The purpose of this study was to investigate the effect of the preparation method on CeO2-promoted Cu/γ -Al2O3 catalysts for the high temperature shift reaction using simulated waste-derived syngas (H2 + CO). To investigate the effect of preparation method on the CeO2-promoted Cu/γ-Al2O3 catalyst, we compared catalytic performance over Ce/Cu/γ-Al2O3, Ce-Cu/γ-Al2O3, Cu/Ce/γ-Al2O3, and Cu/γ-Al2O3 catalysts, and tried to explain the differences in catalytic performance with various characterization methods. The physico-chemical properties of the CeO2-promoted catalysts were characterized using surface spectroscopies such as BET, XRD, TPR, XPS, Raman spectroscopy, photoluminescence spectroscopy, and N2O-chemisorption. The catalyst characterizations were correlated with activity results in the high temperature shift reaction.

Magnetite (Fe3O4) has been prepared directly to avoid the reduction process prior to the H2 production from the high temperature water gas shift reaction of the simulated waste derived synthesis gas. Citric acid has been employed as a complexing agent for the direct synthesis of magnetite. Notably, without the reduction process, the catalyst prepared at the citric acid molar ratio of 1.0 showed 80% CO conversion at 350℃ at a gas hourly space velocity of 40,057 h-1.