Deep eutectic solvents extract bio-oil from algae, removing phospholipids that deactivate hydrogenation catalysts.
Supported metal catalyst with egg-shell active phase distribution enables selective fatty acid conversion.
Replacing insoluble calcium oxides with soluble salts enables mild-temperature reactions, preventing oxidation and polymerization while boosting yield.
Copper and magnesium promoters form stable alloy crystallites that resist dissolution, extending catalyst lifetime in fatty acid hydrogenation.
Hydrolytic cracking splits fatty acid esters into glycerol and free fatty acids before selective hydrogenation.
An integrated process converts renewable organic material into high-value chemicals using hydrotreatment, thermal cracking, and fractionation.
Zirconia or titania carriers prevent leaching in hydrotreating reactions, ensuring long-term stability against water deactivation.
Metathesized unsaturated polyol esters replace silicones to prevent oxidation and off odors while maintaining stability.
High-pressure hydrolysis removes impurities from lipid feeds, protecting hydrotreating catalysts and reducing propane by-products.
Partial deoxygenation of biomass pyrolysis oil reduces production costs while maintaining sufficient energy density for burner applications.
Chloro-1,5-cyclooctadiene iridium dimer converts unsaturated fatty acids into bio-based fuels with controlled aromatic content.
A fat composition with controlled lauric, palmitic, and stearic acid ratios delivers specific solid fat content profiles.
A renewable fuel intermediate composition forms through ketopyrolysis of lipid feedstocks using a metal oxide catalyst.
A graphene-supported catalyst with nickel, palladium, and ruthenium enhances reaction kinetics.
Internal cooling substance injection regulates reactor temperature during bio-based material hydrogenation.
Hydroprocessing biological feedstock yields a renewable hydrocarbon fuel that reduces polycyclic aromatic hydrocarbons while maintaining petrodiesel density.