The Cu Promoter in an Iron−Chromium−Oxide Based Water−Gas Shift

Aug 25, 2010 - Iron-Based Catalysts for the High-Temperature Water–Gas Shift (HT-WGS) ... Catalytic CO 2 gasification of a Powder River Basin coal...
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15410

J. Phys. Chem. C 2010, 114, 15410–15416

The Cu Promoter in an Iron-Chromium-Oxide Based Water-Gas Shift Catalyst under Industrial Conditions Studied by in-Situ XAFS Anna Puig-Molina, Fernando Morales Cano, and Ton V. W. Janssens* Haldor Topsøe A/S, NymølleVej 55, DK-2800 Lyngby, Denmark ReceiVed: April 19, 2010; ReVised Manuscript ReceiVed: July 30, 2010

The chemical state of the Cu promoter (1 wt %) in a Cu-promoted Cr-stabilized iron oxide based water-gas shift catalyst has been studied by in-situ X-ray absorption fine structure (XAFS) at 380 °C and elevated pressures, which is close to the conditions typically applied in industrial processes. The Cu promoter enhances the activity of the catalyst. In this study, the catalyst has been studied as fresh, after use for 2000 h, and after a further wash with an aqueous solution of ammonia. In all three cases, CuO and CuFe2O4-like phases are present; the used catalyst also contains some metallic Cu. X-ray absorption spectroscopy (XAS) shows that upon exposure to a typical feed gas for high-temperature shift containing CO, CO2, H2, and water, both the CuO and the CuFe2O4-phases are reduced to metallic Cu at 250 °C; Cr is present as Cr3+ and is slowly incorporated in the Fe3O4 matrix upon further heating to 380 °C and pressurizing to 12 or 24 bar. Washing a used catalyst with an aqueous solution of ammonia primarily removes the metallic Cu but also some CuO and CuFe2O4. Despite the fact that the Cu content in the catalyst after washing with ammonia varies, the activity is the same as that for the unwashed and fresh catalysts. This indicates that only a smaller part, estimated to