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Challenges in scale-up of electrochemical CO2 reduction to formate integrated with product extraction using electrodialysis

Challenges in scale-up of electrochemical CO2 reduction to formate integrated with product extraction using electrodialysis
Challenges in scale-up of electrochemical CO2 reduction to formate integrated with product extraction using electrodialysis

BACKGROUND: The concept of carbon dioxide (CO2) conversion to formate has attracted increasing interest in recent years and various small-scale studies are present in the literature. However, upscaling of electrochemical CO2 reduction comes with many challenges and there are very few reports available on it. In this study, we present a scalable three-chamber reactor system for electrochemical CO2 reduction to formate, a precursor suitable for the production of fuels, pharmaceuticals and fertilizers and its extraction as pure formic acid by electrodialysis. RESULTS: The reactor produced 11.7 g L–1 formic acid in 6 h, i.e. 1.95 g L–1 h–1 at −1.8 V applied potential, 5 mol L–1 KOH as an electrolyte, GDE (gas diffusion electrode) cathode with SnO2 catalyst and Nafion™ 200 membrane. The maximum Faradaic efficiency achieved was 38%. In addition, recovery of the formate is equally important as its production for use as feedstock to form chemicals. We therefore also investigated the extraction of formic acid through conventional electrodialysis (CED) and bipolar membrane electrodialysis (BMED). The formic acid was extracted with 88% recovery using CED and 46% with BMED. Furthermore, BMED resulted in recovery of >95% K+ as base and 12 L pure CO2 for possible recycling to the electrochemical cell. CONCLUSION: We consider this study to provide essential empirical evidence on factors influencing the scale-up and subsequent performance of a liquid electrolyte-based electrochemical CO2 reduction reaction (CO2RR) system to formate and its extraction at scale. However, optimized systems and operating strategies still need further investigation, and constituent materials, particularly in terms of membranes and cathode catalyst, need to be developed.

CO reduction, electrochemical cell, electrodialysis, formate, KOH recovery, scale-up
0268-2575
2461-2471
Kaur, Amandeep
9418458f-ba40-43f9-b1f7-413183753cdc
Kim, Bongkyu
36df4cf2-8e8b-4c1b-bab2-2d3c5a427f73
Dinsdale, Richard
da945f14-84bf-4e51-83be-6b8487ac87f0
Guwy, Alan
9a3c71f6-1162-4436-8bb1-6077802dd4f3
Yu, Eileen
28e47863-4b50-4821-b80b-71fb5a2edef2
Premier, Giuliano
318775e0-df2e-4ee1-bbab-7100c0da3804
Kaur, Amandeep
9418458f-ba40-43f9-b1f7-413183753cdc
Kim, Bongkyu
36df4cf2-8e8b-4c1b-bab2-2d3c5a427f73
Dinsdale, Richard
da945f14-84bf-4e51-83be-6b8487ac87f0
Guwy, Alan
9a3c71f6-1162-4436-8bb1-6077802dd4f3
Yu, Eileen
28e47863-4b50-4821-b80b-71fb5a2edef2
Premier, Giuliano
318775e0-df2e-4ee1-bbab-7100c0da3804

Kaur, Amandeep, Kim, Bongkyu, Dinsdale, Richard, Guwy, Alan, Yu, Eileen and Premier, Giuliano (2021) Challenges in scale-up of electrochemical CO2 reduction to formate integrated with product extraction using electrodialysis. Journal of Chemical Technology and Biotechnology, 96 (9), 2461-2471. (doi:10.1002/jctb.6812).

Record type: Article

Abstract

BACKGROUND: The concept of carbon dioxide (CO2) conversion to formate has attracted increasing interest in recent years and various small-scale studies are present in the literature. However, upscaling of electrochemical CO2 reduction comes with many challenges and there are very few reports available on it. In this study, we present a scalable three-chamber reactor system for electrochemical CO2 reduction to formate, a precursor suitable for the production of fuels, pharmaceuticals and fertilizers and its extraction as pure formic acid by electrodialysis. RESULTS: The reactor produced 11.7 g L–1 formic acid in 6 h, i.e. 1.95 g L–1 h–1 at −1.8 V applied potential, 5 mol L–1 KOH as an electrolyte, GDE (gas diffusion electrode) cathode with SnO2 catalyst and Nafion™ 200 membrane. The maximum Faradaic efficiency achieved was 38%. In addition, recovery of the formate is equally important as its production for use as feedstock to form chemicals. We therefore also investigated the extraction of formic acid through conventional electrodialysis (CED) and bipolar membrane electrodialysis (BMED). The formic acid was extracted with 88% recovery using CED and 46% with BMED. Furthermore, BMED resulted in recovery of >95% K+ as base and 12 L pure CO2 for possible recycling to the electrochemical cell. CONCLUSION: We consider this study to provide essential empirical evidence on factors influencing the scale-up and subsequent performance of a liquid electrolyte-based electrochemical CO2 reduction reaction (CO2RR) system to formate and its extraction at scale. However, optimized systems and operating strategies still need further investigation, and constituent materials, particularly in terms of membranes and cathode catalyst, need to be developed.

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More information

e-pub ahead of print date: 30 May 2021
Additional Information: Publisher Copyright: © 2021 The Authors. Journal of Chemical Technology and Biotechnology published by John Wiley & Sons Ltd on behalf of Society of Chemical Industry (SCI).
Keywords: CO reduction, electrochemical cell, electrodialysis, formate, KOH recovery, scale-up

Identifiers

Local EPrints ID: 498920
URI: http://eprints.soton.ac.uk/id/eprint/498920
ISSN: 0268-2575
PURE UUID: 93495be1-aa47-4db6-8162-819ef3121a0e
ORCID for Eileen Yu: ORCID iD orcid.org/0000-0002-6872-975X

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Date deposited: 04 Mar 2025 18:08
Last modified: 05 Mar 2025 03:17

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Contributors

Author: Amandeep Kaur
Author: Bongkyu Kim
Author: Richard Dinsdale
Author: Alan Guwy
Author: Eileen Yu ORCID iD
Author: Giuliano Premier

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