Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane

The objective of this study was to analyze the catalytic performance of series of cobalt-modified Zeolite-4A supported catalysts for the syngas (CO and H2) production at 800 °C via the partial oxidation of methane (POM). The Co/Zeolite-4A catalyst was synthesized using a two-step hydrothermal method...

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Main Authors: Amer Zaffar, Bilal Alam Khan, Asif Hussain Khoja, Uneeb Masood Khan, Qassam Sarmad, Muhammad Taqi Mehran, Salman Raza Naqvi, Majid Ali
Format: Article
Language:English
Published: Diponegoro University 2021-09-01
Series:Bulletin of Chemical Reaction Engineering & Catalysis
Subjects:
Online Access:https://ejournal2.undip.ac.id/index.php/bcrec/article/view/10614
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spelling doaj-311ab7fcb1d14e059b6ea18c02947f152021-07-23T08:41:12ZengDiponegoro UniversityBulletin of Chemical Reaction Engineering & Catalysis1978-29932021-09-0116350751610.9767/bcrec.16.3.10614.507-5164861Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of MethaneAmer Zaffar0Bilal Alam Khan1Asif Hussain Khoja2https://orcid.org/0000-0002-9006-3456Uneeb Masood Khan3https://orcid.org/0000-0001-6992-6432Qassam Sarmad4Muhammad Taqi Mehran5https://orcid.org/0000-0002-6045-6558Salman Raza Naqvi6https://orcid.org/0000-0003-4035-181XMajid Ali7School of Chemical and Materials Engineering (SCME), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanDepartment of Applied Science and Technology, Politecnico di Torino, Corso Duca degli Abruzzi, 24, 10129 Torino, ItalyU.S.-Pakistan Centre for Advanced Studies in Energy (USPCAS-E), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanU.S.-Pakistan Centre for Advanced Studies in Energy (USPCAS-E), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanU.S.-Pakistan Centre for Advanced Studies in Energy (USPCAS-E), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanSchool of Chemical and Materials Engineering (SCME), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), Pakistan, PakistanSchool of Chemical and Materials Engineering (SCME), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanU.S.-Pakistan Centre for Advanced Studies in Energy (USPCAS-E), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), PakistanThe objective of this study was to analyze the catalytic performance of series of cobalt-modified Zeolite-4A supported catalysts for the syngas (CO and H2) production at 800 °C via the partial oxidation of methane (POM). The Co/Zeolite-4A catalyst was synthesized using a two-step hydrothermal method from coal fly ash. The synthesized catalysts were characterized by X-ray Diffraction (XRD), Scanning Electron Microscope (SEM), Energy Dispersive X-ray (EDX), and Thermogravimetric Analysis (TGA). The catalyst shows a crystalline structure with stability up to 900 °C. The catalytic performance analysis shows the CH4 conversion increases from 29 to 68% for 0 and 10 wt% Co over Zeolite-4A, respectively. The H2 selectivity was improved from 28–56% while CO selectivity increased from 24–52 % making H2/CO ratio > 1. The stability analysis shows the 10% Co/Zeolite-4A withstand for 24 h a time on stream (TOS). Finally, the spent catalyst analysis was carried out to check the carbon formation along with its structural analysis. The minimal carbon formation is analyzed in 24 h TOS for POM reaction. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).https://ejournal2.undip.ac.id/index.php/bcrec/article/view/10614partial oxidation of methane (pom)zeolite-4ahydrogen productionsyngas
collection DOAJ
language English
format Article
sources DOAJ
author Amer Zaffar
Bilal Alam Khan
Asif Hussain Khoja
Uneeb Masood Khan
Qassam Sarmad
Muhammad Taqi Mehran
Salman Raza Naqvi
Majid Ali
spellingShingle Amer Zaffar
Bilal Alam Khan
Asif Hussain Khoja
Uneeb Masood Khan
Qassam Sarmad
Muhammad Taqi Mehran
Salman Raza Naqvi
Majid Ali
Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
Bulletin of Chemical Reaction Engineering & Catalysis
partial oxidation of methane (pom)
zeolite-4a
hydrogen production
syngas
author_facet Amer Zaffar
Bilal Alam Khan
Asif Hussain Khoja
Uneeb Masood Khan
Qassam Sarmad
Muhammad Taqi Mehran
Salman Raza Naqvi
Majid Ali
author_sort Amer Zaffar
title Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
title_short Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
title_full Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
title_fullStr Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
title_full_unstemmed Synthesis of Ash Derived Co/Zeolite Catalyst for Hydrogen Rich Syngas Production via Partial Oxidation of Methane
title_sort synthesis of ash derived co/zeolite catalyst for hydrogen rich syngas production via partial oxidation of methane
publisher Diponegoro University
series Bulletin of Chemical Reaction Engineering & Catalysis
issn 1978-2993
publishDate 2021-09-01
description The objective of this study was to analyze the catalytic performance of series of cobalt-modified Zeolite-4A supported catalysts for the syngas (CO and H2) production at 800 °C via the partial oxidation of methane (POM). The Co/Zeolite-4A catalyst was synthesized using a two-step hydrothermal method from coal fly ash. The synthesized catalysts were characterized by X-ray Diffraction (XRD), Scanning Electron Microscope (SEM), Energy Dispersive X-ray (EDX), and Thermogravimetric Analysis (TGA). The catalyst shows a crystalline structure with stability up to 900 °C. The catalytic performance analysis shows the CH4 conversion increases from 29 to 68% for 0 and 10 wt% Co over Zeolite-4A, respectively. The H2 selectivity was improved from 28–56% while CO selectivity increased from 24–52 % making H2/CO ratio > 1. The stability analysis shows the 10% Co/Zeolite-4A withstand for 24 h a time on stream (TOS). Finally, the spent catalyst analysis was carried out to check the carbon formation along with its structural analysis. The minimal carbon formation is analyzed in 24 h TOS for POM reaction. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0).
topic partial oxidation of methane (pom)
zeolite-4a
hydrogen production
syngas
url https://ejournal2.undip.ac.id/index.php/bcrec/article/view/10614
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