Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas

Carbon dioxide and/or dry methane reforming serves as an effective pathway to mitigate these greenhouse gases. This work evaluates different oxide supports including alumina, Y-zeolite and H-ZSM-5 zeolite for the catalysis of dry reforming methane with Nickel (Ni). The composite catalysts were prepa...

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Main Authors: Wasim Ullah Khan, Mohammad Rizwan Khan, Rosa Busquets, Naushad Ahmad
Format: Article
Language:English
Published: MDPI AG 2021-11-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/14/21/7324
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author Wasim Ullah Khan
Mohammad Rizwan Khan
Rosa Busquets
Naushad Ahmad
author_facet Wasim Ullah Khan
Mohammad Rizwan Khan
Rosa Busquets
Naushad Ahmad
author_sort Wasim Ullah Khan
collection DOAJ
description Carbon dioxide and/or dry methane reforming serves as an effective pathway to mitigate these greenhouse gases. This work evaluates different oxide supports including alumina, Y-zeolite and H-ZSM-5 zeolite for the catalysis of dry reforming methane with Nickel (Ni). The composite catalysts were prepared by impregnating the supports with Ni (5%) and followed by calcination. The zeolite supported catalysts exhibited more reducibility and basicity compared to the alumina supported catalysts, this was assessed with temperature programmed reduction using hydrogen and desorption using carbon dioxide. The catalytic activity, in terms of CH<sub>4</sub> conversion, indicated that 5 wt% Ni supported on alumina exhibited higher CH<sub>4</sub> conversion (80.5%) than when supported on Y-zeolite (71.8%) or H-ZSM-5 (78.5%). In contrast, the H-ZSM-5 catalyst led to higher CO<sub>2</sub> conversion (87.3%) than Y-zeolite (68.4%) and alumina (83.9%) supported catalysts. The stability tests for 9 h time-on-stream showed that Ni supported with H-ZSM-5 had less deactivation (just 2%) due to carbon deposition. The characterization of spent catalysts using temperature programmed oxidation (O<sub>2</sub>-TPO), X-ray diffraction (XRD) and thermo-gravimetric analysis (TGA) revealed that carbon deposition was a main cause of deactivation and that it occurred in the lowest degree on the Ni H-ZSM-5 catalyst.
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spelling doaj.art-4e1888effaa146db8f9805557226657f2023-12-03T13:26:22ZengMDPI AGEnergies1996-10732021-11-011421732410.3390/en14217324Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of SyngasWasim Ullah Khan0Mohammad Rizwan Khan1Rosa Busquets2Naushad Ahmad3Chemical and Process Engineering, College of Engineering, University of Canterbury, Christchurch 8041, New ZealandDepartment of Chemistry, College of Science, King Saud University, P.O. Box. 2454, Riyadh 11451, Saudi ArabiaSchool of Life Sciences, Pharmacy and Chemistry, Kingston University London, Penrhyn Road, Kingston Upon Thames KTI 2EE, UKDepartment of Chemistry, College of Science, King Saud University, P.O. Box. 2454, Riyadh 11451, Saudi ArabiaCarbon dioxide and/or dry methane reforming serves as an effective pathway to mitigate these greenhouse gases. This work evaluates different oxide supports including alumina, Y-zeolite and H-ZSM-5 zeolite for the catalysis of dry reforming methane with Nickel (Ni). The composite catalysts were prepared by impregnating the supports with Ni (5%) and followed by calcination. The zeolite supported catalysts exhibited more reducibility and basicity compared to the alumina supported catalysts, this was assessed with temperature programmed reduction using hydrogen and desorption using carbon dioxide. The catalytic activity, in terms of CH<sub>4</sub> conversion, indicated that 5 wt% Ni supported on alumina exhibited higher CH<sub>4</sub> conversion (80.5%) than when supported on Y-zeolite (71.8%) or H-ZSM-5 (78.5%). In contrast, the H-ZSM-5 catalyst led to higher CO<sub>2</sub> conversion (87.3%) than Y-zeolite (68.4%) and alumina (83.9%) supported catalysts. The stability tests for 9 h time-on-stream showed that Ni supported with H-ZSM-5 had less deactivation (just 2%) due to carbon deposition. The characterization of spent catalysts using temperature programmed oxidation (O<sub>2</sub>-TPO), X-ray diffraction (XRD) and thermo-gravimetric analysis (TGA) revealed that carbon deposition was a main cause of deactivation and that it occurred in the lowest degree on the Ni H-ZSM-5 catalyst.https://www.mdpi.com/1996-1073/14/21/7324CO<sub>2</sub>CH<sub>4</sub>stabilityH-ZSM-5carbon depositiongreenhouse gas reduction
spellingShingle Wasim Ullah Khan
Mohammad Rizwan Khan
Rosa Busquets
Naushad Ahmad
Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
Energies
CO<sub>2</sub>
CH<sub>4</sub>
stability
H-ZSM-5
carbon deposition
greenhouse gas reduction
title Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
title_full Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
title_fullStr Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
title_full_unstemmed Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
title_short Contribution of Oxide Supports in Nickel-Based Catalytic Elimination of Greenhouse Gases and Generation of Syngas
title_sort contribution of oxide supports in nickel based catalytic elimination of greenhouse gases and generation of syngas
topic CO<sub>2</sub>
CH<sub>4</sub>
stability
H-ZSM-5
carbon deposition
greenhouse gas reduction
url https://www.mdpi.com/1996-1073/14/21/7324
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