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Electrodes Designed for Converting Bicarbonate into CO
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DOI：10.1021/acsenergylett.0c00898.png)
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Abstract
En 中文
The deployment of electrolyzers that convert CO2 into chemicals and fuels requires appropriate integration with upstream carbon capture processes. To this end, the electrolytic conversion of aqueous (bi)carbonate offers the opportunity to avoid the energy-intensive steps currently used to extract pressurized CO, from carbon capture solutions. We demonstrate here that an optimized silver gas diffusion electrode (GDE) architecture enables conversion of model carbon capture solutions (i.e., 3 M KHCO3) into CO at partial current densities (J(CO)) greater than 100 mA cm(-2) with CO2 utilization rates of similar to 70%. These results exceed the performance of any previously reported liquid-fed CO(2)( )electrolyzers and rival gas-fed devices. We were able to hit these metrics through the systematic design of gas diffusion layer (GDL) components (e.g., polytetrafluoroethylene) and catalyst layer constituents (i.e., Nafion, silver) on CO production. A key finding of this work is that hydrophobic GDE components (which are common to gas-fed CO2RR electrolyzers) decrease in situ CO2 generation and thus the formation of the final CO product. These findings show a clear path toward industrially relevant reactors that couple electrolytic CO2 conversion with carbon capture.
Keywords:
GAS-DIFFUSION ELECTRODES
CARBON-DIOXIDE REDUCTION
BIPOLAR MEMBRANES
CATALYST LAYER
ELECTROLYSIS
NAFION
FUEL
CAPTURE
CELL
ELECTROREDUCTION
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