Abstract

The chemical conversion of CO2 into hydrocarbon fuels and chemicals using green hydrogen not only utilizes abundant CO2 as a carbon feedstock but also enables the storage of hydrogen. Herein, we investigate the direct hydrogenation of CO2 to gasoline and olefins over a series of bifunctional iron-zeolite tandem catalysts operated at high temperatures (> 300 ℃). This process may efficiently utilize CO2 discharged from industrial combustion and green H2 produced by solid oxide electrolytic cells (SOEC). The optimized FeMnK+H-ZSM-5 catalyst offers a 70% selectivity of C5−C11 range hydrocarbons together with a 17% selectivity of C2−C4 lower olefins at 320 °C. The CO2 conversion levels and the aromatics contents could be greatly enhanced as the temperature increases from 320 ℃ to 400 ℃. The hydrocarbon distribution is mainly determined by the micropore size of the zeolites. The dynamic evolution of bifunctional catalysts and its impact on bifunctional catalysis was systematically investigated.

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