4.7 Article

Evaluation of the water gas shift reaction in a palladium membrane reactor

期刊

CATALYSIS TODAY
卷 156, 期 3-4, 页码 165-172

出版社

ELSEVIER
DOI: 10.1016/j.cattod.2010.02.034

关键词

Membrane reactor; Palladium composite membrane; Water gas shift; Carbon monoxide conversion

资金

  1. Ministry of Economic Development - General Directorate for Energy and Mining Resources and ERSE S.p.A. (formerly CESI RICERCA)

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The water gas shift (WGS) reaction of a syngas mixture has been carried out in a tubular palladium membrane reactor at a temperature of 410-414 degrees C. A composite palladium-porous stainless steel membrane. 29 mu m thick, obtained by electroless plating, has been first extensively tested with pure gases (H-2, He, CO2) and syngas mixtures in the 310-455 degrees C temperature range and up to 800 kPa. Long-term stability of the membrane in H-2 at 400 degrees C has also been checked over a period of 1200 h. The membrane has been then used for WGS tests in a membrane reactor. The membrane reactor, packed with a pulverized Fe/Cr commercial catalyst, has been operated at a reaction pressure of 100-600 kPa in the counter-current mode, with a nitrogen sweep-gas. The reactor has been fed with a shift gas mixture with a 7.6% CO concentration and H2O/CO ratio in the 2.7-3.6 range. The membrane reactor was able to achieve up to the 85.0% of CO conversion, while only the 37% as a maximum, was reached with the traditional reactor in the same operating conditions. Up to the 82% of hydrogen has been recovered with a purity exceeding the 97%. (C) 2010 Elsevier B.V. All rights reserved.

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