Oligomerizing C4 olefins with a zeolite catalyst yields jet-range hydrocarbons with smooth boiling distributions.
Oxygen pretreatment of phosphorus-modified zeolite catalysts delays deactivation from carbonaceous deposits, maintaining high p-xylene selectivity.
Dual-function catalysts convert ketones to olefins in one step, avoiding side reactions that lower propylene selectivity.
A sulfur-tolerant zeolite catalyst oligomerizes impure ethylene from FCC off-gas, eliminating costly purification steps.
Di(cyclopentylmethyl)dimethylammonium cations direct SSZ-63 molecular sieve crystallization.
Jet fuel composition with controlled aromatic content prevents deposit formation in turbine engines during high-temperature operation.
Aerosol synthesis creates spherical zeolite-silica particles that trap metallic species, preventing refractory phase formation during sulfurization.
Segmenting the reactor into multiple secondary zones manages uneven carbon deposition, resolving low selectivity in methanol-to-olefins processes.
A fluidized bed reactor process converts methanol into dimethyl ether using integrated heat exchange and catalyst regeneration.
Solid acid catalysts enable high single-pass conversion of cyclic olefins to esters, overcoming low yield and complex separation issues in traditional routes.
Composite manganese carbonate Fischer-Tropsch catalyst and zeolite solid acid produce high-octane gasoline fractions from syngas.
Acid treatment lowers plasticity of titanium-containing MWW zeolite, enabling extrusion shaping while preserving catalytic activity.
A reduced template zeolite beta catalyst contacts olefins and alcohols to produce monoalkyl ethers with high purity.
A hydrogenation catalyst with 15 to 40 angstrom pores saturates aromatics in lubricating oil feedstreams.
Mechanical agitation contacts solid polyolefins with a solid catalyst below 100°C, reducing energy consumption compared to high-temperature pyrolysis.
Replacing corrosive triflic acid with a solid acid catalyst reduces capital investment for equipment metallurgy while maintaining product quality.
Impregnating catalytic precursors with dialkyl succinates and carboxylic acids to maintain Keggin heteropolyanions without calcination.
A composite catalyst of copper sulfate and zeolite converts glycerin to acrolein with high selectivity.
Segmented chlorination, purging, and decoking steps restore spent aromatization catalyst activity while reducing corrosivity in metal reactors.
Silicoalumina composites resolve the contradiction between thermal stability and catalytic performance by increasing mesoporous volume.
Adjusting impregnation solution pH to 1-5.5 stabilizes metal deposition during hydroprocessing catalyst manufacturing.
Segmented perforated catalyst carriers enable larger tube diameters while maintaining precise temperature control in exothermic reactions.
A porous carbon catalyst with phenolic hydroxyl groups converts cellulose into glucose.
Synthesizing organic-free metal-containing zeolite Beta eliminates costly structure directing agents while maintaining high NOx conversion rates.
A solid acid and metal catalyst converts naphthenic compounds into branched paraffins to boost lubricant viscosity index.
Amine functionalized zeolites introduce primary amine functionalities and silazane groups to the microporous framework.
Hydrothermal synthesis of β-type iron silicate uses controlled fluorine to resolve the contradiction between high metal dispersion and prolonged synthesis time.
Acid-functionalized silica gel catalyzes polyol transesterification to produce cyclic carbonates, eliminating toxic phosgene and costly enzyme requirements.
Alkali-exchanged zeolite catalysts resist deactivation from acetone impurities, extending effective life during acetic acid production.
Single-substrate zoned catalyst merges oxidation and SCR functions to boost CO conversion while lowering pressure drop in gas turbines.
Zeolite catalysts selectively combust hydrogen into water, preventing organic compounds from oxidizing into carbon dioxide.
Binder mediates zeolite dispersion to maintain high porosity, reducing diffusion resistance during aromatic alkylation.
Bifunctional catalyst oxidizes hydrogen chloride to chlorine gas while incinerating chlorobenzene impurities, preventing polychlorinated benzene accumulation.
A bifunctional catalyst performs simultaneous hydrocracking and hydroisomerization to produce high-quality lube base stocks.