The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production

The time-on-stream catalytic performance and stability of 8 wt. % Ni catalyst supported on two commercially available catalytic supports, ZrO2 and 15 wt.% WO3-ZrO2, was investigated under the biogas dry reforming reaction for syngas production, at 750°C and a biogas quality equal to CH4/CO2 = 1.5, t...

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Main Authors: Nikolaos D. Charisiou, Georgios Siakavelas, Kyriakos N. Papageridis, Apostolos Baklavaridis, Lazaros Tzounis, Grammatiki Goula, Ioannis V. Yentekakis, Kyriaki Polychronopoulou, Maria A. Goula
Format: Article
Language:English
Published: Frontiers Media S.A. 2017-10-01
Series:Frontiers in Environmental Science
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Online Access:http://journal.frontiersin.org/article/10.3389/fenvs.2017.00066/full
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spelling doaj-0f0a03052f1d4e97919a3250f4771baa2020-11-24T23:14:12ZengFrontiers Media S.A.Frontiers in Environmental Science2296-665X2017-10-01510.3389/fenvs.2017.00066289015The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas ProductionNikolaos D. Charisiou0Georgios Siakavelas1Kyriakos N. Papageridis2Apostolos Baklavaridis3Lazaros Tzounis4Grammatiki Goula5Ioannis V. Yentekakis6Kyriaki Polychronopoulou7Maria A. Goula8Laboratory of Alternative Fuels and Environmental Catalysis, Department of Environmental and Pollution Control Engineering, Western Macedonia University of Applied Sciences, Kozani, GreeceLaboratory of Alternative Fuels and Environmental Catalysis, Department of Environmental and Pollution Control Engineering, Western Macedonia University of Applied Sciences, Kozani, GreeceLaboratory of Alternative Fuels and Environmental Catalysis, Department of Environmental and Pollution Control Engineering, Western Macedonia University of Applied Sciences, Kozani, GreeceLaboratory of Alternative Fuels and Environmental Catalysis, Department of Environmental and Pollution Control Engineering, Western Macedonia University of Applied Sciences, Kozani, GreeceComposite and Smart Materials Laboratory, Department of Materials Science and Engineering, University of Ioannina, Ioannina, GreeceLaboratory of Physical Chemistry and Chemical Processes, School of Environmental Engineering, Technical University of Crete, Crete, GreeceLaboratory of Physical Chemistry and Chemical Processes, School of Environmental Engineering, Technical University of Crete, Crete, GreeceDepartment of Mechanical Engineering, Khalifa University of Science and Technology, Abu Dhabi, United Arab EmiratesLaboratory of Alternative Fuels and Environmental Catalysis, Department of Environmental and Pollution Control Engineering, Western Macedonia University of Applied Sciences, Kozani, GreeceThe time-on-stream catalytic performance and stability of 8 wt. % Ni catalyst supported on two commercially available catalytic supports, ZrO2 and 15 wt.% WO3-ZrO2, was investigated under the biogas dry reforming reaction for syngas production, at 750°C and a biogas quality equal to CH4/CO2 = 1.5, that represents a common concentration of real biogas. A number of analytical techniques such as N2 adsorption/desorption (BET method), XRD, H2-TPR, NH3- and CO2-TPD, SEM, ICP, thermal analysis (TGA/DTG) and Raman spectroscopy were used in order to determine textural, structural and other physicochemical properties of the catalytic materials, and the type of carbon deposited on the catalytic surface of spent samples. These techniques were used in an attempt to understand better the effects of WO3-induced modifications on the catalyst morphology, physicochemical properties and catalytic performance. Although Ni dispersion and reducibility characteristics were found superior on the modified Ni/WZr sample than that on Ni/Zr, its dry reforming of methane (DRM) performance was inferior; a result attributed to the enhanced acidity and complete loss of the basicity recorded on this catalyst, an effect that competes and finally overshadows the benefits of the other superior properties. Raman studies revealed that the degree of graphitization decreases with the insertion of WO3 in the crystalline structure of the ZrO2 support, as the ID/IG peak intensity ratio is 1.03 for the Ni/Zr and 1.29 for the Ni/WZr catalyst.http://journal.frontiersin.org/article/10.3389/fenvs.2017.00066/fullbiogas utilizationsyngas productionzirconiatungstated zirconiadry reforming of methanerenewable carbon sources
collection DOAJ
language English
format Article
sources DOAJ
author Nikolaos D. Charisiou
Georgios Siakavelas
Kyriakos N. Papageridis
Apostolos Baklavaridis
Lazaros Tzounis
Grammatiki Goula
Ioannis V. Yentekakis
Kyriaki Polychronopoulou
Maria A. Goula
spellingShingle Nikolaos D. Charisiou
Georgios Siakavelas
Kyriakos N. Papageridis
Apostolos Baklavaridis
Lazaros Tzounis
Grammatiki Goula
Ioannis V. Yentekakis
Kyriaki Polychronopoulou
Maria A. Goula
The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
Frontiers in Environmental Science
biogas utilization
syngas production
zirconia
tungstated zirconia
dry reforming of methane
renewable carbon sources
author_facet Nikolaos D. Charisiou
Georgios Siakavelas
Kyriakos N. Papageridis
Apostolos Baklavaridis
Lazaros Tzounis
Grammatiki Goula
Ioannis V. Yentekakis
Kyriaki Polychronopoulou
Maria A. Goula
author_sort Nikolaos D. Charisiou
title The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
title_short The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
title_full The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
title_fullStr The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
title_full_unstemmed The Effect of WO3 Modification of ZrO2 Support on the Ni-Catalyzed Dry Reforming of Biogas Reaction for Syngas Production
title_sort effect of wo3 modification of zro2 support on the ni-catalyzed dry reforming of biogas reaction for syngas production
publisher Frontiers Media S.A.
series Frontiers in Environmental Science
issn 2296-665X
publishDate 2017-10-01
description The time-on-stream catalytic performance and stability of 8 wt. % Ni catalyst supported on two commercially available catalytic supports, ZrO2 and 15 wt.% WO3-ZrO2, was investigated under the biogas dry reforming reaction for syngas production, at 750°C and a biogas quality equal to CH4/CO2 = 1.5, that represents a common concentration of real biogas. A number of analytical techniques such as N2 adsorption/desorption (BET method), XRD, H2-TPR, NH3- and CO2-TPD, SEM, ICP, thermal analysis (TGA/DTG) and Raman spectroscopy were used in order to determine textural, structural and other physicochemical properties of the catalytic materials, and the type of carbon deposited on the catalytic surface of spent samples. These techniques were used in an attempt to understand better the effects of WO3-induced modifications on the catalyst morphology, physicochemical properties and catalytic performance. Although Ni dispersion and reducibility characteristics were found superior on the modified Ni/WZr sample than that on Ni/Zr, its dry reforming of methane (DRM) performance was inferior; a result attributed to the enhanced acidity and complete loss of the basicity recorded on this catalyst, an effect that competes and finally overshadows the benefits of the other superior properties. Raman studies revealed that the degree of graphitization decreases with the insertion of WO3 in the crystalline structure of the ZrO2 support, as the ID/IG peak intensity ratio is 1.03 for the Ni/Zr and 1.29 for the Ni/WZr catalyst.
topic biogas utilization
syngas production
zirconia
tungstated zirconia
dry reforming of methane
renewable carbon sources
url http://journal.frontiersin.org/article/10.3389/fenvs.2017.00066/full
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