectively, compared to the reference reactor. The process efficiency for each optimal design varied slightly, with one achieving a 105.05% increase in efficiency, another remaining stable at 100.48%, and a third experiencing a slight decrease to 86.66% compared to the reference case. The results offer practical insights for planning an on-site distributed hydrogen production system, demonstrating that an increase in overall process efficiency can be achieved even with a reduced reactor size. This work is the first attempt to optimize a hydrogen production system by simultaneously considering overall process efficiency and SMR reactor design.& COPY; 2023 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:29928 / 29941
页数:14
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