Catalytic properties of a pure Ni coil catalyst for methane steam reforming

被引:18
|
作者
Hirano, Toshiyuki [1 ]
Xu, Ya [1 ]
机构
[1] NIMS, 1-2-1 Sengen, Tsukuba, Ibaraki 3050047, Japan
基金
日本学术振兴会;
关键词
Hydrogen production; Metallic monolithic catalyst; Ni coil catalyst; Geometric specific surface area; Space velocity; Steam-to-carbon ratio; METAL MONOLITH; MICROCHANNEL REACTORS; STRUCTURED CATALYST; HYDROGEN-PRODUCTION; HEAT-TRANSFER; NATURAL-GAS; FUEL;
D O I
10.1016/j.ijhydene.2017.10.135
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
A tightly rolled pure Ni coil catalyst was assembled to ensure a stable catalytic performance in a wide range of conditions for methane steam reforming. With a high geometric specific surface area of 88.1 cm(2)/cm(3), the coil catalyst achieved the objective of this study in the range of the space velocity (455-2800 h(-1)), steam-to-carbon ratio (0.62-2.48), and temperature (973-1073 K), which was hard to achieve on our previously developed Ni honeycomb catalyst with a geometric specific surface area of 59.4 cm(2)/cm(3). Methane steam reforming reaction was slightly accelerated by the reactant flow because of the mass transfer enhancement of H-2, CO, and CO2. The conversion, selectivity, and yield of the products were evaluated as a function of the conditions mentioned above. The high H-2 production rate per unit catalyst volume demonstrated the high potential of the Ni coil catalyst for applications to small-scale hydrogen production system. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:30621 / 30629
页数:9
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