Enabling Stable and Salt-Free Formic Acid Production via Reactive Interface Optimization in Forward-Bias Bipolar-Membrane CO <sub>2</sub> Electrolyzers

High Resolution Image Download MS PowerPoint Slide Electrochemical conversion of CO 2 to liquid products is limited by parasitic reactions that consume products and destabilize operation. Here, we show that salt-free formic acid synthesis in a forward-bias bipolar-membrane CO 2 electrolyzer is governed by a coupled reaction-transport instability driven by parasitic anode formic acid oxidation. Operando mass spectrometry reveals that this process proceeds through CO-mediated poisoning, identifying catalyst tolerance to CO as a key descriptor of anode selectivity. Among the catalysts examined, PtRu/C preferentially promotes hydrogen oxidation over formic acid oxidation. Coupling this catalyst with transport-interface engineering improves product removal, enhances Faradaic and energy efficiency, and enables stable operation at 200 mA/cm 2 for 190 h with a voltage decay of 0.64 mV/h. Techno-economic analysis indicates an 18% reduction in minimum selling price and highlights product concentration as the dominant cost lever. These results establish a general framework for suppressing product oxidation in liquid-product electrolyzers.

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Publication Details

Journal
ACS Energy Letters
Published
2026-06-30
DOI
https://doi.org/10.1021/acsenergylett.6c00932
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
0.00

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article

Enabling Stable and Salt-Free Formic Acid Production via Reactive Interface Optimization in Forward-Bias Bipolar-Membrane CO 2 Electrolyzers

K.C. Neyerlin, Arthur Jeremy Kropf, Carly Byron, Fry Intia et al.
ACS Energy Letters
CO2 Reduction Techniques and Catalysts
article

Enabling Stable and Salt-Free Formic Acid Production via Reactive Interface Optimization in Forward-Bias Bipolar-Membrane CO 2 Electrolyzers

K.C. Neyerlin, Arthur Jeremy Kropf, Carly Byron, Fry Intia, Magali Ferrandon, Leiming Hu, I. Berry, Jacob A. Wrubel, James L. Young, Deborah J. Myers, David A. Cullen, Recep Kaş, Zhe Huang, Carlos Baez-Cotto, Matthew E. Sweers, Kimberly S. Reeves, Luke Cherniack, Piyush Kumar
article en

Abstract

High Resolution Image Download MS PowerPoint Slide Electrochemical conversion of CO 2 to liquid products is limited by parasitic reactions that consume products and destabilize operation. Here, we show that salt-free formic acid synthesis in a forward-bias bipolar-membrane CO 2 electrolyzer is governed by a coupled reaction-transport instability driven by parasitic anode formic acid oxidation. Operando mass spectrometry reveals that this process proceeds through CO-mediated poisoning, identifying catalyst tolerance to CO as a key descriptor of anode selectivity. Among the catalysts examined, PtRu/C preferentially promotes hydrogen oxidation over formic acid oxidation. Coupling this catalyst with transport-interface engineering improves product removal, enhances Faradaic and energy efficiency, and enables stable operation at 200 mA/cm 2 for 190 h with a voltage decay of 0.64 mV/h. Techno-economic analysis indicates an 18% reduction in minimum selling price and highlights product concentration as the dominant cost lever. These results establish a general framework for suppressing product oxidation in liquid-product electrolyzers.

ACS Energy Letters
Argonne National Laboratory (US), Oak Ridge National Laboratory (US), Center for NanoScience (DE), Museum of the Rockies (US), Catalytic Materials (United States) (US), Center for Nanophase Materials Sciences
U.S. Department of Energy, University of Chicago, Office of Fossil Energy, Office of Science, Office of Energy Efficiency and Renewable Energy, Office of Nuclear Energy, Division of Materials Research, Argonne National Laboratory, National Renewable Energy Laboratory
Openalex Percentile: Top 20%
CO2 Reduction Techniques and Catalysts
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