77th Annual Gaseous Electronics Conference
Monday–Friday, September 30–October 4 2024;
San Diego, California
Session EF2: Plasma Catalysis
10:00 AM–12:00 PM,
Friday, October 4, 2024
Room: Shutters West I and II
Chair: Hongtao Zhong, Stanford University
Abstract: EF2.00002 : Modeling of plasma assisted CO2 hydrogenation over a Co/Al2O3 catalyst with argon dilution
10:15 AM–10:30 AM
Abstract
Presenter:
Nicholas Deak
(National Renewable Energy Laboratory (NREL))
Authors:
Nicholas Deak
(National Renewable Energy Laboratory (NREL))
Ross Larsen
(National Renewable Energy Laboratory)
Hariswaran Sitaraman
(National Renewable Energy Laboratory)
The use of non-thermal plasma-mediated catalysis has emerged as a viable strategy in recent years for enhancing the reactivity of CO2 hydrogenation to C1 intermediates (e.g. CO, methanol, methane), which form the building blocks for clean fuels and chemical synthesis using renewable hydrogen and electricity. However, considerable uncertainty remains pertaining to the coupling and synergistic effects of plasma catalysis. In this work, numerical modeling of CO2 hydrogenation over a Co/Al2O3 catalyst at atmospheric pressure under varying temperatures and gas compositions (including argon as a carrier gas) is performed. This work will specifically address the research question on the optimal argon fraction that favors both optimal plasma power coupling and CO2/H2 reactivity. First, a reduced microkinetic mechanism is presented that describes a wide array of gas-phase plasma processes including the excitation, dissociation, and ionization of CO2, H2, and argon species, excited species quenching, charge transfer reactions, charged species recombination, and electron attachment and detachment. The gas-phase kinetics mechanism is coupled with a surface kinetics mechanism that describes various pathways by which CO2 conversion and hydrocarbon (HC) formation occur over a Co/Al2O3 catalyst with and without the presence of non-thermal plasma. Molecular scale simulations are performed to calculate sticking probabilities of the dominant gas-phase species, which are used to evaluate the surface reaction rate coefficients in the microkinetics model. These mechanisms are then incorporated into a massively-parallel open-source plasma fluid solver, and multidimensional simulations of a propagating streamer interacting with a catalytic surface are performed. The temperature of the gas and the argon dilution are varied from 300-500 K and 0-90%, respectively, to explore how these parameters impact CO2 conversion and HC formation. It is found that elevated temperatures and increased argon dilution enhance catalyst reactivity up to a point, indicating the existence of an optimal set of parameters for catalytic activity. Lastly, detailed insight is given into which surface reaction pathways play a dominant role in HC formation over the Co/Al2O3 catalyst.