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Article

Combined Magnesia, Ceria and Nickel catalyst supported over γ-Alumina Doped with Titania for Dry Reforming of Methane

by
Ahmed Sadeq Al-Fatesh
1,*,
Samsudeen Olajide Kasim
1,
Ahmed Aidid Ibrahim
1,
Anis Hamza Fakeeha
1,
Ahmed Elhag Abasaeed
1,
Rasheed Alrasheed
2,
Rawan Ashamari
2 and
Abdulaziz Bagabas
2,*
1
Chemical Engineering Department, College of Engineering, King Saud University, P.O. Box 800, Riyadh 11421, Saudi Arabia
2
National Petrochemical Technology Center (NPTC), Materials Science Research Institute (MSRI), King Abdulaziz City for Science and Technology, P.O. Box 6086, Riyadh 11442, Saudi Arabia
*
Authors to whom correspondence should be addressed.
Catalysts 2019, 9(2), 188; https://doi.org/10.3390/catal9020188
Submission received: 21 January 2019 / Revised: 5 February 2019 / Accepted: 13 February 2019 / Published: 18 February 2019
(This article belongs to the Special Issue Catalysts for Syngas Production)

Abstract

This study investigated dry reforming of methane (DRM) over combined catalysts supported on γ-Al2O3 support doped with 3.0 wt. % TiO2. Physicochemical properties of all catalysts were determined by inductively coupled plasma/mass spectrometry (ICP-MS), nitrogen physisorption, X-ray diffraction, temperature programmed reduction/oxidation/desorption/pulse hydrogen chemisorption, thermogravimetric analysis, and scanning electron microscopy. Addition of CeO2 and MgO to Ni strengthened the interaction between the Ni and the support. The catalytic activity results indicate that the addition of CeO2 and MgO to Ni did not reduce carbon deposition, but improved the activity of the catalysts. Temperature programmed oxidation (TPO) revealed the formation of carbon that is mainly amorphous and small amount of graphite. The highest CH4 and CO2 conversion was found for the catalyst composed of 5.0 wt. % NiO-10.0 wt. % CeO2/3.0 wt. %TiO2-γ-Al2O3 (Ti-CAT-II), resulting in H2/CO mole ratio close to unity. The optimum reaction conditions in terms of reactant conversion and H2/CO mole ratio were achieved by varying space velocity and CO2/CH4 mole ratio.
Keywords: CH4; CeO2; dry reforming; MgO; Ni; TiO2 CH4; CeO2; dry reforming; MgO; Ni; TiO2

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MDPI and ACS Style

Sadeq Al-Fatesh, A.; Olajide Kasim, S.; Aidid Ibrahim, A.; Hamza Fakeeha, A.; Elhag Abasaeed, A.; Alrasheed, R.; Ashamari, R.; Bagabas, A. Combined Magnesia, Ceria and Nickel catalyst supported over γ-Alumina Doped with Titania for Dry Reforming of Methane. Catalysts 2019, 9, 188. https://doi.org/10.3390/catal9020188

AMA Style

Sadeq Al-Fatesh A, Olajide Kasim S, Aidid Ibrahim A, Hamza Fakeeha A, Elhag Abasaeed A, Alrasheed R, Ashamari R, Bagabas A. Combined Magnesia, Ceria and Nickel catalyst supported over γ-Alumina Doped with Titania for Dry Reforming of Methane. Catalysts. 2019; 9(2):188. https://doi.org/10.3390/catal9020188

Chicago/Turabian Style

Sadeq Al-Fatesh, Ahmed, Samsudeen Olajide Kasim, Ahmed Aidid Ibrahim, Anis Hamza Fakeeha, Ahmed Elhag Abasaeed, Rasheed Alrasheed, Rawan Ashamari, and Abdulaziz Bagabas. 2019. "Combined Magnesia, Ceria and Nickel catalyst supported over γ-Alumina Doped with Titania for Dry Reforming of Methane" Catalysts 9, no. 2: 188. https://doi.org/10.3390/catal9020188

APA Style

Sadeq Al-Fatesh, A., Olajide Kasim, S., Aidid Ibrahim, A., Hamza Fakeeha, A., Elhag Abasaeed, A., Alrasheed, R., Ashamari, R., & Bagabas, A. (2019). Combined Magnesia, Ceria and Nickel catalyst supported over γ-Alumina Doped with Titania for Dry Reforming of Methane. Catalysts, 9(2), 188. https://doi.org/10.3390/catal9020188

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