Characterization of Ag-promoted Ni/SiO2 Catalysts for Syngas Production via Carbon Dioxide (CO2) Dry Reforming of Glycerol

Norazimah Harun  -  Faculty of Chemical Engineering & Natural Resources, Universiti Malaysia Pahang, 26300 Gambang, Pahang,, Malaysia
Jolius Gimbun  -  Faculty of Chemical Engineering & Natural Resources, Universiti Malaysia Pahang, 26300 Gambang, Pah, Malaysia
Mohammad Tazli Azizan  -  Department of Chemical Engineering, Faculty of Engineering, Universiti Teknologi PETRONAS, 32610 Bandar Seri Iskandar, Perak Darul Ridzuan,, Malaysia
*Sumaiya Zainal Abidin  -  Faculty of Chemical Engineering & Natural Resources, Universiti Malaysia Pahang, 26300 Gambang, Pah, Malaysia
Received: 20 Jun 2016; Published: 20 Aug 2016.
Open Access Copyright (c) 2016 Bulletin of Chemical Reaction Engineering & Catalysis
License URL: http://creativecommons.org/licenses/by-sa/4.0

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Article Info
Section: The International Conference on Fluids and Chemical Engineering (FluidsChE 2015)
Language: EN
In 2016: BCREC Volume 11 Issue 2 Year 2016 (SCOPUS and Web of Science Indexed, August 2016)
Statistics: 939 370
Abstract

The carbon dioxide (CO2) dry reforming of glycerol for syngas production is one of the promising ways to benefit the oversupply crisis of glycerol worldwide. It is an attractive process as it converts carbon dioxide, a greenhouse gas into a synthesis gas and simultaneously removed from the carbon biosphere cycle. In this study, the glycerol dry reforming was carried out using Silver (Ag) promoted Nickel (Ni) based catalysts supported on silicon oxide (SiO2) i.e. Ag-Ni/SiO2. The catalysts were prepared through wet impregnation method and characterized by using Brunauer-Emmett-Teller (BET) surface area, Scanning Electron Microscopy (SEM), X-ray Diffraction (XRD), and Thermo Gravimetric (TGA) analysis. The experiment was conducted in a tubular reactor which condition fixed at 973 K and CO2:glycerol molar ratio of 1, under atmospheric pressure. It was found that the main gaseous products are H₂, CO and CH4 with H₂:CO molar ratio < 1.0. From the reaction study, Ag(5)-Ni/SiO2 results in highest glycerol conversion and hydrogen yield, accounted for 32.6% and 27.4%, respectively. Copyright © 2016 BCREC GROUP. All rights reserved

Received: 22nd January 2016; Revised: 22nd February 2016; Accepted: 23rd February 2016

How to Cite: Harun, N., Gimbun, J., Azizan, M.T., Abidin S.Z. (2016). Characterization of Ag-promoted Ni/SiO2 Catalysts for Syngas Production via Carbon Dioxide (CO2) Dry Reforming of Glycerol. Bulletin of Chemical Reaction Engineering & Catalysis, 11 (2): 220-229 (doi:10.9767/bcrec.11.2.553.220-229)

Permalink/DOI: http://dx.doi.org/10.9767/bcrec.11.2.553.220-229

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Keywords: Glycerol; Dry reforming; Syngas; Nickel-based catalysts; Silicon Oxide

Article Metrics:

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  1. A review on glycerol reforming processes over Ni-based catalyst for hydrogen and syngas productions
    Nurul Asmawati Roslan, Sumaiya Zainal Abidin, Asmida Ideris, Dai-Viet N. Vo, International Journal of Hydrogen Energy, 2019. doi: 10.1016/j.ijhydene.2019.08.211
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