From Flue Gas to Syngas: Composite Electrode Based on Ionic Liquid and Microporous Polymer for MEA‐Based CO<sub>2</sub> Electrolysis

H Hesamoddin Rabiee (Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland) A Abhijit Dutta (Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland) P Penghui Yan (School of Chemical Engineering The University of Queensland Brisbane QLD 4072 Australia) L Lei Ge F Fatereh Dorosti (School of Chemical Engineering The University of Queensland Brisbane QLD 4072 Australia) X Xin Yu (BGI Research, Qingdao, China.) A Alain Rieder (Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland) P Peter Broekmann (Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland)

Abstract

AbstractThe electrochemical CO2 reduction reaction (ECO2R) offers a promising pathway to convert CO2 into value‐added products. While catalyst advances remain crucial, gas‐diffusion electrodes (GDEs) architecture is equally vital in CO2 electrolyzer design. Most ECO2R studies use pure CO2 feeds, whereas industrial sources like flue gas contain ∼15% CO2, requiring costly purification. Eliminating this step demands electrolyzers that directly process impure streams via in situ separation. Here, we introduce a composite GDE (CGDE) featuring a thin CO2‐selective interlayer of intrinsically microporous polymer (PIM‐1) reinforced with the CO2‐philic ionic liquid [Emim][BF4]. This layer selectively adsorbs CO2 and suppresses N2/O2 existence at the catalyst interface. In simulated flue gas (15% CO2, 5% O2 in N2), the CGDE with 20 wt% [Emim][BF4]/PIM‐1 achieved &gt;70% CO Faradaic efficiency (FE) at 100 mA cm−2, versus ∼20% FE for a pristine GDE. Multiphysics simulations confirmed effective CO2 delivery through the selective layer, with minimal O2 permeation. Cost estimation analysis indicates around 25% reduction in CO's minimum selling price using the integrated design and &gt;50% under ideal performance metrics by eliminating compression/transport. These results demonstrate that advanced electrode design with CO2‐selective interlayer enables direct mixed‐gas ECO2R, establishes key design criteria for selective layers, and significantly improves process economics.

Article Details

Volume / Issue Vol. 64, Issue 40
Published September 26, 2025
ISSN 1433-7851
Publisher Wiley

Journal Info

Angewandte Chemie International Edition

Wiley

ISSN: 1433-7851 Physical Sciences

Authors (8)

H

Hesamoddin Rabiee

Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland

A

Abhijit Dutta

Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland

P

Penghui Yan

School of Chemical Engineering The University of Queensland Brisbane QLD 4072 Australia

L

Lei Ge

F

Fatereh Dorosti

School of Chemical Engineering The University of Queensland Brisbane QLD 4072 Australia

X

Xin Yu

BGI Research, Qingdao, China.

A

Alain Rieder

Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland

P

Peter Broekmann

Department of Chemistry, Biochemistry and Pharmaceutical Science, University of Bern, Freiestrasse 3, 3012 Bern, Switzerland