Tandem Rh-based structured reformer and Ni-YSZ SOFC for decentralized gasoline-to-power conversion

• Autothermal reforming of commercial gasoline (RON-92) over Rh/CZ/A-FCA catalyst. • Stable syngas flow of 70 Nl/h with 37 % H 2 maintained for 50 h. • Catalyst characterized by HRTEM, XRD, and XPS for performance understanding. • Syngas compatible with Ni–YSZ SOFC anodes without purification. • Reformer–SOFC tandem concept proposed for ∼ 50 W telecom power supply. This work reports on the performance of a 0.24 wt% Rh/Ce 0.75 Zr 0.25 O 2 –δ–η-Al 2 O 3 /FeCrAl structured catalyst in the autothermal reforming of commercial gasoline with a research octane number of 92. Stable syngas production amounting to 70 Nl·h −1 containing of 33.8 vol% H 2 and 9.8 vol% CO was demonstrated over 50 h of continuous operation. The origin of the high catalytic efficiency was elucidated by physicochemical characterization (XPS, STEM, XRD), which confirmed the role of Rh redox flexibility (Rh 3+ ⇄ Rh⁰) and Ce 4+ ⇄ Ce 3+ cycling in suppressing carbon formation and maintaining active site dispersion. The compatibility of the produced syngas with Ni–YSZ solid oxide fuel cells was assessed, and a reformer–SOFC tandem concept was proposed to supply 50 W to telecommunication equipment, with operational parameters derived from the present reformer performance. Such a system highlights the potential of integrating catalytic reforming with SOFC conversion for decentralized power generation in remote applications where access to centralized infrastructure is limited.

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Publication Details

Journal
Fuel
Published
2026-01-08
DOI
https://doi.org/10.1016/j.fuel.2026.138249
Primary Topic
Catalysts for Methane Reforming
Type
article
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article

Tandem Rh-based structured reformer and Ni-YSZ SOFC for decentralized gasoline-to-power conversion

P.V. Snytnikov, D.I. Potemkin, J.W. Thybaut, N.V. Ruban et al.
Fuel
Catalysts for Methane Reforming
article

Tandem Rh-based structured reformer and Ni-YSZ SOFC for decentralized gasoline-to-power conversion

P.V. Snytnikov, D.I. Potemkin, J.W. Thybaut, N.V. Ruban, D.A. Svintsitskiy, V.N. Rogozhnikov, V.P. Pakharukova
article en

Abstract

• Autothermal reforming of commercial gasoline (RON-92) over Rh/CZ/A-FCA catalyst. • Stable syngas flow of 70 Nl/h with 37 % H 2 maintained for 50 h. • Catalyst characterized by HRTEM, XRD, and XPS for performance understanding. • Syngas compatible with Ni–YSZ SOFC anodes without purification. • Reformer–SOFC tandem concept proposed for ∼ 50 W telecom power supply. This work reports on the performance of a 0.24 wt% Rh/Ce 0.75 Zr 0.25 O 2 –δ–η-Al 2 O 3 /FeCrAl structured catalyst in the autothermal reforming of commercial gasoline with a research octane number of 92. Stable syngas production amounting to 70 Nl·h −1 containing of 33.8 vol% H 2 and 9.8 vol% CO was demonstrated over 50 h of continuous operation. The origin of the high catalytic efficiency was elucidated by physicochemical characterization (XPS, STEM, XRD), which confirmed the role of Rh redox flexibility (Rh 3+ ⇄ Rh⁰) and Ce 4+ ⇄ Ce 3+ cycling in suppressing carbon formation and maintaining active site dispersion. The compatibility of the produced syngas with Ni–YSZ solid oxide fuel cells was assessed, and a reformer–SOFC tandem concept was proposed to supply 50 W to telecommunication equipment, with operational parameters derived from the present reformer performance. Such a system highlights the potential of integrating catalytic reforming with SOFC conversion for decentralized power generation in remote applications where access to centralized infrastructure is limited.

FuelVol. 413
Ghent University (BE), Boreskov Institute of Catalysis (RU)
Industry, innovation and infrastructure
Openalex Percentile: Top 96%
Catalysts for Methane Reforming
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Tandem Rh-based structured reformer and Ni-YSZ SOFC for decentralized gasoline-to-power conversion — P.V. Snytnikov, D.I. Potemkin, et al. · Fuel (2026) | TGRS Research Map | TGRS