2022
DOI: 10.1016/j.jcou.2021.101823
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Producing formic acid at low pH values by electrochemical CO2 reduction

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Cited by 32 publications
(15 citation statements)
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“…During CPE, H + was rapidly consumed by CO 2 RR, which may result in a locally higher pH microenvironment by diffusion limitation from porous confinement. [ 25 ] The higher pH microenvironment is significant to obtain high selectivity of acidic CO 2 RR, [ 6a,26 ] allowing high performance of TDPE‐PPSU at pH 1.8.…”
Section: Resultsmentioning
confidence: 99%
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“…During CPE, H + was rapidly consumed by CO 2 RR, which may result in a locally higher pH microenvironment by diffusion limitation from porous confinement. [ 25 ] The higher pH microenvironment is significant to obtain high selectivity of acidic CO 2 RR, [ 6a,26 ] allowing high performance of TDPE‐PPSU at pH 1.8.…”
Section: Resultsmentioning
confidence: 99%
“…[ 5 ] According to the Pourbaix diagram, the turning point for CO 2 RR to FA/formate is located at pH 3.77, corresponding to the p K a of FA. [ 6 ] Utilizing acidic conditions below pH 3.77 could directly generate FA, overcoming the carbonation problem. However, when pH is sufficiently low, HER can quickly become kinetically dominant, [ 6a ] causing low Faradaic efficiency of FA.…”
Section: Introductionmentioning
confidence: 99%
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“…However, abundant H + /H 3 O + at the cathode will promote the competing HER in an acidic environment (similar to the CSA-MEA configuration with acid crossover), thereby reducing the FE of the CO 2 RR. Advanced catalyst and/or reaction system design that can suppress the HER under acidic conditions, such as by using a catholyte with a high concentration of alkali cations, is highly desired to further improve the efficiency of the CO (2) RR. …”
Section: Flow Cell Design and Developmentmentioning
confidence: 99%
“…Generally, the CO 2 RR yields formic acid operating at acidic conditions below the pKa of formic acid (3.8) and formate productions at highly alkaline electrolyte systems (pH > 8). [87] Some excellent reviews also have summarized the state-of-art electrocatalysts for electrocatalytic conversion of CO 2 into formic acid/formate. [35,42,88] Nevertheless, it is also critical to obtain highly concentrated formic acid/formate from CO 2 RR, as a highconcentration liquid product in downstream separation processes will require low energy consumption, thereby compromising the overall CO 2 RR economic feasibility.…”
Section: Introductionmentioning
confidence: 99%