Harnessing electrochemical CO<sub>2</sub> reduction and assisted water electrolysis <i>via</i> constrained thermodynamic modeling

Electrochemical CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) and assisted water electrolysis (AWE) using organic compounds offer promising pathways for sustainable energy conversion. However, the thermodynamic feasibility and efficiency of these processes are strongly influenced by CO<sub>2</sub> phase transitions (both gaseous and aqueous) and operating conditions, such as temperature and pH. This study systematically examines the thermodynamic behavior of CO<sub>2</sub>RR and AWE by calculating Gibbs free energy (Δ<i>G</i>), enthalpy (Δ<i>H</i>), and theoretical potentials (<i>E</i><sub>TN</sub> and <i>E</i><sub>RE</sub>) over a broad temperature range (0-1000 °C) and varying pH conditions. Pourbaix diagrams for key CO<sub>2</sub>-derived products, including CO, hydrocarbons, organic acids, and alcohols, are constructed to assess their stability across different electrochemical environments. The analysis reveals that in aqueous-phase CO<sub>2</sub> systems, equilibrium potentials shift due to the effects of CO<sub>2</sub> speciation. In alkaline conditions, dissolved CO<sub>2</sub> undergoes sequential conversion into HCO<sub>3</sub><sup>-</sup> and CO<sub>3</sub><sup>2-</sup>, resulting in increased overpotentials in CO<sub>2</sub>RR. Conversely, gaseous CO<sub>2</sub> maintains a stable equilibrium potential, mitigating pH-induced fluctuations that could hinder reaction selectivity and efficiency. In AWE, the phase transition during reaction conditions lowers oxidation potentials, resulting in enhanced energy efficiency. The calculated <i>V</i><sub>TN</sub> and <i>V</i><sub>RE</sub> values demonstrate that organic oxidation reactions in AWE require substantially lower energy inputs than conventional oxygen evolution reactions, providing a thermodynamic advantage for energy-efficient hydrogen production. This study establishes a comprehensive thermodynamic framework for CO<sub>2</sub> electrochemical conversion, integrating Pourbaix diagrams and temperature-dependent electrochemical modeling to optimize reaction conditions and energy efficiency. These insights contribute to the rational design of electrocatalytic systems and the development of scalable CO<sub>2</sub> conversion technologies for industrial applications.

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Publication Details

Journal
Physical Chemistry Chemical Physics
Published
2025-01-01
DOI
https://doi.org/10.1039/d5cp01408e
Citations
9
Primary Topic
CO2 Reduction Techniques and Catalysts
Type
article
Field-Weighted Citation Impact
3.27

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article

Harnessing electrochemical CO2 reduction and assisted water electrolysis via constrained thermodynamic modeling

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9 citations
Physical Chemistry Chemical Physics
CO2 Reduction Techniques and Catalysts
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article

Harnessing electrochemical CO2 reduction and assisted water electrolysis via constrained thermodynamic modeling

Uk Sim, Subramani Surendran, Hyojung Lim, Joon Bo Shim, Jinuk Choi, Seonghyeon Park, Gyoung Hwa Jeong
article en
9 citations

Abstract

Electrochemical CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) and assisted water electrolysis (AWE) using organic compounds offer promising pathways for sustainable energy conversion. However, the thermodynamic feasibility and efficiency of these processes are strongly influenced by CO<sub>2</sub> phase transitions (both gaseous and aqueous) and operating conditions, such as temperature and pH. This study systematically examines the thermodynamic behavior of CO<sub>2</sub>RR and AWE by calculating Gibbs free energy (Δ<i>G</i>), enthalpy (Δ<i>H</i>), and theoretical potentials (<i>E</i><sub>TN</sub> and <i>E</i><sub>RE</sub>) over a broad temperature range (0-1000 °C) and varying pH conditions. Pourbaix diagrams for key CO<sub>2</sub>-derived products, including CO, hydrocarbons, organic acids, and alcohols, are constructed to assess their stability across different electrochemical environments. The analysis reveals that in aqueous-phase CO<sub>2</sub> systems, equilibrium potentials shift due to the effects of CO<sub>2</sub> speciation. In alkaline conditions, dissolved CO<sub>2</sub> undergoes sequential conversion into HCO<sub>3</sub><sup>-</sup> and CO<sub>3</sub><sup>2-</sup>, resulting in increased overpotentials in CO<sub>2</sub>RR. Conversely, gaseous CO<sub>2</sub> maintains a stable equilibrium potential, mitigating pH-induced fluctuations that could hinder reaction selectivity and efficiency. In AWE, the phase transition during reaction conditions lowers oxidation potentials, resulting in enhanced energy efficiency. The calculated <i>V</i><sub>TN</sub> and <i>V</i><sub>RE</sub> values demonstrate that organic oxidation reactions in AWE require substantially lower energy inputs than conventional oxygen evolution reactions, providing a thermodynamic advantage for energy-efficient hydrogen production. This study establishes a comprehensive thermodynamic framework for CO<sub>2</sub> electrochemical conversion, integrating Pourbaix diagrams and temperature-dependent electrochemical modeling to optimize reaction conditions and energy efficiency. These insights contribute to the rational design of electrocatalytic systems and the development of scalable CO<sub>2</sub> conversion technologies for industrial applications.

Physical Chemistry Chemical PhysicsVol. 27(33)
Luoyang Normal University (CN)
National Research Foundation of Korea, Korea Institute of Energy Technology Evaluation and Planning
Responsible consumption and production
Openalex Percentile: Top 8%
CO2 Reduction Techniques and Catalysts
3.27
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