Steam methane reforming in a Pd-Au membrane reactor: Long-term assessment

被引:55
作者
Abu El Hawa, Hani W. [1 ]
Lundin, Sean-Thomas B. [1 ]
Patki, Neil S. [1 ]
Way, J. Douglas [1 ]
机构
[1] Colorado Sch Mines, Dept Chem & Biol Engn, Golden, CO 80401 USA
关键词
Palladium-gold composite membrane; Steam methane reforming; Catalytic membrane reactor; Hydrogen separation; Electroless plating; EFFICIENT HYDROGEN-PRODUCTION; COMPOSITE MEMBRANES; ALLOY MEMBRANES; TERNARY ALLOY; SEPARATION; CATALYST; PERFORMANCE; PERMEATION; FABRICATION; BINARY;
D O I
10.1016/j.ijhydene.2016.04.244
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 work, electroless deposition was used to fabricate a 5.0 mu m thick Pd-28Au (wt. %) membrane (16.10 cm(2)) supported on a YSZ/PSS substrate. After annealing in hydrogen, steam methane reforming (SMR) was conducted continuously for 530 h, with permeate purity remaining above 99.2% for the duration. The reactor used a 0.5 wt. % Ru/Al2O2 catalyst and ran at 2.8 MPa and a steam-to-carbon ratio of 3, with temperature varied between 480 degrees C and 580 degrees C. Methane conversion was as high as 94% depending on temperature and space velocity. This represents a significant improvement over the thermodynamic equilibrium shift of 35% under similar conditions. Additionally, the hydrogen flux and overall methane conversion showed stable performance over time. The membrane thickness and composition were verified using SEM/EDS, XRD, XRF and ICP-AES. Furthermore, cross sectional EDS and XRD data indicated uniform gold composition throughout the film, suggesting homogeneous alloy formation. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:10193 / 10201
页数:9
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