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Updated: Sep 19, 2025

Synthesis and Performance Characterizations of Transition Metal Single Atom Catalyst for Electrochemical CO2 Reduction
Published on: April 10, 2018
Harnessing electrochemical CO2 reduction and assisted water electrolysis via constrained thermodynamic modeling
Jinuk Choi1, Hyojung Lim1, Subramani Surendran1
1Hydrogen Energy Technology Laboratory, Korea Institute of Energy Technology (KENTECH), 58330 Naju, Republic of Korea. usim@kentech.ac.kr.
Abstract:
Electrochemical CO2 reduction reaction (CO2RR) 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 CO2 phase transitions (both gaseous and aqueous) and operating conditions, such as temperature and pH. This study systematically examines the thermodynamic behavior of CO2RR and AWE by calculating Gibbs free energy (ΔG), enthalpy (ΔH), and theoretical potentials (ETN and ERE) over a broad temperature range (0-1000 °C) and varying pH conditions. Pourbaix diagrams for key CO2-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 CO2 systems, equilibrium potentials shift due to the effects of CO2 speciation. In alkaline conditions, dissolved CO2 undergoes sequential conversion into HCO3- and CO32-, resulting in increased overpotentials in CO2RR. Conversely, gaseous CO2 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 VTN and VRE 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 CO2 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 CO2 conversion technologies for industrial applications.
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