Water-gas shift of reformate streams over mono-metallic PGM catalysts |
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Authors: | Stephen J Roberts Jack V Fletcher Yi Zhou Niels TJ Luchters Jack CQ Fletcher |
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Affiliation: | Catalysis Institute, Department of Chemical Engineering, University of Cape Town, Private Bag X3, Rondebosch, 7701, South Africa |
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Abstract: | Mono-metallic Pt and Rh catalysts supported on both CeO2 and TiO2 were prepared and tested for water-gas shift activity in a Flowrence, high throughput reactor system. The feed composition mimicked a typical fuel processor, steam methane reformer outlet stream. The Pt/CeO2 catalyst showed the best metal activity of ~3.8 E-07 moles CO converted·gPt-1 s-1, at a Pt loading of 0.5 wt%, activity decreasing with increasing metal loading. Furthermore, the Pt/CeO2 catalyst produced almost no methane while the Rh based catalysts led to substantial methanation. |
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Keywords: | Water-gas shift Fuel processor High throughput PGM |
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