Acidic Electroreduction of CO2 to Multi-Carbon Products with CO2 Recovery and Recycling from Carbonate
Source abstract
Abstract
High Resolution Image Download MS PowerPoint Slide Gas-fed flow cells can facilitate high-rate electrochemical CO 2 reduction (CO 2 R). However, under alkaline and neutral conditions, CO 2 is lost through reaction with hydroxide ions to form (bi)carbonate. In acidic solutions, although (bi)carbonate is still formed due to increased pH at the electrode, the low bulk pH of the electrolyte solution can regenerate CO 2 which is then available for re-reaction or release─this therefore avoids permanent CO 2 loss. Here, we show how CO 2 is converted and released in a bipolar-membrane-based gas-fed flow cell for CO 2 R to multicarbon products (C 2+ faradaic efficiency >60%) employing an acidic catholyte. Under the highest conversion conditions, we showed that almost exclusively CO 2 R products were obtained at one outlet, while, at the second outlet, a nearly product-free stream of CO 2 was obtained due to the continuous internal regeneration from (bi)carbonate. The system presented here avoids permanent reactant loss through the straightforward recovery and recycling of CO 2 to improve the overall CO 2 utilization.
Source: openalex_inverted_index · Quality: baseline
Research context
OpenAlex topics: CO2 Reduction Techniques and Catalysts · Ionic liquids properties and applications · Carbon dioxide utilization in catalysis
SciVX discovery tags are terminology-based. OpenAlex topics are source-provided classifications.
Affiliations
Laboratoire de Chimie des Processus Biologiques, CNRS UMR 8229, Collège de France, 75231 Paris, France
School of Chemical and Physical Sciences, Keele University, Staffordshire ST5 5BG, U.K.
Total Research and Technology, Refining and Chemicals, Division CO2 Conversion, Feluy, 7181 Seneffe, Belgium
Funding
Total
References (35)
Show source-provided references
1. 10.1021/acsenergylett.0c0261010.1021/acsenergylett.0c02610 ↗
2. 10.1002/aenm.20200265210.1002/aenm.202002652 ↗
3. 10.1126/science.aay421710.1126/science.aay4217 ↗
4. 10.1002/anie.20220627910.1002/anie.202206279 ↗
5. 10.1002/adma.20180311110.1002/adma.201803111 ↗
6. 10.1021/acsenergylett.9b0150910.1021/acsenergylett.9b01509 ↗
7. 10.1016/j.jpowsour.2015.09.12410.1016/j.jpowsour.2015.09.124 ↗
8. 10.1038/s41467-020-19135-810.1038/s41467-020-19135-8 ↗
9. 10.1039/D0EE00047G10.1039/D0EE00047G ↗
10. 10.1016/j.joule.2021.01.00710.1016/j.joule.2021.01.007 ↗
11. 10.1126/science.abg658210.1126/science.abg6582 ↗
12. 10.1038/s41929-022-00788-110.1038/s41929-022-00788-1 ↗
13. 10.1038/s41929-022-00761-y10.1038/s41929-022-00761-y ↗
14. 10.1021/jacs.9b0700010.1021/jacs.9b07000 ↗
15. 10.1021/acsenergylett.2c0289710.1021/acsenergylett.2c02897 ↗
16. 10.1021/acsenergylett.6b0055710.1021/acsenergylett.6b00557 ↗
17. 10.1002/celc.20210074210.1002/celc.202100742 ↗
18. 10.1038/s41557-020-00602-010.1038/s41557-020-00602-0 ↗
19. 10.1038/s41467-022-31295-310.1038/s41467-022-31295-3 ↗
20. 10.1039/D0SC03047C10.1039/D0SC03047C ↗
21. 10.1021/acsenergylett.1c0205810.1021/acsenergylett.1c02058 ↗
22. 10.1021/jacs.1c1302410.1021/jacs.1c13024 ↗
23. 10.1021/acsenergylett.1c0193710.1021/acsenergylett.1c01937 ↗
24. 10.1016/S0167-577X(01)00361-510.1016/S0167-577X(01)00361-5 ↗
25. 10.1038/s41929-021-00655-510.1038/s41929-021-00655-5 ↗
26. 10.1038/s41467-021-24936-610.1038/s41467-021-24936-6 ↗
27. 10.1021/acscatal.9b0474610.1021/acscatal.9b04746 ↗
28. 10.1021/acsenergylett.2c0110610.1021/acsenergylett.2c01106 ↗
29. 10.1021/acsenergylett.1c0112210.1021/acsenergylett.1c01122 ↗
30. 10.1016/j.joule.2019.07.02110.1016/j.joule.2019.07.021 ↗
31. 10.1016/0011-9164(93)80183-N10.1016/0011-9164(93)80183-N ↗
32. 10.1016/j.memsci.2020.11853810.1016/j.memsci.2020.118538 ↗
33. 10.1038/s41467-022-31429-710.1038/s41467-022-31429-7 ↗
34. 10.1126/science.aaz148710.1126/science.aaz1487 ↗
35. 10.1021/acsenergylett.1c0226310.1021/acsenergylett.1c02263 ↗