Decline in Hydrogen Permeation Due to Concentration Polarization and CO Hindrance in a Palladium Membrane Reactor

Hydrogen separation from binary gas mixtures, Ar−H2 and CO−H2, using a double-tube type of palladium membrane reactor (PMR) was carried out and analyzed by solving mathematical models taking into account mixing diffusion of hydrogen in the radial direction of the catalyst-packed bed. The experiment...

Full description

Saved in:
Bibliographic Details
Published inIndustrial & engineering chemistry research Vol. 38; no. 12; pp. 4913 - 4918
Main Authors Hara, S, Sakaki, K, Itoh, N
Format Journal Article
LanguageEnglish
Published Washington, DC American Chemical Society 01.12.1999
Subjects
Online AccessGet full text

Cover

Loading…
More Information
Summary:Hydrogen separation from binary gas mixtures, Ar−H2 and CO−H2, using a double-tube type of palladium membrane reactor (PMR) was carried out and analyzed by solving mathematical models taking into account mixing diffusion of hydrogen in the radial direction of the catalyst-packed bed. The experiment showed that carbon monoxide prevented hydrogen permeation through the membrane at temperatures less than 280 °C. The decline in hydrogen permeation could be estimated by solving a model describing the concentration polarization and the hindrance by cabon monoxide. Furthermore, the mathematical models were applied to analyze methanol decomposition in the same PMR, showing that a drop in hydrogen permeation due to both the factors had a significant influence on the performance of the PMR.
Bibliography:istex:9CF14D11674003A4F3D846C44628807316D23815
ark:/67375/TPS-56MSWMWG-M
ISSN:0888-5885
1520-5045
DOI:10.1021/ie990200n