Abstract
The performance of a СuO–ZnO/γ-Al2O3 catalyst for the reactions of methanol, dimethyl ether (DME) and dimethoxymethane (DMM) steam reforming (SR) to hydrogen-rich gas was studied. The catalyst was found to be active and selective for methanol and DMM SR producing hydrogen-rich gas with low content of CO (<1 vol %). It provided complete conversion of methanol and DMM at 300°C, and hydrogen productivity of, respectively, 15 and 16.5 LH2gcat -1h-1. With the use of physicochemical methods and catalytic experiments, it was shown that the catalyst surface contained the acid sites typical for γ-Al2O3, and CuO–ZnO agglomerates, responsible, respectively, for DMM hydration to methanol and formaldehyde, and SR of these compounds to hydrogen-rich gas.
Original language | English |
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Pages (from-to) | 577-584 |
Number of pages | 8 |
Journal | Kinetics and Catalysis |
Volume | 58 |
Issue number | 5 |
DOIs | |
Publication status | Published - Sep 2017 |
Keywords
- copper-zinc catalysts
- dimethyl ether
- dimetoxymethane
- fuel cells
- hydrogen
- methanol
- steam reforming
- PERFORMANCE
- COPPER
- CO
- HYDROGEN-RICH GAS
- METHANATION
- BIFUNCTIONAL CATALYSTS
- FUEL-CELL APPLICATIONS
- CU-BASED CATALYSTS