(391a) Modeling the Reactions and Transport in Gas Diffusion Electrode (GDE) for the Electrochemical Reduction of Nitrogen to Ammonia
AIChE Annual Meeting
2020
2020 Virtual AIChE Annual Meeting
Transport and Energy Processes
Transport Processes in Flow Reactors
Tuesday, November 17, 2020 - 8:00am to 8:15am
The improvement in current density is due to the higher surface area, the suppression of mass transfer limitation of N2 to reach the catalyst surface, and minimum concentration polarization near the cathode surface. In this work we developed a multi-physics continuum model for the entire reactor system, that solves the transport of N2 and water across the GDE, transport of N2 in the electrolyte, charge transport and the kinetics of the Nitrogen Reduction Reaction (NRR) and the competing HER (Hydrogen Evolution Reaction). The model has been compared with the experimental results. The effect of various operating conditions such as pH, flow rates of N2 and electrolytes has been studied. The effect of GDE parameters such as porosity, thickness of the catalyst and permeability has been investigated. Different reactor configurations have been simulated at various operating conditions to improve the existing performance of the catalyst.
References
- Weng, L.C., A.T. Bell, and A.Z. Weber, Modeling gas-diffusion electrodes for CO2 reduction. Phys Chem Chem Phys, 2018. 20(25): p. 16973-16984.
- Higgins, D., et al., Gas-Diffusion Electrodes for Carbon Dioxide Reduction: A New Paradigm. ACS Energy Letters, 2018. 4(1): p. 317-324.