Hydrogen‐Free Production of Green Diesel from Deoxygenation of Methyl Palmitate via Cross‐Metathesis with Bio‐Ethylene Using Supported WO <sub>3</sub> Catalyst

dc.contributor.authorMochamad Solehudin
dc.contributor.authorKanokwan Wengwirat
dc.contributor.authorPratya Promchana
dc.contributor.authorYingyot Poo‐arporn
dc.contributor.authorWanwisa Limphirat
dc.contributor.authorKittisak Choojun
dc.contributor.authorTawan Sooknoi
dc.date.accessioned2026-05-08T19:18:52Z
dc.date.issued2025-5-16
dc.description.abstract) sites, yielding a C16-ene majority with trace amounts of C17-ene. Smaller hydrocarbons (<C15) are obtained as minor components from decarbonylation, hydrogen transfer, and cracking. The increased contact time (27-106 g h/mol) at 460 °C results in increased conversion (30%-87 %), green diesel (12%-57%), SAF (3.5%-12.7%), and bio-naphtha (1.3%-5.3%). Optimal green diesel production of 2.92 h⁻¹ with 73% selectivity can be achieved at 480 °C. SAF and bio-naphtha yields can be tuned by varying temperature from 460 to 500 °C. This provides a sustainable pathway for renewable liquid fuels without an external hydrogen supply.
dc.identifier.doi10.1002/asia.202401581
dc.identifier.urihttps://dspace.kmitl.ac.th/handle/123456789/16725
dc.publisherChemistry - An Asian Journal
dc.subjectCatalysis and Hydrodesulfurization Studies
dc.subjectCatalysis for Biomass Conversion
dc.subjectCarbon dioxide utilization in catalysis
dc.titleHydrogen‐Free Production of Green Diesel from Deoxygenation of Methyl Palmitate via Cross‐Metathesis with Bio‐Ethylene Using Supported WO <sub>3</sub> Catalyst
dc.typeArticle

Files

Collections