4.7 Article

Hydrogen production from low temperature WGS reaction on co-precipitated Cu-CeO2 catalysts: An optimization of Cu loading

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 39, Issue 17, Pages 9135-9142

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2014.04.005

Keywords

Water-gas shift reaction; Co-precipitated; Cu-CeO2; Strong metal to support interaction; Sintering

Funding

  1. Research and Development Program of the Korea Institute of Energy Research (KIER) [B4-2423-02]
  2. Basic Science Research Program through the National Research Foundation of Korea (NRF) - Ministry of Science, ICT and Future Planning [2013R1A1A1A05007370]
  3. National Research Foundation of Korea [2013R1A1A1A05007370, 21A20130011104] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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Low temperature water-gas shift (WGS) reaction has been carried out at the gas hourly space velocity of 72,152 h(-1) over Cu-CeO2 catalyst prepared by a co-precipitation method. Cu loading was optimized to obtain highly active co-precipitated Cu-CeO2 catalysts for low temperature WGS. 80 wt% Cu-CeO2 exhibited the highest CO conversion as well as the most stable activity (X-CO > 46% at 240 degrees C for 100 h). The excellent catalytic performance is mainly due to a strong metal to support interaction, resulting in the prevention of Cu sintering. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.

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