Promoting effect of CaO-MgO mixed oxide on Ni/γ-Al2O3 catalyst for selective catalytic deoxygenation of palm oil
Autor: | S. AlKhoori, Steven J. Hinder, Kyriakos N. Papageridis, Savvas Douvartzides, Maria A. Goula, Mark A. Baker, Victor Sebastian, Kyriaki Polychronopoulou, Nikolaos D. Charisiou |
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Přispěvatelé: | Hellenic Foundation for Research and Innovation, General Secretariat of Research and Technology (Greece), University of Western Macedonia, Abu Dhabi National Oil Company, Khalifa University, European Commission |
Rok vydání: | 2020 |
Předmět: |
060102 archaeology
Renewable Energy Sustainability and the Environment Chemistry 020209 energy Vegetable oil refining chemistry.chemical_element Palm oil 06 humanities and the arts 02 engineering and technology Renewable diesel Catalysis Crystallinity Adsorption Chemical engineering Selective deoxygenation Desorption 0202 electrical engineering electronic engineering information engineering Mixed oxide 0601 history and archaeology Nickel based catalysts Deoxygenation Carbon |
Zdroj: | Digital.CSIC. Repositorio Institucional del CSIC instname |
ISSN: | 0960-1481 |
DOI: | 10.1016/j.renene.2020.09.133 |
Popis: | The study presented herein examines, for the first time in the literature, the role of CaO-MgO as a modifier of γ-Αl2O3 for Ni catalysts for the production of green diesel through the deoxygenation of palm oil. The characteristics of the catalytic samples were examined by N2 adsorption/desorption, XRD, NH3-TPD, CO2-TPD, H2-TPR, XPS and TEM analysis. The carbon deposited on the catalytic surfaces was characterized by TPO, Raman and TEM/HR-TEM. Experiments were conducted between 300 and 400 °C, at 30 bar. Maximum triglyceride conversion and the yield of the target n–C15–n–C18 paraffins increased with temperature up to 375 °C for both catalysts. Both samples promoted deCO2 and deCO deoxygenation reactions much more extensively than HDO. However, although both catalysts exhibited similar activity at the optimal temperature of 375 °C, the Ni/modAl was more active at lower reaction temperatures, which can be probably understood on the basis of the increased dispersion of Ni on its surface and its lower acidity, which suppressed hydrocracking reactions. Time-on-stream experiments carried out for 20 h showed that the Ni/modAl catalyst was considerably more stable than the Ni/Al, which was attributed to the lower amount and lower crystallinity of the carbon deposits and to the suppression of sintering due to the presence of the CaO-MgO modifiers. KNP is grateful for the support of the Hellenic Foundation for Research and Innovation (HFRI) and the General Secretariat for Research and Technology (GSRT), under the HFRI PhD Fellowship grant (GA. no. 359). MAG and NDC gratefully acknowledge that this researched was co-financed by Greece and the European Union (European Social Fund- ESF) through the Operational Programme «Human Resources Development, Education and Lifelong Learning» (MIS-5050170). SD is thankful for financial assistance provided by the Research Committee of the University of Western Macedonia (grant number 70277). KP acknowledges the financial support from the Abu Dhabi Department of Education and Knowledge (ADEK) under the AARE 2019-233 grant and support by the Khalifa University of Science and Technology under Award No. RC2-2018-024. |
Databáze: | OpenAIRE |
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