The utilization of CO2 provides a decarbonization pathway for hard-to-abate emissions, with solid-oxide and low-temperature electrochemical CO2 conversion offering routes to value-added chemicals. Unfortunately, CO2 sources are dilute and contain reactive impurities (NOx/SOx/O2) that influence electrolyzer performance. Research has then focused on understanding the implications of impurities on operation and designing catalyst structures that tolerate impure feeds. High feed tolerances would be promising as electrolyzers could then be co-located with point-source emissions and avoid pre-processing. However, electrolyzers operated with dilute or impurity-tolerant feeds merely transfer separation burdens downstream. Sulfur limits for methanol or FischerTropsch synthesis are more stringent than the electrolysis step, while separating CO/N2 downstream is more complex than separating CO2/N2 upstream. Last, post-electrolysis oxygen impurities may pose flammability risks with by-product H2. In this perspective, we critically examine CO2 feedstocks and invoke a higher-level discussion reflecting where reactive impurities should be addressed in the electrochemical value chain

Where to Address N2 and Reactive Impurities in the CO2 Electrochemical Value Chain? / Gatti, L., Mezza, A., Sacco, A., Thomas, B.. - In: JOULE. - ISSN 2542-4351. - (2026), pp. 1-11.

Where to Address N2 and Reactive Impurities in the CO2 Electrochemical Value Chain?

Gatti, Laura;Mezza, Alessio;Sacco, Adriano;
2026

Abstract

The utilization of CO2 provides a decarbonization pathway for hard-to-abate emissions, with solid-oxide and low-temperature electrochemical CO2 conversion offering routes to value-added chemicals. Unfortunately, CO2 sources are dilute and contain reactive impurities (NOx/SOx/O2) that influence electrolyzer performance. Research has then focused on understanding the implications of impurities on operation and designing catalyst structures that tolerate impure feeds. High feed tolerances would be promising as electrolyzers could then be co-located with point-source emissions and avoid pre-processing. However, electrolyzers operated with dilute or impurity-tolerant feeds merely transfer separation burdens downstream. Sulfur limits for methanol or FischerTropsch synthesis are more stringent than the electrolysis step, while separating CO/N2 downstream is more complex than separating CO2/N2 upstream. Last, post-electrolysis oxygen impurities may pose flammability risks with by-product H2. In this perspective, we critically examine CO2 feedstocks and invoke a higher-level discussion reflecting where reactive impurities should be addressed in the electrochemical value chain
2026
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11583/3013523