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Ahmed H, Alotibi MF, Fakeeha AH, Ibrahim AA, Abasaeed AE, Osman AI, Al‐Awadi AS, Alarifi N, Al‐Fatesh AS. Hydrogen Production via Methane Decomposition over Alumina Doped with Titanium Oxide-Supported Iron Catalyst for Various Calcination Temperatures. ChemistryOpen 2024; 13:e202300173. [PMID: 38085118 PMCID: PMC11004458 DOI: 10.1002/open.202300173] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 08/24/2023] [Revised: 11/23/2023] [Indexed: 04/11/2024] Open
Abstract
The decomposition of methane has been chosen as an alternative method for producing hydrogen. In this study, 20 % Fe was used as the active metal part of the catalyst. To better comprehend the impact of the supporting catalytic properties, alumina and titania-alumina composite were investigated as supports. Iron-based catalysts were prepared by impregnation method and then calcined at different temperatures (300 °C, 500 °C, and 800 °C). The catalysts were examined at 800 °C under atmospheric pressure with a 15 mL/min total flow rate and 2 : 1 CH4 to N2 feed ratio. The textural and morphological characteristics of the fresh calcined and spent catalysts were investigated. The catalytic activity and stability data demonstrated that Fe supported over TiO2-Al2O3 calcined at 500 °C performed the best of all evaluated catalysts with a more than 80 % hydrogen yield. The Raman spectra result showed that graphitic carbon was produced for all used titanium dioxide catalysts. Moreover, according to transmission electron microscopy (TEM) results, the carbon deposited on the catalysts' surface is carbon nanotubes (CNT).
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Affiliation(s)
- Hamid Ahmed
- College of EngineeringKing Saud UniversityP.O. Box 800Riyadh11421 (Kingdom ofSaudi Arabia
| | - Mohammed F. Alotibi
- Institute of Refining and Petrochemicals TechnologiesKing Abdulaziz City for Science and Technology (KACST)P.O. Box 6086Riyadh11442Kingdom of Saudi Arabia
| | - Anis H. Fakeeha
- College of EngineeringKing Saud UniversityP.O. Box 800Riyadh11421 (Kingdom ofSaudi Arabia
| | - Ahmed A. Ibrahim
- College of EngineeringKing Saud UniversityP.O. Box 800Riyadh11421 (Kingdom ofSaudi Arabia
| | - Ahmed E. Abasaeed
- College of EngineeringKing Saud UniversityP.O. Box 800Riyadh11421 (Kingdom ofSaudi Arabia
| | - Ahmed I. Osman
- School of Chemistry and Chemical EngineeringQueen's University BelfastBelfastBT9 5AGNorthern Ireland (UK
| | | | - Naif Alarifi
- Institute of Refining and Petrochemicals TechnologiesKing Abdulaziz City for Science and Technology (KACST)P.O. Box 6086Riyadh11442Kingdom of Saudi Arabia
| | - Ahmed S. Al‐Fatesh
- College of EngineeringKing Saud UniversityP.O. Box 800Riyadh11421 (Kingdom ofSaudi Arabia
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Saconsint S, Srifa A, Koo-Amornpattana W, Assabumrungrat S, Sano N, Fukuhara C, Ratchahat S. Development of Ni-Mo carbide catalyst for production of syngas and CNTs by dry reforming of biogas. Sci Rep 2023; 13:12928. [PMID: 37558901 PMCID: PMC10412613 DOI: 10.1038/s41598-023-38436-8] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/21/2023] [Accepted: 07/07/2023] [Indexed: 08/11/2023] Open
Abstract
Biogas has been widely regarded as a promising source of renewable energy. Recently, the direct conversion of biogas over heterogeneous catalysts for the simultaneous production of syngas and carbon nanotubes exhibits a high potential for full utilization of biogas with great benefits. Involving the combined dry reforming of methane and catalytic decomposition of methane, the efficiency of process is strongly depended on the catalyst activity/stability, mainly caused by carbon deposition. In this study, Ni-Mo catalyst is engineered to provide a life-long performance and perform high activity in the combined process. The surface modification of catalysts by a controlled carburization pretreatment is proposed for the first time to produce a carbide catalyst along with improving the catalyst stability as well as the reactivity for direct conversion of biogas. The performance of as-prepared carbide catalysts is investigated with comparison to the oxide and metallic ones. As a result, the Ni-Mo2C catalyst exhibited superior activity and stability over its counterparts, even though the condensed nanocarbon was largely grown and covered on the surface. In addition, up to 82% of CH4 conversion and 93% of CO2 conversion could remain almost constant at 800 °C throughout the entire test period of 3 h under a high flowrate inlet stream of pure biogas at 48,000 cm3 g-1 h-1. The XPS spectra of catalysts confirmed that the presence of Mo2C species on the catalyst surface could promote the stability and reactivity of the catalyst, resulting in higher productivity of carbon nanotubes over a longer time.
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Affiliation(s)
- Supanida Saconsint
- Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand
| | - Atthapon Srifa
- Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand
| | - Wanida Koo-Amornpattana
- Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand
| | - Suttichai Assabumrungrat
- Department of Chemical Engineering, Faculty of Engineering, Center of Excellence in Catalysis and Catalytic Reaction Engineering, Chulalongkorn University, Bangkok, 10330, Thailand
| | - Noriaki Sano
- Department of Chemical Engineering, Faculty of Engineering, Kyoto University, Kyoto, 615-8510, Japan
| | - Choji Fukuhara
- Department of Applied Chemistry and Biochemical Engineering, Graduate School of Engineering, Shizuoka University, Shizuoka, 432-8561, Japan
| | - Sakhon Ratchahat
- Department of Chemical Engineering, Faculty of Engineering, Mahidol University, Nakhon Pathom, 73170, Thailand.
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