Identifying and enhancing the spillover of crucial intermediates on the Fischer–Tropsch catalyst: A mechanistic approach

Understanding and enhancing spillover phenomena in Fischer–Tropsch Synthesis (FTS) is critical for optimizing catalyst performance. In this study, we present a comprehensive evaluation of hydrogen, carbon monoxide, and water (θ-H, θ-CO, and θ-H 2 O) spillover mechanisms over a series of engineered multi-shell nanocomposite catalysts: Co@C( Z -d)@SiO 2 @CeO 2 (NC), the etched NC (NCE), and the Ru-doped NCE (RNCE). A suite of advanced characterization techniques, XRD, HR-XPS, FTIR, Raman, UV–Vis DRS, and TPD, along with molecular dynamics (MD) simulations, was employed to elucidate structure–function relationships and quantify the spillover behavior of key FTS intermediates. Our findings reveal that etching the silica layer significantly enhances oxygen vacancy formation and overall spillover activity. Among all catalysts, RNCE exhibits the highest oxygen vacancy concentration, the lowest oxygen vacancy formation energy, and the narrowest band gap, attributes that contribute to its superior spillover capacity. MD simulation results confirm that θ-H 2 O and θ-CO spillovers dominate over hydroxyl and θ-HCO spillovers, with RNCE achieving the highest spillover rates across all intermediate species. Performance tests conducted under varying partial pressures of H 2 , CO, and H 2 O further validate that enhanced spillover correlates directly with increased CO conversion and C 5 + hydrocarbon selectivity. This study not only deciphers the mechanistic role of spillover in FTS but also highlights the synergistic effects of Ru promotion, silica etching, and oxygen vacancy engineering in advancing the design of high-performance FTS catalysts for efficient hydrocarbon production. • Spillover of H, CO, and H 2 O intermediates in FTS was mechanistically evaluated. • Etched silica and Ru doping enhanced spillover via increased Co dispersion and oxygen vacancies. • MD simulations confirmed θ-H 2 O and θ-CO as dominant spillover species. • RNCE catalyst showed superior spillover, CO conversion, and C 5 + selectivity. • Provides a design strategy for high-efficiency FTS catalysts via spillover control.

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Publication Details

Journal
Fuel Processing Technology
Published
2025-05-01
DOI
https://doi.org/10.1016/j.fuproc.2025.108225
Citations
16
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
6.22

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article

Identifying and enhancing the spillover of crucial intermediates on the Fischer–Tropsch catalyst: A mechanistic approach

Jafar Towfighi, Masoud Safari Yazd, Mohammad Reza Pourmand, Farshid Sobhani Bazghaleh et al.
16 citations
Fuel Processing Technology
Catalysts for Methane Reforming
6.22
article

Identifying and enhancing the spillover of crucial intermediates on the Fischer–Tropsch catalyst: A mechanistic approach

Jafar Towfighi, Masoud Safari Yazd, Mohammad Reza Pourmand, Farshid Sobhani Bazghaleh, Farshad Sobhani Bazghaleh
article en
16 citations

Abstract

Understanding and enhancing spillover phenomena in Fischer–Tropsch Synthesis (FTS) is critical for optimizing catalyst performance. In this study, we present a comprehensive evaluation of hydrogen, carbon monoxide, and water (θ-H, θ-CO, and θ-H 2 O) spillover mechanisms over a series of engineered multi-shell nanocomposite catalysts: Co@C( Z -d)@SiO 2 @CeO 2 (NC), the etched NC (NCE), and the Ru-doped NCE (RNCE). A suite of advanced characterization techniques, XRD, HR-XPS, FTIR, Raman, UV–Vis DRS, and TPD, along with molecular dynamics (MD) simulations, was employed to elucidate structure–function relationships and quantify the spillover behavior of key FTS intermediates. Our findings reveal that etching the silica layer significantly enhances oxygen vacancy formation and overall spillover activity. Among all catalysts, RNCE exhibits the highest oxygen vacancy concentration, the lowest oxygen vacancy formation energy, and the narrowest band gap, attributes that contribute to its superior spillover capacity. MD simulation results confirm that θ-H 2 O and θ-CO spillovers dominate over hydroxyl and θ-HCO spillovers, with RNCE achieving the highest spillover rates across all intermediate species. Performance tests conducted under varying partial pressures of H 2 , CO, and H 2 O further validate that enhanced spillover correlates directly with increased CO conversion and C 5 + hydrocarbon selectivity. This study not only deciphers the mechanistic role of spillover in FTS but also highlights the synergistic effects of Ru promotion, silica etching, and oxygen vacancy engineering in advancing the design of high-performance FTS catalysts for efficient hydrocarbon production. • Spillover of H, CO, and H 2 O intermediates in FTS was mechanistically evaluated. • Etched silica and Ru doping enhanced spillover via increased Co dispersion and oxygen vacancies. • MD simulations confirmed θ-H 2 O and θ-CO as dominant spillover species. • RNCE catalyst showed superior spillover, CO conversion, and C 5 + selectivity. • Provides a design strategy for high-efficiency FTS catalysts via spillover control.

Fuel Processing TechnologyVol. 273
Tarbiat Modares University (IR), K. N. Toosi University of Technology (IR)
Iran National Science Foundation
Openalex Percentile: Top 3%
Catalysts for Methane Reforming
6.22
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