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  • Perspective
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Scaling and heating will drive low-temperature CO2 electrolysers to operate at higher temperatures

Abstract

Low-temperature carbon dioxide electrolysis (CO2E) provides a one-step means of converting CO2 into carbon-based fuels using electrical inputs at temperatures below 100 °C. Over the past decade, an abundance of work has been carried out at ambient temperature, and high CO2E rates and product selectivities have been achieved. With scaling of CO2E technologies underway, greater discourse surrounding heat management and the viable operating temperatures of larger systems is important. In this Perspective we argue that, owing to the energy inefficiency of electrolysers, heat generation in CO2E stacks will favour operating temperatures of between 40 and 70 °C, far from the ambient temperatures used so far. Such elevated temperatures put further pressure on catalyst and membrane stability and on the stack design. On the other hand, elevated temperatures could alleviate challenges in salt precipitation, water management and high cell voltages, aiding the technology. We reflect on these aspects and discuss the opportunities for waste heat valorization to increase the economic feasibility of the process.

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Fig. 1: Heat balance analysis for CO2E stack.
Fig. 2: Operable temperature range and single-pass spatial temperature gradient.
Fig. 3: Effect of temperature on relevant system properties.
Fig. 4: Heat recuperation and impact on achievable process efficiencies.

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References

  1. Barecka, M. H. & Ager, J. W. Towards an accelerated decarbonization of the chemical industry by electrolysis. Energy Adv. 2, 268–279 (2023).

    Article  Google Scholar 

  2. Segets, D., Andronescu, C. & Apfel, U.-P. Accelerating CO2 electrochemical conversion towards industrial implementation. Nat. Commun. 14, 7950 (2023).

    Article  Google Scholar 

  3. Burdyny, T. & Mulder, F. M. Scale-up of CO2 and CO electrolyzers. Joule 8, 2449–2452 (2024).

    Article  Google Scholar 

  4. Petrov, K. V. et al. Bipolar membranes for intrinsically stable and scalable CO2 electrolysis. Nat. Energy https://doi.org/10.1038/s41560-024-01574-y (2024).

    Article  Google Scholar 

  5. Ozden, A. et al. Energy- and carbon-efficient CO2/CO electrolysis to multicarbon products via asymmetric ion migration–adsorption. Nat. Energy 8, 179–190 (2023).

    Article  Google Scholar 

  6. Reichbauer, T. et al. Electrical energy input efficiency limitations in CO2-to-CO electrolysis and attempts for improvement. Electrochem. Sci. Adv. 4, e2300024 (2024).

    Article  Google Scholar 

  7. Endrődi, B. et al. High carbonate ion conductance of a robust PiperION membrane allows industrial current density and conversion in a zero-gap carbon dioxide electrolyzer cell. Energy Environ. Sci. 13, 4098–4105 (2020).

    Article  Google Scholar 

  8. Technical targets for proton exchange membrane electrolysis. US Department of Energy (accessed 20 March 2025); https://www.energy.gov/eere/fuelcells/technical-targets-proton-exchange-membrane-electrolysis

  9. Giron Rodriguez, C. A. et al. Insights into zero-gap CO2 electrolysis at elevated temperatures. EES Catal. 2, 850–861 (2024).

    Article  Google Scholar 

  10. Vos, R. E. et al. How temperature affects the selectivity of the electrochemical CO2 reduction on copper. ACS Catal. 13, 8080–8091 (2023).

    Article  Google Scholar 

  11. Schellekens, M. P., Raaijman, S. J., Koper, M. T. M. & Corbett, P. J. Temperature-dependent selectivity for CO electroreduction on copper-based gas-diffusion electrodes at high current densities. Chem. Eng. J. 483, 149105 (2024).

    Article  Google Scholar 

  12. Krause, R. et al. Industrial application aspects of the electrochemical reduction of CO2 to CO in aqueous electrolyte. Chem. Ing. Tech. 92, 53–61 (2020).

    Article  Google Scholar 

  13. Quentmeier, M., Schmid, B., Tempel, H. & Eichel, R.-A. Modular CO2-to-CO electrolysis short-stack design—impact of temperature gradients and insights into position-dependent cell behavior. ACS Sustain. Chem. Eng. 12, 3876–3885 (2024).

    Article  Google Scholar 

  14. Crandall, B. S. et al. Kilowatt-scale tandem CO2 electrolysis for enhanced acetate and ethylene production. Nat. Chem. Eng. 1, 421–429 (2024).

    Article  Google Scholar 

  15. Wakerley, D. et al. Gas diffusion electrodes, reactor designs and key metrics of low-temperature CO2 electrolysers. Nat. Energy 7, 130–143 (2022).

    Article  Google Scholar 

  16. Lees, E. W., Mowbray, B. A. W., Parlane, F. G. L. & Berlinguette, C. P. Gas diffusion electrodes and membranes for CO2 reduction electrolysers. Nat. Rev. Mater. 7, 55–64 (2022).

    Article  Google Scholar 

  17. Iglesias van Montfort, H.-P. et al. An advanced guide to assembly and operation of CO2 electrolyzers. ACS Energy Lett. 8, 4156–4161 (2023).

    Article  Google Scholar 

  18. Kibria, M. G. et al. Electrochemical CO2 reduction into chemical feedstocks: from mechanistic electrocatalysis models to system design. Adv. Mater. 31, 1807166 (2019).

    Article  Google Scholar 

  19. Weng, L.-C., Bell, A. T. & Weber, A. Z. Towards membrane-electrode assembly systems for CO2 reduction: a modeling study. Energy Environ. Sci. 12, 1950–1968 (2019).

    Article  Google Scholar 

  20. Hansen, K. U., Cherniack, L. H. & Jiao, F. Voltage loss diagnosis in CO2 electrolyzers using five-electrode technique. ACS Energy Lett. 7, 4504–4511 (2022).

    Article  Google Scholar 

  21. Garg, S., Giron Rodriguez, C. A., Rufford, T. E., Varcoe, J. R. & Seger, B. How membrane characteristics influence the performance of CO2 and CO electrolysis. Energy Environ. Sci. 15, 4440–4469 (2022).

    Article  Google Scholar 

  22. Incropera, F. P., DeWitt, D. P., Bergman, T. L. & Lavine, A. S. Fundamentals of Heat and Mass Transfer 6th edn (Wiley, 2007).

  23. Wijaya, G. H. A., Im, K. S. & Nam, S. Y. Advancements in commercial anion exchange membranes: a review of membrane properties in water electrolysis applications. Desalin. Water Treat. 320, 100605 (2024).

    Article  Google Scholar 

  24. Industrial Cooling Systems (Callens, accessed 19 September 2024); https://www.callens.eu/en/air-technology/industrial-cooling

  25. Mokhatab, S., Poe, W. A. & Mak, J. Y. in Handbook of Natural Gas Transmission and Processing: Principles and Practices 537–578 (Elsevier, 2019); https://doi.org/10.1016/B978-0-12-815817-3.00018-6

  26. Toghyani, S., Afshari, E., Baniasadi, E. & Atyabi, S. A. Thermal and electrochemical analysis of different flow field patterns in a PEM electrolyzer. Electrochim. Acta 267, 234–245 (2018).

    Article  Google Scholar 

  27. Rossen, A., Daems, N., Choukroun, D. & Breugelmans, T. Differential pressure across a gas diffusion electrode controls efficiency of liquid-fed electrolyzers for CO2 electroreduction at elevated temperatures. ACS Sustain. Chem. Eng. https://doi.org/10.1021/acssuschemeng.4c01908 (2024).

    Article  Google Scholar 

  28. Deng, X., Yang, F., Li, Y., Dang, J. & Ouyang, M. Quantitative study on gas evolution effects under large current density in zero-gap alkaline water electrolyzers. J. Power Sources 555, 232378 (2023).

    Article  Google Scholar 

  29. Belsa, B. et al. Materials challenges on the path to gigatonne CO2 electrolysis. Nat. Rev. Mater. https://doi.org/10.1038/s41578-024-00696-9 (2024).

    Article  Google Scholar 

  30. Moss, A. B. et al. In operando investigations of oscillatory water and carbonate effects in MEA-based CO2 electrolysis devices. Joule 7, 350–365 (2023).

    Article  Google Scholar 

  31. Disch, J. et al. High-resolution neutron imaging of salt precipitation and water transport in zero-gap CO2 electrolysis. Nat. Commun. 13, 6099 (2022).

    Article  Google Scholar 

  32. Joensen, B. Ó. et al. Unveiling transport mechanisms of cesium and water in operando zero-gap CO2 electrolyzers. Joule https://doi.org/10.1016/j.joule.2024.02.027 (2024).

    Article  Google Scholar 

  33. Sisler, J. et al. Ethylene electrosynthesis: a comparative techno-economic analysis of alkaline vs membrane electrode assembly vs CO2–CO–C2H4 tandems. ACS Energy Lett. 6, 997–1002 (2021).

    Article  Google Scholar 

  34. García De Arquer, F. P. CO2 electrolysis to multicarbon products at activities greater than 1 A cm−2. Science 367, 661–666 (2020).

    Article  Google Scholar 

  35. Nesbitt, N. T. et al. Liquid–solid boundaries dominate activity of CO2 reduction on gas-diffusion electrodes. ACS Catal. 10, 14093–14106 (2020).

    Article  Google Scholar 

  36. Biemolt, J., Singh, J., Prats Vergel, G., Pelzer, H. M. & Burdyny, T. Preventing salt formation in zero-gap CO2 electrolyzers by quantifying cation accumulation. ACS Energy Lett. 10, 807–814 (2025).

    Article  Google Scholar 

  37. Nesbitt, N. T. & Smith, W. A. Water and solute activities regulate CO2 reduction in gas-diffusion electrodes. J. Phys. Chem. C 125, 13085–13095 (2021).

    Article  Google Scholar 

  38. Zhang, H., Gao, J., Raciti, D. & Hall, A. S. Promoting Cu-catalysed CO2 electroreduction to multicarbon products by tuning the activity of H2O. Nat. Catal. 6, 807–817 (2023).

    Article  Google Scholar 

  39. Luo, X., Rojas-Carbonell, S., Yan, Y. & Kusoglu, A. Structure–transport relationships of poly(aryl piperidinium) anion-exchange membranes: effect of anions and hydration. J. Membr. Sci. 598, 117680 (2020).

    Article  Google Scholar 

  40. Wheeler, D. G. et al. Quantification of water transport in a CO2 electrolyzer. Energy Environ. Sci. 13, 5126–5134 (2020).

    Article  Google Scholar 

  41. Hurkmans, J.-W., Pelzer, H. M., Burdyny, T., Peeters, J. & Vermaas, D. A. Heating dictates the scalability of CO2 electrolyzer types. EES Catal. https://doi.org/10.1039/D4EY00190G (2025)

  42. Jensen, J. K. et al. Heat pump COP, part 2: generalized COP estimation of heat pump processes. In Proc. 13th IIR Gustav Lorentzen Conference on Natural Refrigerants (GL2018) (International Institute of Refrigeration, 2018); https://doi.org/10.18462/IIR.GL.2018.1386

  43. Siegmund, D. et al. Crossing the valley of death: from fundamental to applied research in electrolysis. JACS Au 1, 527–535 (2021).

    Article  Google Scholar 

  44. Garg, S. et al. How alkali cations affect salt precipitation and CO2 electrolysis performance in membrane electrode assembly electrolyzers. Energy Environ. Sci. 16, 1631–1643 (2023).

    Article  Google Scholar 

  45. Solubility Table for Water at Temperature (Merck, accessed 10 September 2024); https://www.sigmaaldrich.com/NL/en/support/calculators-and-apps/solubility-table-compounds-water-temperature

  46. Sustainion® Anion Exchange Membranes (Dioxide Materials, accessed 11 September 2024); https://dioxidematerials.com/technology/sustainion-membranes/

  47. Vaughan, G. L. & Carrington, C. G. Psychrometric properties of a moist carbon dioxide atmosphere. Int. J. Food Prop. 1, 77–87 (1998).

    Article  Google Scholar 

  48. Zheng, Y. et al. Energy related CO2 conversion and utilization: advanced materials/nanomaterials, reaction mechanisms and technologies. Nano Energy 40, 512–539 (2017).

    Article  Google Scholar 

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Acknowledgements

This project received funding from project “e-Heat: Understanding and controlling heat to enable large scale electrolysers” (NWO OTP 19757).

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Conceptualization was by H.M.P., D.V. and T.B. Visualization was by H.M.P., N.K., D.V. and T.B. The original draught was written by H.M.P., N.K., D.V. and T.B., and the manuscript was reviewed and edited by H.M.P., D.V. and T.B. Funding acquisition was by D.V. and T.B.

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Correspondence to Henri M. Pelzer or Thomas Burdyny.

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Nature Energy thanks Feng Jiao, Guenter Schmid and the other, anonymous, reviewer(s) for their contribution to the peer review of this work.

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Pelzer, H.M., Kolobov, N., Vermaas, D.A. et al. Scaling and heating will drive low-temperature CO2 electrolysers to operate at higher temperatures. Nat Energy 10, 549–556 (2025). https://doi.org/10.1038/s41560-025-01745-5

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