Abstract
A two-step tandem electrochemical-thermochemical reaction scheme is demonstrated to convert CO2into value-added C3oxygenate molecules: CO2was electrochemically reduced to ethylene, CO, and H2, followed by the thermochemical hydroformylation reaction to produce 1-propanol and propanal. The CO2electrolyzer was evaluated with Cu catalysts containing different oxidation states and with modifications to the gas diffusion layer hydrophobicity, while the hydroformylation reactor was tested over a Rh1Co3/MCM-41 catalyst. In situ X-ray absorption spectroscopy showed minimal changes to the Cu and Rh catalysts in the electrochemical and thermochemical reactions, respectively. The tandem configuration achieved a total C3oxygenate product selectivity (on a basis of reduced CO2) of ∼18%, representing over a 4-fold improvement compared to direct electrochemical CO2conversion to 1-propanol in flow cells. Additionally, the CO2electrolyzer was scaled to a 25 cm2device to enhance the C3oxygenate production rate up to 11.8 μmol min-1and demonstrate potential scalability of the tandem system.
| Original language | English |
|---|---|
| Pages (from-to) | 2904-2910 |
| Number of pages | 7 |
| Journal | ACS Energy Letters |
| Volume | 7 |
| Issue number | 9 |
| DOIs | |
| State | Published - Sep 9 2022 |
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