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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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 |
work_keys_str_mv |
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1721290236034547712 |