Liquid soak and steam vaporization restore zeolite pore access, recovering NOx conversion efficiency without muffler replacement.
Replacing erosion-prone orifice grids with disposable particulate beds eliminates plugging and vibration while maintaining reliable pressure reduction.
Modified Na-MOR catalyst with tetraalkyl ammonium exchange resolves activity stability trade-off, achieving 8000 hour lifetime.
Two-step impregnated composite catalyst stabilizes copper against high-temperature loss to increase chlorine yield from hydrogen chloride oxidation.
A catalytic reaction system adjusts reactor water levels to optimize catalyst performance.
A rapid synthesis method produces small-crystal-grain ZSM-5 molecular sieves using low-temperature nucleation and high-temperature crystallization growth.
Oxidized disulfide oil compounds replace conventional acids as peptization agents to form solid catalyst particles with comparable strength.
A copper-exchanged chabazite molecular sieve catalyst enables selective nitrogen oxide reduction in diesel exhaust systems.
Segmented catalyst stages optimize branching to improve low temperature properties while maintaining yield of high viscosity index lube base oils.
A titanium-silicalite molecular sieve synthesis method uses acetylacetone to regulate hydrolysis kinetics and maintain optimal titanium-oxygen-silicon bonding.
Hydrothermal conversion of zeolitic material to AEI framework type incorporating transition metal M.
Acid-washing mesoporous silica supports optimizes tantalum distribution, reducing by-product formation during ethanol to butadiene conversion.
Mesoporous zeolites disperse transition metals throughout the microporous framework to enhance catalytic activity and stability.
Segmented SCR catalyst converters with oxidation intermediaries reduce catalyst poisoning and maintain high NOx purification efficiency at low temperatures.
A phosphorus-modified rare earth Y-type molecular sieve uses ion exchange to locate ions in sodalite cages.
Pre-sintered mullite particles bond during firing to maintain structural integrity while reducing energy consumption and production time.
An upgrading reactor converts C3-C4 paraffins into aromatics within a methanol-to-gasoline process.
Amorphous Co-SiOx catalyst activates peroxymonosulfate through octahedral cobalt sites to degrade organic pollutants.
Purging residual hydrogen and olefins before mode switching prevents side reactions that reduce alkylate yield.
Sintered oxide coatings on wall-flow filters resist liquid water and minimize exhaust-gas back pressure.
Pre-loaded platinum molecular sieves increase diesel fuel yield and reduce cracking in hydroisomerization.
A Group 9 iridium catalyst complex with a ketone cocatalyst drives alkane dehydrogenation to generate olefins efficiently.
Specific Cu/Al and Ce/Al molar ratios in CHA zeolite prevent ammonia oxidation, maintaining NOx purification rates after thermal stress.
Metal catalysts in fluidized bed reactors convert carbohydrates to organic acids while preventing caramelization.
Reducing MCM-22 crystal agglomerate sizes below 16 microns improves monoalkylated aromatic compound selectivity by minimizing polyalkylated impurities.
A catalytic fluidized bed reactor converts olefinic naphtha and light paraffins into high-octane reformate using a zeolite catalyst.
Molding a high-solid plastic mixture of molecular sieves and insoluble metal precursors into shaped articles.
Blending narrow and broad molecular weight distribution polyethylenes balances moldability, impact strength, and transparency in thin-walled products.
Boric acid catalysts replace corrosive mineral acids to reduce equipment corrosion and wastewater complexity while maintaining esterification efficiency.
A hydroisomerization catalyst with a calcined zeolite support converts normal paraffins to isoparaffins.
Adding seeding agents allows zeolite X synthesis above 120°C, eliminating impurity phases while reducing duration.
Combining distinct organosilane templates tunes mesoporous BEA zeolite pore widths continuously, overcoming discrete template limitations.
Nitrogen metallophosphate catalysts enable biodiesel production from free fatty acid feeds without costly glycerin purification.
Hydrothermal conversion of FAU zeolites yields spherical LTL crystallites that reduce diffusion limitations and enhance catalyst activity.
Slurry processing creates homogeneous bifunctional catalysts that mitigate segregation and reduce deactivation during syngas to dimethyl ether conversion.
A vanadium-based catalyst with specific XRD peaks enables high conversion in halogenated aromatic nitrile production.
Atomic layer deposition deposits silicon-oxygen species onto amorphous silica-alumina to decouple pore size from acidity for biomass conversion.
Steamed zeolite catalysts convert alkyl halides into ethylene and propylene while suppressing aromatics and coke formation.
Metal-substituted USY zeolites boost olefin yield and selectivity, resolving the contradiction between high productivity and low conversion efficiency.
A chabazite-type zeolite catalyst incorporates copper and alkali earth metal ions to establish active catalytic centers for exhaust treatment.
A pre-hydrocarbon pooling device treats regenerated catalyst to form active species before conversion.
Cerium-tungsten composite catalysts expand the operational temperature window and resist sulfur poisoning.
Self-heating cerium zirconium catalyst eliminates external heating requirements by generating oxidation heat during ammonia decomposition.
A micro-spherical iron-based catalyst with modified structure promoters enhances mechanical strength and hydrocarbon selectivity.
A composite catalyst disperses nickel oxide within a transition metal oxide support to enhance catalytic activity.
Barrier particles prevent transition metal oxide aggregation during heat treatment, maintaining low-temperature purifying efficiency.
Nano-ZSM-5 molecular sieve modified with organosilanes to create an amphiphilic structure with lipophilic exterior and hydrophilic interior.
SSZ-92 molecular sieve catalyst suppresses cracking loss during dewaxing to improve base oil yield and quality.
A bifunctional catalyst system converts ketones directly into olefins through integrated hydrogenation and dehydration steps.
Replacing adamantane templates with cycloalkylammonium agents cuts synthesis costs while maintaining reliable CHA framework formation.