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Article

Comparative Study on Ni/MgO-Al2O3 Catalysts for Dry and Combined Steam–CO2 Reforming of Methane

by
Tingting Zheng
1,
Yuqi Zhou
1,
Hongjie Cui
2 and
Zhiming Zhou
1,*
1
State Key Laboratory of Green Chemical Engineering and Industrial Catalysis, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China
2
Industrial Catalysis Center, Department of Chemical Engineering, Tsinghua University, Beijing 100084, China
*
Author to whom correspondence should be addressed.
Catalysts 2025, 15(7), 659; https://doi.org/10.3390/catal15070659
Submission received: 9 June 2025 / Revised: 30 June 2025 / Accepted: 3 July 2025 / Published: 6 July 2025
(This article belongs to the Section Catalytic Reaction Engineering)

Abstract

The dry reforming of methane (DRM) and the combined steam–CO2 reforming of methane (CSCRM) are promising routes for syngas production while simultaneously utilizing two major greenhouse gases—CO2 and CH4. In this study, a series of Ni/MgO-Al2O3 catalysts with varying Mg/Al molar ratios (Ni/MgAl(x), x = 0.5–0.9), along with Ni/MgO and Ni/Al2O3, were synthesized, characterized, and evaluated in both the DRM and CSCRM. Ni/MgO and Ni/Al2O3 exhibited a lower activity due to fewer active sites and a poor CH4/CO2 activation balance. In contrast, Ni/MgAl(0.6), Ni/MgAl(0.7), and Ni/MgAl(0.8) showed an enhanced activity, attributed to more abundant active sites and a more balanced activation of CH4 and CO2. Ni/MgAl(0.7) delivered the best DRM performance, whereas Ni/MgAl(0.8) was optimal for the CSCRM, likely due to its greater number of strong basic sites promoting CO2 and H2O adsorption. At 750 °C and 0.1 MPa over 100 h, Ni/MgAl(0.7) maintained a stable DRM performance (77% CH4 and 86% CO2 conversion; H2/CO = 0.9) at 120 L/(gcat·h), while Ni/MgAl(0.8) achieved a stable CSCRM performance (80% CH4 and 62% CO2 conversion; H2/CO = 2.1) at 132 L/(gcat·h). This study provides valuable insights into designing efficient Ni/MgO-Al2O3 catalysts for targeted syngas production.
Keywords: dry reforming of methane; combined steam–CO2 reforming of methane; syngas; Ni/MgO-Al2O3; structure–performance relationship dry reforming of methane; combined steam–CO2 reforming of methane; syngas; Ni/MgO-Al2O3; structure–performance relationship

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MDPI and ACS Style

Zheng, T.; Zhou, Y.; Cui, H.; Zhou, Z. Comparative Study on Ni/MgO-Al2O3 Catalysts for Dry and Combined Steam–CO2 Reforming of Methane. Catalysts 2025, 15, 659. https://doi.org/10.3390/catal15070659

AMA Style

Zheng T, Zhou Y, Cui H, Zhou Z. Comparative Study on Ni/MgO-Al2O3 Catalysts for Dry and Combined Steam–CO2 Reforming of Methane. Catalysts. 2025; 15(7):659. https://doi.org/10.3390/catal15070659

Chicago/Turabian Style

Zheng, Tingting, Yuqi Zhou, Hongjie Cui, and Zhiming Zhou. 2025. "Comparative Study on Ni/MgO-Al2O3 Catalysts for Dry and Combined Steam–CO2 Reforming of Methane" Catalysts 15, no. 7: 659. https://doi.org/10.3390/catal15070659

APA Style

Zheng, T., Zhou, Y., Cui, H., & Zhou, Z. (2025). Comparative Study on Ni/MgO-Al2O3 Catalysts for Dry and Combined Steam–CO2 Reforming of Methane. Catalysts, 15(7), 659. https://doi.org/10.3390/catal15070659

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