International Journal of Hydrogen Energy Journal
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.
For details: Water-gas shift of reformate streams over mono-metallic PGM catalysts
Stephen J. Roberts, Jack V. Fletcher, Yi Zhou, Niels T.J. Luchters, Jack C.Q. Fletcher
Catalysis Institute, Department of Chemical Engineering, University of Cape Town, Private Bag X3, Rondebosch, 7701, South Africa
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International Journal of Hydrogen Energy Journal
https://doi.org/10.1016/j.ijhydene.2018.01.193
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