Adsorbent beds strip oxygenates, aromatics, and other poisons from renewable paraffins before dehydrogenation to protect catalysts and preserve product purity.
A heat-transfer fluid and stabilizer enable selective fuel blending with lower polyaromatic by-products, fewer impurities, and less reactor coke.
A heat-transfer fluid and stabilizer route multistep olefin conversion toward cleaner monomers, cutting polyaromatics, impurities, and reactor coke.
A heat-transfer-fluid and stabilizer route converts isoprene to terpene-based SAF with useful MAHs, low PAHs, fewer impurities, and less coke.
Lewis acid oligomerization of C14/C16 mono-olefins yields PAO base stocks with higher viscosity index, lower volatility, and better 0W blending.
Wet air oxidation with ion exchange restores hydrogenation catalysts while cutting water use, regeneration time, and peroxide damage.
A butanol pre-impregnation step creates free pores that confine nickel to the alumina shell, improving hydrogenation activity and selectivity.
A staged ethanol conversion route uses hydroformylation, aldol condensation, and hydrogenation to make paraffinic motor fuels with lower CO2 emissions.
Metallocene-catalyzed polymerization of cyclic and linear alpha-olefins raises PAO dimer content for distinctive lubricant and specialty chemical properties.
Heat transfer fluid and stabilizer control terpene-forming reactions to limit PAHs, impurities, and coke in high-energy rocket fuel.
Butanol impregnation and maturation create a peripheral nickel phase and NiCu alloy that improve hydrogenation activity and selectivity with less nickel.
Controlled thermal alloying confines active layers to the metal foam surface, preserving core strength and fixed-bed catalyst stability.
A butanol impregnation and maturation sequence keeps nickel near the support shell, cutting nickel use while preserving hydrogenation activity and selectivity.
Blending HLD and IsoHLD traction fluid isomers lowers sub-zero viscosity while preserving EHD shear strength and reducing foaming at high speeds.
A low-value mixed decene by-product is oligomerized with C4-C6 alpha-olefins and hydrogenated to make SAF-range paraffins at lower cost.
A solvent-slurry reactor absorbs acetylene and hydrogen, controls reaction heat, and enables continuous catalyst regeneration for selective ethylene production.
Thermoluminescent catalyst particles remove heat as light and enable in-situ temperature mapping to prevent hot spots in exothermic fixed-bed reactions.
A cooled solvent recycle loop absorbs acetylene and manages reaction heat, enabling selective hydrogenation to ethylene with lower coke risk.
A heat transfer fluid and stabilizer improve tackifying polymer synthesis by limiting by-products, PAHs, and coke while maintaining high yield.
A heat-transfer fluid and stabilizer improve multistep fuel synthesis by limiting PAHs, impurities, and coke in continuous reactors.
A heat transfer fluid and stabilizer in the reactant mixture curb coke and polyaromatics while preserving high-selectivity olefin upgrading.