Syngas Production via Methane Dry Reforming over Ceria–Magnesia Mixed Oxide-Supported Nickel Catalysts-Reference-Cited by-同舟云学术

Syngas Production via Methane Dry Reforming over Ceria–Magnesia Mixed Oxide-Supported Nickel Catalysts

Published:2018-10-24 Issue:2 Volume:58 Page:539-552
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Al-Swai Basem M.¹^ORCID,Osman Noridah¹,Alnarabiji Mohamad Sahban¹,Adesina Adesoji A.²,Abdullah Bawadi¹³^ORCID

Affiliation:

1. Chemical Engineering Department, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, 32610 Perak, Malaysia

2. ATODATECH LLC, Pasadena, California 91101, United States

3. CO2 Utilization Group, Institute Contaminant Management for Oil and Gas, Universiti Teknologi PETRONAS, Bandar Seri Iskandar, 32610 Perak, Malaysia

Funder

Universiti Teknologi Petronas

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.8b03671

Reference80 articles.

1. U.S. Energy Information Administration. International Energy Outlook 2016; DOE/EIA-0484(2016); U.S. Department of Energy, May 2016.

2. Catalytic conversion of methane to more useful chemicals and fuels: a challenge for the 21st century

3. Highly active and coke resistant Ni/SiO 2 catalysts for oxidative reforming of model biogas: Effect of low ceria loading

4. Ni/CeO 2 based catalysts as oxygen vectors for the chemical looping dry reforming of methane for syngas production

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