Your new experience awaits. Try the new design now and help us make it even better

ORIGINAL RESEARCH article

Front. Energy Res.

Sec. Solar Energy

This article is part of the Research TopicSolar Thermochemistry for Chemical ConversionsView all articles

A Fixed-Bed Reactor for Methane Dry Reforming via a Ceria-based Redox Cycle – Modeling and Experimental Validation

Provisionally accepted
  • 1ETH Zürich, Zurich, Switzerland
  • 2Synhelion SA, Lugano, Switzerland

The final, formatted version of the article will be published soon.

This study explores the production of sustainable aviation fuels through the sun-to-liquid pathway, focusing on the thermochemical production of syngas – a mixture of H2 and CO – using concentrated solar energy. One promising route, termed dry redox reforming, involves the dry reforming of CH4 via 20 a 2-step redox cyclic process using non-stoichiometric ceria (CeO2). This process consists of: (1) the methanothermal reduction of ceria to form syngas; and (2) the oxidation of reduced ceria with CO2 to form CO. Thermodynamic modeling and fixed-bed tubular reactor simulations of dry redox reforming are presented. Ellingham diagrams and species-temperature diagrams illustrate reaction favourability 25 and equilibrium compositions, detailing how elevated non-stoichiometries improve syngas selectivity. The thermodynamic relations are incorporated into a computational fluid dynamic solver developed within OpenFOAM. The transient solver models a system of reversible heterogeneous reactions and fluid flow over a non-stoichiometric solid oxide as a fixed-bed, accounting for the governing conservation equations in both fluid and solid phases. The model is validated with experiments 30 conducted in a lab-scale tubular reactor (𝐷fxb = 19 mm, 𝑙fxb = 30 cm, 5% educts, 𝑉̇in = 1 Ln·min-1, 𝑇sp = 936–1016 °C, ambient pressure, ceria pellet morphology), showing relative errors within 7% for key metrics such as cumulative and instantaneous conversion and selectivity. The validated model is applied as a design tool. A geometric case study considering 100% CH4 educt, ambient pressure, 𝑙fxb = 2 m, and temperatures at around 990 °C, suggests optimal operation of a reactor tube at 𝑉̇in = 10 35 Ln·min-1, with tube diameters of 7–10 cm. A novel operating strategy is introduced, priming and cycling, that leverages the 𝛿-gradient in the fixed-bed to enhance syngas selectivity and conversion, indicating the potential production of a high-purity syngas stream.

Keywords: Solar thermochemistry, Redox cycles, Cerium oxide, Methane, Thermodynamics, Tubular reactor, experimental, computational

Received: 09 Apr 2025; Accepted: 03 Nov 2025.

Copyright: © 2025 Zuber, Steinfeld and Ackermann. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) or licensor are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.

* Correspondence: Aldo Steinfeld, aldo.steinfeld@ethz.ch

Disclaimer: All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article or claim that may be made by its manufacturer is not guaranteed or endorsed by the publisher.