Role of Crowded Surfaces in Microkinetic Modeling of CO <sub>2</sub> Methanation on Nickel

First-principles microkinetic models are instrumental to elucidate reaction mechanisms and guide catalyst design, yet they often rely on low-coverage DFT calculations and therefore fail to describe the crowded surfaces present during low-temperature and high-pressure catalytic reactions. By employing realistic surface coverages in DFT calculations for intermediates and transition states, a dual-site microkinetic model for the methanation of CO2 over nickel catalysts was constructed. Several pathways were considered, including H- and OH-assisted COx activation, which are crucial to lowering the activation energies and increasing reaction rates. Simulations for a packed bed reactor show that the reaction occurs via intermediate formation of CO, quickly reaching a pseudo-steady-state CO partial pressure where the net rate of CO formation from CO2 is equal to the rate of CO conversion to CH4. Simulations based on realistic surface coverage show significant quantitative and qualitative improvement over microkinetic models constructed with low-coverage DFT calculations. Turnover frequencies vary around 10–3 s–1, close to experimentally observed values, with high CH4 selectivities at CO2 conversions above 1%. Simulated total coverages are close to the coverages used in the reference DFT calculations, but the ratio between CO* and H* is strongly temperature- and pressure-dependent. In the reaction mechanism, CO2 activation primarily occurs on the terraces and is the main rate-controlling step for CO2 activation, while CO is activated on B5 sites via a COH# intermediate, one of the rate-controlling steps in CH4 formation. Without B5 sites, the CO concentration reaches a reverse water–gas shift equilibrium before slow methane formation starts. The dominant reaction mechanism identified by microkinetic models based on DFT calculations for realistic surface coverages qualitatively differs from the mechanism identified based on low-coverage DFT calculations, illustrating the crucial role of modeling realistic coverages for reactions on crowded surfaces.

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Publication Details

Journal
ACS Catalysis
Published
2026-03-11
DOI
https://doi.org/10.1021/acscatal.5c07963
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
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article

Role of Crowded Surfaces in Microkinetic Modeling of CO 2 Methanation on Nickel

Konstantijn T. Rommens, Thobani G. Gambu, Mark Saeys
ACS Catalysis
Catalysts for Methane Reforming
article

Role of Crowded Surfaces in Microkinetic Modeling of CO 2 Methanation on Nickel

Konstantijn T. Rommens, Thobani G. Gambu, Mark Saeys
article en

Abstract

First-principles microkinetic models are instrumental to elucidate reaction mechanisms and guide catalyst design, yet they often rely on low-coverage DFT calculations and therefore fail to describe the crowded surfaces present during low-temperature and high-pressure catalytic reactions. By employing realistic surface coverages in DFT calculations for intermediates and transition states, a dual-site microkinetic model for the methanation of CO2 over nickel catalysts was constructed. Several pathways were considered, including H- and OH-assisted COx activation, which are crucial to lowering the activation energies and increasing reaction rates. Simulations for a packed bed reactor show that the reaction occurs via intermediate formation of CO, quickly reaching a pseudo-steady-state CO partial pressure where the net rate of CO formation from CO2 is equal to the rate of CO conversion to CH4. Simulations based on realistic surface coverage show significant quantitative and qualitative improvement over microkinetic models constructed with low-coverage DFT calculations. Turnover frequencies vary around 10–3 s–1, close to experimentally observed values, with high CH4 selectivities at CO2 conversions above 1%. Simulated total coverages are close to the coverages used in the reference DFT calculations, but the ratio between CO* and H* is strongly temperature- and pressure-dependent. In the reaction mechanism, CO2 activation primarily occurs on the terraces and is the main rate-controlling step for CO2 activation, while CO is activated on B5 sites via a COH# intermediate, one of the rate-controlling steps in CH4 formation. Without B5 sites, the CO concentration reaches a reverse water–gas shift equilibrium before slow methane formation starts. The dominant reaction mechanism identified by microkinetic models based on DFT calculations for realistic surface coverages qualitatively differs from the mechanism identified based on low-coverage DFT calculations, illustrating the crucial role of modeling realistic coverages for reactions on crowded surfaces.

ACS Catalysis
University of Cape Town (ZA), Ghent University (BE)
Clean water and sanitation
Openalex Percentile: Top 27%
Catalysts for Methane Reforming
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