Hydrogen permeation through a Pd-based membrane and RWGS conversion in H2/CO2, H2/N2/CO2 and H2/H2O/CO2 mixtures

被引:35
|
作者
Barreiro, M. M. [1 ]
Marono, M. [1 ]
Sanchez, J. M. [1 ]
机构
[1] Combust & Gasificat Div, Madrid 28040, Spain
关键词
Pd-based membranes; Hydrogen separation; Inhibition effects; GAS SHIFT REACTION; PALLADIUM MEMBRANE; THIN PD/AG;
D O I
10.1016/j.ijhydene.2013.11.089
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 investigated the effect of gases such as CO2, N-2, H2O on hydrogen permeation through a Pd-based membrane -0.012 m(2) - in a bench-scale reactor. Different mixtures were chosen of H-2/CO2, H-2/N-2/CO2 and H-2/H2O/CO2 at temperatures of 593-723 K and a hydrogen partial pressure of 150 kPa. Operating conditions were determined to minimize H-2 loss due to the reverse water gas shift (RWGS) reaction. It was found that the feed flow rate had an important effect on hydrogen recovery (HR). Furthermore, an identification of the inhibition factors to permeability was determined. Additionally, under the selected conditions, the maximum hydrogen permeation was determined in pure H-2 and the H-2/CO2 mixtures. The best operating conditions to separate hydrogen from the mixtures were identified. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4710 / 4716
页数:7
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