2021
DOI: 10.1016/j.xcrp.2021.100353
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Achieving high current density for electrocatalytic reduction of CO2 to formate on bismuth-based catalysts

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Cited by 51 publications
(56 citation statements)
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“…In gas-fed electrolyzers the rate of CO 2 RR is not limited by slow CO 2 mass transport, and as a consequence, much higher applied overpotentials (or current densities) can be achieved, while still maintaining high formate selectivity. [54][55]58 In the present study, we demonstrate that an accelerated mass transport of gaseous CO 2 not only boosts the formate production to values beyond PCD formate = -1 A cm -2 but can also lead to a substantial stabilization of subcarbonate phases beyond the stability regime observed in classical CO 2 RR test environments. 38 Our experimental results strongly suggest that observations previously made using H-type cell configurations cannot simply be transferred to experimental conditions realized in practical gas-fed electrolyzers.…”
Section: Introductionsupporting
confidence: 52%
“…In gas-fed electrolyzers the rate of CO 2 RR is not limited by slow CO 2 mass transport, and as a consequence, much higher applied overpotentials (or current densities) can be achieved, while still maintaining high formate selectivity. [54][55]58 In the present study, we demonstrate that an accelerated mass transport of gaseous CO 2 not only boosts the formate production to values beyond PCD formate = -1 A cm -2 but can also lead to a substantial stabilization of subcarbonate phases beyond the stability regime observed in classical CO 2 RR test environments. 38 Our experimental results strongly suggest that observations previously made using H-type cell configurations cannot simply be transferred to experimental conditions realized in practical gas-fed electrolyzers.…”
Section: Introductionsupporting
confidence: 52%
“…Considering that the current density cannot reach 200 mA cm -2 in a traditional H-type cell, we designed a flow cell with a gas diffusion electrode (GDE) as depicted in Figure 6a and Figure S34, Supporting Information. [29] The GDE can reduce the mass transfer resistance by accelerating the CO 2 diffusion rate on the cathode surface, thereby increasing the current density of the CO 2 RR process. [30] LSV and chronopotentiometry measurements were conducted to evaluate the catalytic performance of the three catalysts in 1 m KOH electrolyte, and the solution resistance (Rs) and iR compensation of flow cell were given in Table S6, Supporting Information.…”
Section: Flow Cell Performancementioning
confidence: 99%
“…Weekes et al 222 and Endrődi et al 223 discussed the role of cell architecture in the electroreduction of CO2, while more detailed aspects are out of the scope as well as the analysis of the recent development in electrocatalytic CO2 reduction, which for formate production from CO2 reached recently extremely high current densities (~930 mA•cm -2 ) with high Faradaic efficiency (FEHCOO-= 93%) on defective Bi2O2CO3 nanosheets. 227 While thus high J and FE are possible in the electrocatalytic approach (with an external source of potential and electrical current), the direct integration of a photoactive element in the device (photoanode, PV cell) allows largely lower J values, although with other advantages as earlier discussed.…”
Section: The Case Of Co2mentioning
confidence: 97%