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

Author:

Zaffar Amer1,Khan Bilal Alam2,Khoja Asif Hussain3ORCID,Khan Uneeb Masood3ORCID,Sarmad Qassam3,Mehran Muhammad Taqi4ORCID,Naqvi Salman Raza1ORCID,Ali Majid3

Affiliation:

1. School of Chemical and Materials Engineering (SCME), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), Pakistan

2. Department of Applied Science and Technology, Politecnico di Torino, Corso Duca degli Abruzzi, 24, 10129 Torino, Italy

3. U.S.-Pakistan Centre for Advanced Studies in Energy (USPCAS-E), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), Pakistan

4. School of Chemical and Materials Engineering (SCME), National University of Sciences & Technology (NUST), Sector H-12 Islamabad (44000), Pakistan, Pakistan

Abstract

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). 

Funder

USPCAS-E and SCME NUST

Publisher

Bulletin of Chemical Reaction Engineering and Catalysis

Subject

Process Chemistry and Technology,Catalysis

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