Process intensified lauric acid self-ketonization and its economic and environmental impact on biolubricant base oil production

dc.contributor.authorGoculdas, Tejas
dc.contributor.authorYuliu, Zhifei
dc.contributor.authorSadula, Sunitha
dc.contributor.authorZheng, Weiqing
dc.contributor.authorSaha, Basudeb
dc.contributor.authorNanduri, Arvind
dc.contributor.authorIerapetritou, Marianthi
dc.contributor.authorVlachos, Dionisios G.
dc.date.accessioned2024-08-05T19:35:41Z
dc.date.available2024-08-05T19:35:41Z
dc.date.issued2024-07-03
dc.descriptionThis article was originally published in Green Chemistry. The version of record is available at: https://doi.org/10.1039/D4GC01721H . This journal is © The Royal Society of Chemistry 2024
dc.description.abstractLubricant base oils, traditionally derived from non-renewable petroleum, contribute significantly to greenhouse gas emissions. In contrast, oils sourced from furfural and long-chain ketones through aldol condensation and hydrodeoxygenation present a renewable, cost-effective, and environmentally friendly alternative, offering superior cold flow properties. However, the production of long-chain ketones, a crucial component, currently relies on solvent dewaxing in refineries, which is costly and non-selective. One promising biobased approach involves self-ketonization of long-chain fatty acids derived from coconut or palm kernel oils. This method typically employs high boiling point solvents like dodecane or is done in a batch configuration, limiting its scale and industrial viability. This study addresses this bottleneck by eliminating solvents, transitioning to a continuous flow reactor, and achieving kilogram-scale production of long-chain ketones with exceptional selectivity (90%). The lab-scale setup can yield up to 25 kg of 12-tricosanone per month, utilizing earth-abundant MgO as a catalyst. The catalyst underwent slight deactivation due to carbonate formation. Catalyst stabilization, using mixed metal oxides, and regeneration via simple calcination in air are also discussed. Techno-economic analysis (TEA) indicates a 29% lower minimum selling price than the commercial synthetic poly alpha olefin (PAO). Life cycle assessment (LCA) evaluates the global warming potential (GWP) under different environmental assumptions. Under the carbon-neutral assumption for lauric acid production, an 8.9% reduction in GWP was achieved compared to petroleum-based lubricants.
dc.description.sponsorshipThis work was supported as part of the Delaware Biosciences Center for Advanced Technology grant with award number 12A00448 and a Small Business Innovation Research grant from the Department of Energy, award number DE-SC0021559.
dc.identifier.citationGoculdas, Tejas, Zhifei Yuliu, Sunitha Sadula, Weiqing Zheng, Basudeb Saha, Arvind Nanduri, Marianthi Ierapetritou, and Dionisios G. Vlachos. “Process Intensified Lauric Acid Self-Ketonization and Its Economic and Environmental Impact on Biolubricant Base Oil Production.” Green Chemistry 26, no. 15 (2024): 8818–30. https://doi.org/10.1039/D4GC01721H.
dc.identifier.issn1463-9270
dc.identifier.urihttps://udspace.udel.edu/handle/19716/34645
dc.language.isoen_US
dc.publisherGreen Chemistry
dc.rightsAttribution 3.0 Unporteden
dc.rights.urihttp://creativecommons.org/licenses/by/3.0/
dc.subjectresponsible consumption and production
dc.subjectclimate action
dc.subjectindustry, innovation and infrastructure
dc.titleProcess intensified lauric acid self-ketonization and its economic and environmental impact on biolubricant base oil production
dc.typeArticle

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