Current advances in the development of cathodes for continuous scale-up electrochemical CO2 reduction toward formate
Guillermo Díaz-Sainz a, Mario Coz-Cruz a, Kevin Fernández-Caso a, José Antonio Abarca a, Manuel Alvarez-Guerra a, Angel Irabien a
a University of Cantabria, Avenida de los Castros, Santander, Spain
Materials for Sustainable Development Conference (MATSUS)
Proceedings of MATSUS Fall 2024 Conference (MATSUSFall24)
#PECCO2 - Advances in (Photo)Electrochemical CO2 Conversion to Chemicals and Fuels
Lausanne, Switzerland, 2024 November 12th - 15th
Organizers: Deepak PANT, Adriano Sacco and juqin zeng
Invited Speaker, Guillermo Díaz-Sainz, presentation 004
DOI: https://doi.org/10.29363/nanoge.matsusfall.2024.004
Publication date: 28th August 2024

Carbon capture, utilization, and storage (CCUS) strategies are gaining attention as effective methods to achieve carbon dioxide neutrality while creating value-added products through CO2 conversion. Among these strategies, electrochemical CO2 reduction stands out due to its low temperature and pressure requirements and its ability to store energy from renewable sources like solar and wind in the form of valuable chemicals such as formic acid or formate [1].

The “Development of Chemical Processes and Pollution Control” (DePRO) research group at the University of Cantabria, Spain, has been actively working on the continuous electrochemical reduction of CO2 to formate. Various electrocatalysts for both the cathode and anode, along with different electrode configurations, have been investigated. This communication focuses on the recent advancements and challenges in the lab’s research on continuous CO2 electrocatalytic reduction to formate. The experiments were conducted using a consistent setup and operating conditions, with variations in cathodic electrocatalysts, including Pb-, Sn-, and Bi-based materials, and different cathode configurations like plate electrodes, particulate electrodes (PE), Gas Diffusion Electrodes (GDE), Catalyst Coated Membrane Electrodes (CCME), and Membrane Electrode Assembly (MEA). We have also explored various anodes, such as DSA/O2 and Ni-based electrodes, and different ion exchange membranes, including Nafion cationic exchange membranes (CEM) and Sustainion anionic exchange membranes (AEM), while performing the Oxygen Evolution Reaction in the anodic compartment [2].

Notable achievements were made using a Bi MEA configuration with a CO2-humidified input stream [3]. These results include formate concentrations of up to 337 g·L-1, Faradaic Efficiencies of 89 %, and energy consumption values as low as 180 kWh·kmol-1, representing one of the best trade-offs reported in the literature, marking noteworthy progress in this field.

Further research is essential to scale up this process industrially by developing more stable electrocatalysts for both the cathode and anode. Recent work by the research group has focused on optimizing the manufacturing of GDEs for CO2 electroreduction to formate using the automatic spray pyrolysis technique [4]. This approach has yielded valuable insights into creating more efficient electrodes for CO2 reduction.

Additionally, replacing the Oxygen Evolution Reaction at the anode with more valuable oxidation reactions is crucial. The research group has explored the coupling of the Glycerol Oxidation Reaction with CO2 electroreduction to formate, resulting in valuable products in both compartments of the electrochemical reactor. Recent results include high formate concentrations of up to 359 g·L⁻¹ with Faradaic efficiencies up to 95% at the cathode, along with dihydroxyacetone production at a rate of 0.434 mmol·m⁻²·s⁻¹ [5]. This represents a significant advancement in the development and application of this technology.

The authors gratefully acknowledge financial support through projects PID2019-108136RB-C31, PID2020-112845RB-I00, TED2021-129810B-C21, PLEC2022-009398 (MCIN/AEI/10.13039/501100011033 and Unión Europea Next GenerationEU/PRTR), PID2022-138491OB-C31 (MICIU/AEI /10.13039/501100011033 and FEDER, UE) and the Complementary Plan in the area of Energy and Renewable Hydrogen” (funded by Autonomous Community of Cantabria, Spain, and the European Union Next GenerationEU/PRTR). The present work is related to CAPTUS Project. This project has received funding from the European Union’s Horizon Europe research and innovation programme under grant agreement No 101118265​. Jose Antonio Abarca gratefully acknowledges the predoctoral research grant (FPI) PRE2021-097200.

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