Prominent enhancement of Mn or Co addition on the performance of Cu-Ce-O catalyst used for H2 production via dimethyl ether steam reforming

The Mn or Co promoted Cu-Ce-O catalysts were prepared by citric acid complexation, and used for the catalytic production of hydrogen via the route of dimethyl ether steam reforming (DME SR). Multiple techniques such as X-ray diffraction (XRD), X-ray absorption fine structure (XAFS), X-ray photoelectron spectra (XPS), temperature-programmed reduction by H2 (H2-TPR), CO-pulse chemisorption and thermal gravimetry/differential thermal analysis (TG/DTA) were employed for catalyst characterization. It is revealed by the results of XRD, XPS and XAFS that in the spent catalysts the copper species mainly exist as Cu0 and Cu+. The addition of Co or Mn could enhance both the dispersion and the reducibility of copper species, significantly increasing the DME conversion and H2 yield at the temperature of 400 °C or below. At higher temperature, the H2 yield over Cu-Ce-Co-O is almost the same as that for Cu-Ce-O, due to the side reactions of CH3OH decomposition and/or DME steam reforming to syngas. Addition of Mn to Cu-Ce-O can increase both DME conversion and H2 yield in the whole temperature region of 300–450 °C. Much higher CO2 selectivity is achieved over the Mn promoted catalyst. XPS and CO-pulse chemisorption results indicate that Cu-Ce-Mn-O catalyst contains more Cu+ species, which determines its novel catalytic performance including higher DME conversion and higher H2 yield.

Graphical abstractFigure optionsDownload full-size imageDownload as PowerPoint slideHighlights► Co or Mn promoted Cu-Ce-O is much more active for DME steam reforming to produce H2. ► The main copper species in the catalysts are Cu0 and Cu+ during DME steam reforming. ► Addition of Co or Mn enhances the dispersion and reducibility of the copper species. ► Cu-Ce-Mn-O contains more Cu+ species, determining its better catalytic performance.