Effects of support on Ni-based catalysts for dry reforming of methane

• Synthesis of Ni-based catalysts supported on La 2 O 3 , ZrO 2 , and Al 2 O 3 by solution combustion synthesis method. • Testing of for dry reformation of methane. • Excellent performance and stability of the Ni/Al 2 O 3 catalysts during DRM reaction. We report the development and evaluation of Ni-based catalysts supported on La 2 O 3 , ZrO 2 , and Al 2 O 3 for dry methane reformation. The catalysts were synthesized using the solution combustion synthesis (SCS) method, characterized using several cutting-edge analytical tools, and tested for CO 2 reformation of methane in a fixed bed plug-flow reactor. Catalytic activity and physicochemical properties of the studied catalysts varied considerably, indicating that the nature of support had a considerable impact. The Ni/Al 2 O 3 nanocatalyst outperformed the Ni/La 2 O 3 and Ni/ZrO 2 catalysts in terms of catalytic activity and stability during the DRM process. During T.O.S. stability tests, the Ni/La 2 O 3 catalyst demonstrated higher initial CH 4 conversion (∼95.3%) than the Ni/Al 2 O 3 catalyst (∼88.7%). However, after 50 hours on stream, the Ni/La 2 O 3 catalyst deactivated significantly, but the Ni/Al 2 O 3 catalyst remained active. Amongst the catalysts tested, the zirconia-supported Ni catalyst had the least activity and demonstrated no activity at temperatures below 800°C. The analysis of the TPR profile of the Ni/ZrO 2 catalyst demonstrated the presence of α-NiO species, indicating a weak metal to support contact, resulting in deactivation due to carbon deposition and aggregation of active sites. The thermogram of the Ni/La 2 O 3 catalyst indicated a combination of two Ni species. The first reduction peak at 342.2°C occurred by the reduction of α-NiO species. The second reduction peak at 695°C was caused by the reduction of surface β-NiO species. The absence of δ-NiO species in the La 2 O 3 crystals suggests that Ni 2+ did not induce inside the lattice. In contrast, Ni/Al 2 O 3 showed the presence of NiAl 2 O 4 nanocrystallite (δ-NiO) spinel and NiO-Al 2 O 3 solid solution, responsible for high activity and stability. Effects of Ni loading on activity and stability during DRM reaction.

Authors

Institutions

Publication Details

Journal
Cleaner Chemical Engineering
Published
2025-08-18
DOI
https://doi.org/10.1016/j.clce.2025.100201
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.00

Funders

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

Effects of support on Ni-based catalysts for dry reforming of methane

Sardar Ali, Mahmoud M. Khader
Cleaner Chemical Engineering
Catalysts for Methane Reforming
article

Effects of support on Ni-based catalysts for dry reforming of methane

Sardar Ali, Mahmoud M. Khader
article en

Abstract

• Synthesis of Ni-based catalysts supported on La 2 O 3 , ZrO 2 , and Al 2 O 3 by solution combustion synthesis method. • Testing of for dry reformation of methane. • Excellent performance and stability of the Ni/Al 2 O 3 catalysts during DRM reaction. We report the development and evaluation of Ni-based catalysts supported on La 2 O 3 , ZrO 2 , and Al 2 O 3 for dry methane reformation. The catalysts were synthesized using the solution combustion synthesis (SCS) method, characterized using several cutting-edge analytical tools, and tested for CO 2 reformation of methane in a fixed bed plug-flow reactor. Catalytic activity and physicochemical properties of the studied catalysts varied considerably, indicating that the nature of support had a considerable impact. The Ni/Al 2 O 3 nanocatalyst outperformed the Ni/La 2 O 3 and Ni/ZrO 2 catalysts in terms of catalytic activity and stability during the DRM process. During T.O.S. stability tests, the Ni/La 2 O 3 catalyst demonstrated higher initial CH 4 conversion (∼95.3%) than the Ni/Al 2 O 3 catalyst (∼88.7%). However, after 50 hours on stream, the Ni/La 2 O 3 catalyst deactivated significantly, but the Ni/Al 2 O 3 catalyst remained active. Amongst the catalysts tested, the zirconia-supported Ni catalyst had the least activity and demonstrated no activity at temperatures below 800°C. The analysis of the TPR profile of the Ni/ZrO 2 catalyst demonstrated the presence of α-NiO species, indicating a weak metal to support contact, resulting in deactivation due to carbon deposition and aggregation of active sites. The thermogram of the Ni/La 2 O 3 catalyst indicated a combination of two Ni species. The first reduction peak at 342.2°C occurred by the reduction of α-NiO species. The second reduction peak at 695°C was caused by the reduction of surface β-NiO species. The absence of δ-NiO species in the La 2 O 3 crystals suggests that Ni 2+ did not induce inside the lattice. In contrast, Ni/Al 2 O 3 showed the presence of NiAl 2 O 4 nanocrystallite (δ-NiO) spinel and NiO-Al 2 O 3 solid solution, responsible for high activity and stability. Effects of Ni loading on activity and stability during DRM reaction.

Cleaner Chemical EngineeringVol. 11
Qatar Science and Technology Park (QA), Qatar University (QA)
Qatar Foundation, Qatar National Research Fund
Openalex Percentile: Top 88%
Catalysts for Methane Reforming
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.