Hollow fibre membrane reactors for high H2 yields in the WGS reaction

被引:31
作者
Garcia-Garcia, F. R. [2 ]
Torrente-Murciano, L. [1 ]
Chadwick, D. [2 ]
Li, K. [2 ]
机构
[1] Univ Bath, Dept Chem Engn, Bath BA2 7AY, Avon, England
[2] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, London SW7 2AZ, England
基金
英国工程与自然科学研究理事会;
关键词
Pd-based membranes; Asymmetric ceramic hollow fibre; Ceria; Nanostructured catalysts; GAS SHIFT REACTION; CARBON-MONOXIDE; HYDROGEN FLUX; THIN; PERMEATION; STEAM; PD/AG;
D O I
10.1016/j.memsci.2012.02.031
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Alumina hollow fibres with narrow pore size distribution and high surface area/volume ratio are presented as a cost-effective alternative support for metallic membranes which can potentially ease the large-scale implementation of membrane reactors. In this article, we demonstrate the formation of a defect-free thin (similar to 5 mu m) Pd/Ag layer over the smooth outer surface of hollow fibres with high H-2 permeation fluxes (48.41 L m(-2) h(-1) at 450 degrees C and Delta P-0.5 of 1.01 atm(0.5)) and 100% H-2 perm-selectivity. Their use in hollow fibre membrane reactors (HFMR) allows the selective extraction of H-2 from the reaction medium, especially relevant in H-2-formation equilibrium reactions. Thus, the water-gas shift reaction was used as a proof-reaction. When the HFMR is combined with a highly stable and active nanostructured Pt/CeO2 catalyst, enhanced selectivities and activities are achieved as a result of the integration of the reaction and separation steps. The best results were obtained at high temperatures (375-525 degrees C) where the thermodynamic equilibrium conversion was exceeded by up to 14%. (C) 2012 Elsevier B. V. All rights reserved.
引用
收藏
页码:30 / 37
页数:8
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