Integration design optimization of self-thermal methanol steam reforming microreactor for hydrogen production

被引:7
|
作者
Zheng, Tianqing [1 ]
Zhou, Dongjie [2 ]
Zhan, Youji [1 ]
Xu, Yongchao [3 ]
机构
[1] Fujian Univ Technol, Fujian key Lab Intelligent Machining Technol & Equ, Fuzhou 350118, Peoples R China
[2] Fujian Univ Technol, Sch Humanities, Fuzhou 350118, Peoples R China
[3] Fujian Univ Technol, Sch Mat Sci & Engn, Fuzhou 350118, Peoples R China
关键词
Hydrogen production catalyst; support; Combustion catalyst support; Self-thermal microreactor for; CATALYST SUPPORT; PERFORMANCE; REACTOR;
D O I
10.1016/j.ijhydene.2023.05.013
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
To enhance hydrogen production (HP) capability of self-thermal methanol steam reforming microreactor (MSRM), the integration design of MSRM is optimized from the aspects of the structure of combustion catalyst support (CCS), the number of CCS, the relative flow di-rection between HP reactant and combustion reactant, and the capability amplification mode of the microreactor. The results show that, when the microreactor uses the CCS with optimized structure in its front-end and integrates 2 CCSs with non-optimized structure in its back-end, meanwhile adopting the opposite flow direction between HP reactant and combustion reactant, as well as employing the number-amplified capability amplification method, it can obtain higher HP capability, whose CH3OH conversion, H2 quantity and CO selectivity are up to 100%, 2.519 mol/h and 4.43%, respectively, at the feed quantity of 48 mL/h methanol-water compound (fuel for HP) and 3.2 mL/min methanol (fuel for
引用
收藏
页码:32642 / 32653
页数:12
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