G. AbdulKareem-Alsultan, Nur Athirah Adzahar, G. Omer-Alsultan, N. Asikin-Mijan, H. V. Lee, Tonni Agustiono Kurniawan and Y. H. Taufiq-Yap
{"title":"Green diesel production via deoxygenation of triolein catalysed by nickel-molybdenum-supported catalysts","authors":"G. AbdulKareem-Alsultan, Nur Athirah Adzahar, G. Omer-Alsultan, N. Asikin-Mijan, H. V. Lee, Tonni Agustiono Kurniawan and Y. H. Taufiq-Yap","doi":"10.1039/D5RA04601G","DOIUrl":null,"url":null,"abstract":"<p >The deoxygenation of triolein into hydrocarbons has been carried out over NiO/CeO<small><sub>2</sub></small>, MoO<small><sub>2</sub></small>/CeO<small><sub>2</sub></small> and NiO–MoO<small><sub>2</sub></small>/CeO<small><sub>2</sub></small> under partial vacuum and solvent-free conditions. NiO–MoO<small><sub>2</sub></small>/CeO<small><sub>2</sub></small> exhibited a remarkably higher yield of hydrocarbons (65%) and <em>n</em>-C<small><sub>17</sub></small> selectivity (37%) in comparison with single metal oxide–supported CeO<small><sub>2</sub></small> catalysts. Interestingly, the rich acid–base character and excellent synergistic effect between Ni–Mo and CeO<small><sub>2</sub></small> positively impacted the deoxygenation reaction while suppressing the cracking reaction. The addition of Ni- and Mo-rich species deteriorated the deoxygenation activity. The highest hydrocarbon yield (77%) and <em>n</em>-C<small><sub>17</sub></small> selectivity (58%) can be achieved at a reaction temperature of 340 °C, 1 h of reaction time, 15 wt% of catalyst loading and 10 mbar of reaction pressure under partial vacuum conditions. Based on catalyst support comparison (CeO<small><sub>2</sub></small>, Al<small><sub>2</sub></small>O<small><sub>3</sub></small>, SiO<small><sub>2</sub></small>, and ZSM-5), CeO<small><sub>2</sub></small> is a promising catalyst support for the production of diesel-rich fuels <em>via</em> solvent-free catalytic deoxygenation of triolein.</p>","PeriodicalId":102,"journal":{"name":"RSC Advances","volume":" 45","pages":" 37876-37887"},"PeriodicalIF":4.6000,"publicationDate":"2025-10-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.rsc.org/en/content/articlepdf/2025/ra/d5ra04601g?page=search","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"RSC Advances","FirstCategoryId":"92","ListUrlMain":"https://pubs.rsc.org/en/content/articlelanding/2025/ra/d5ra04601g","RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
Abstract
The deoxygenation of triolein into hydrocarbons has been carried out over NiO/CeO2, MoO2/CeO2 and NiO–MoO2/CeO2 under partial vacuum and solvent-free conditions. NiO–MoO2/CeO2 exhibited a remarkably higher yield of hydrocarbons (65%) and n-C17 selectivity (37%) in comparison with single metal oxide–supported CeO2 catalysts. Interestingly, the rich acid–base character and excellent synergistic effect between Ni–Mo and CeO2 positively impacted the deoxygenation reaction while suppressing the cracking reaction. The addition of Ni- and Mo-rich species deteriorated the deoxygenation activity. The highest hydrocarbon yield (77%) and n-C17 selectivity (58%) can be achieved at a reaction temperature of 340 °C, 1 h of reaction time, 15 wt% of catalyst loading and 10 mbar of reaction pressure under partial vacuum conditions. Based on catalyst support comparison (CeO2, Al2O3, SiO2, and ZSM-5), CeO2 is a promising catalyst support for the production of diesel-rich fuels via solvent-free catalytic deoxygenation of triolein.
期刊介绍:
An international, peer-reviewed journal covering all of the chemical sciences, including multidisciplinary and emerging areas. RSC Advances is a gold open access journal allowing researchers free access to research articles, and offering an affordable open access publishing option for authors around the world.