Design of Ni-promoted Ca2Fe2O5/modified ceria as oxygen carrier for fast and carbon-resistant chemical-looping steam methane reforming

Chemical looping steam methane reforming enables the production of high-purity syngas and hydrogen while eliminating the energy-intensive downstream separation steps typically required by conventional technologies. Ca 2 Fe 2 O 5 is a promising oxygen carrier thanks to its high redox stability and low equilibrium pO 2 . However, its practical application is hindered by sluggish reduction kinetics. Here, we have overcome this limitation by preparing nickel-promoted composite oxygen carriers (OC) through the physical mixing of Ca 2 Fe 2 O 5 and modified CeO 2 . The selective deposition of Ni on the surface of the CeO 2 -based phase significantly increases the OC reduction rate, outperforming samples in which Ni is in close contact with Ca 2 Fe 2 O 5 (either on the surface or within the lattice). SiO 2 modified ceria was found to be more effective than CeO 2 -Al 2 O 3 and Ce 0.8 Zr 0.2 O 2 in promoting the microstructural stability of CeO 2 within the composite, ensuring consistent performance over multiple redox cycles. The co-presence of Ca 2 Fe 2 O 5 and the catalyst in the same reactive bed effectively limits carbon formation at a low OC conversion degree. In situ synchrotron X-ray diffraction and isothermal packed-bed tests revealed a gas-mediated synergistic mechanism whereby carbon deposition was inhibited by H 2 O and CO 2 generated locally from the reduction of Ca 2 Fe 2 O 5 . This led to fast oxygen exchange and stable syngas production. After 50 reaction cycles, the composite OC produced 13.0 mmol/g of syngas in the reduction step with 88% CH 4 conversion, and 6.8 mmol/g of H 2 in the water splitting step with >99% purity, demonstrating the potential of this OC design strategy. (5×13 cm) • The simple mixing of Ca 2 Fe 2 O 5 and Ni/CeO 2 -SiO 2 yields active and stable OCs. • Ni spatially localized on CeO 2 -SiO 2 promotes Ca 2 Fe 2 O 5 reduction. • Gas phase mediated synergism among components is effective for carbon suppression. • Obtained high syngas/H₂ yield, stability over 50 cycles, and >99% H₂ purity.

Authors

Institutions

Publication Details

Journal
Applied Catalysis B: Environmental
Published
2025-10-04
DOI
https://doi.org/10.1016/j.apcatb.2025.126037
Citations
4
Primary Topic
Chemical Looping and Thermochemical Processes
Type
article
Field-Weighted Citation Impact
2.70

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Design of Ni-promoted Ca2Fe2O5/modified ceria as oxygen carrier for fast and carbon-resistant chemical-looping steam methane reforming

Marta Boaro, Juan Basbus, Alessandro Trovarelli, Carla de Leitenburg et al.
4 citations
Applied Catalysis B: Environmental
Chemical Looping and Thermochemical Processes
2.70
article

Design of Ni-promoted Ca2Fe2O5/modified ceria as oxygen carrier for fast and carbon-resistant chemical-looping steam methane reforming

Marta Boaro, Juan Basbus, Alessandro Trovarelli, Carla de Leitenburg, Jordi Llorca, Andrea Strazzolini
article en
4 citations

Abstract

Chemical looping steam methane reforming enables the production of high-purity syngas and hydrogen while eliminating the energy-intensive downstream separation steps typically required by conventional technologies. Ca 2 Fe 2 O 5 is a promising oxygen carrier thanks to its high redox stability and low equilibrium pO 2 . However, its practical application is hindered by sluggish reduction kinetics. Here, we have overcome this limitation by preparing nickel-promoted composite oxygen carriers (OC) through the physical mixing of Ca 2 Fe 2 O 5 and modified CeO 2 . The selective deposition of Ni on the surface of the CeO 2 -based phase significantly increases the OC reduction rate, outperforming samples in which Ni is in close contact with Ca 2 Fe 2 O 5 (either on the surface or within the lattice). SiO 2 modified ceria was found to be more effective than CeO 2 -Al 2 O 3 and Ce 0.8 Zr 0.2 O 2 in promoting the microstructural stability of CeO 2 within the composite, ensuring consistent performance over multiple redox cycles. The co-presence of Ca 2 Fe 2 O 5 and the catalyst in the same reactive bed effectively limits carbon formation at a low OC conversion degree. In situ synchrotron X-ray diffraction and isothermal packed-bed tests revealed a gas-mediated synergistic mechanism whereby carbon deposition was inhibited by H 2 O and CO 2 generated locally from the reduction of Ca 2 Fe 2 O 5 . This led to fast oxygen exchange and stable syngas production. After 50 reaction cycles, the composite OC produced 13.0 mmol/g of syngas in the reduction step with 88% CH 4 conversion, and 6.8 mmol/g of H 2 in the water splitting step with >99% purity, demonstrating the potential of this OC design strategy. (5×13 cm) • The simple mixing of Ca 2 Fe 2 O 5 and Ni/CeO 2 -SiO 2 yields active and stable OCs. • Ni spatially localized on CeO 2 -SiO 2 promotes Ca 2 Fe 2 O 5 reduction. • Gas phase mediated synergism among components is effective for carbon suppression. • Obtained high syngas/H₂ yield, stability over 50 cycles, and >99% H₂ purity.

Applied Catalysis B: EnvironmentalVol. 383
University of Udine (IT), National Interuniversity Consortium of Materials Science and Technology (IT), University of Genoa (IT), Universitat Politècnica de Catalunya (ES)
European Commission, Agencia Estatal de Investigación
Openalex Percentile: Top 9%
Chemical Looping and Thermochemical Processes
2.70
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.