B01J35/64

PROCESS FOR PREPARING PHOSGENE

The present invention relates to a continuous process for preparing phosgene as well as a production unit for carrying out said process.

FCC CATALYST WITH ENHANCED MESOPOROSITY, ITS PREPARATION AND USE

Process for the preparation of a catalyst by adding, clay, boehmite, a first silica to form a slurry, digesting the slurry with a monoprotic acid to a pH of less than 4, adding one or more zeolites, adding a rare earth component to the slurry and mixing, adjusting the slurry pH to below 4 with monoprotic acid, adding a second silica anywhere in the preceding steps, destabilizing the slurry by raising the pH, shaping and collecting the resulting catalyst, wherein the resulting catalyst has enhanced mesoporosity.

FUNCTIONALIZED LIGNOCELLULOSE COMPOUND AND USES THEREOF

Provided is a methodology to improve soil performance by dispersing stabilized low C:N non-highly polymerized porous lignocellulose catalytic that improves porosity, carbon capture, and microbial activities.

Method for synthesizing mesoporous nano-sized ultra-stable Y zeolite

Methods for synthesizing a mesoporous nano-sized ultra-stable Y zeolite include combining a microporous Y zeolite having a SiO.sub.2/Al2O.sub.3 molar ratio of less than 5.2 with water to form a microporous Y zeolite slurry and heating the microporous Y zeolite slurry to 30? C. to 100? C. to form a heated microporous Y zeolite slurry. Further the method includes adding a 0.1M to 2.0M ammonium hexafluorosilicate solution and a 0.1M to 2.0M ammonium hydroxide solution in a drop-wise manner, either sequentially or simultaneously, to the heated microporous Y zeolite slurry to form a treated zeolite solution and holding the treated zeolite solution at 50? C. to 100? C. Finally the method includes filtering and washing the dealuminated solution with water to form an ultra-stable Y zeolite precursor, drying the ultra-stable Y zeolite precursor, and calcining the dried zeolite precursor to form the nano-sized ultra-stable Y zeolite.

Heavy hydrocarbon hydroprocessing catalyst and methods of making and using thereof
12048917 · 2024-07-30 · ·

The specification discloses a highly macroporous catalyst for hydroprocessing and hydroconversion of heavy hydrocarbon feedstocks. The high macroporosity catalyst incudes an inorganic oxide, molybdenum, and nickel components. It has a pore structure such that at least 18% of its total pore volume is in pores of a diameter greater than 5,000 angstroms and at least 25% of its total pore volume is in pores of a diameter greater than 1,000 angstroms. Preferably, the pore structure is bimodal. The catalyst is made by co-mulling the catalytic components with a high molecular weight polyacrylamide followed by forming the co-mulled mixture into a particle or an extrudate. The particle or extrudate is dried and calcined under controlled calcination temperature conditions to yield a calcined particle or extrudate of the high macroporosity catalyst composition.

Method for making a photocatalyst and treating dye-contaminated water

An efficient photocatalyst nanocomposite comprising reduced graphene oxide, noble metal, and a metal oxide prepared by a one-step method that utilizes date seed extract as a reducing and nanoparticle determining size agent. The photocatalyst of the invention is a more effective sunlight photocatalyst than that prepared by traditional method in the photo decomposition of organic compounds in contaminated water.

MIXTURE OF MONOBRANCHED AND POLYBRANCHED FATTY ACIDS
20240254408 · 2024-08-01 ·

A composition of branched fatty acids or esters thereof and the processes for preparing such compositions and to a process of producing a composition of branched C10-C24 fatty acids or esters thereof with a high portion, at least 70% by weight, of mono and polybranched C10-C24 fatty acids or esters thereof.

TITANIA PARTICLES AND A PROCESS FOR THEIR PRODUCTION

The present invention provides titania particles which are formed by providing a titania sol and spray drying the titania sol. A morphology of the dried titania particles is controlled by producing the titania sol from a TiO.sub.2 containing slurry and controlling the pH of the slurry to be 3 pH units or more from the iso-electric point of the titania by adding a peptizing agent to reduce an extent to which the titania sol is flocculated, or by producing the titania sol from a TiO.sub.2 containing slurry and adjusting the iso-electric point to be 3 pH units or more from the pH of the slurry by adding a dispersant to reduce an extent to which the titania sol is flocculated. The titania particles have a continuous exterior convex surface, a diameter of 30 m or less, a BET specific surface area of 50 m.sup.2/g or more, and are porous.

CATALYST CONTAINING PHOSPHATED KAOLIN AND ALUMINA FROM ACH AND METHOD OF USING THE SAME
20190070595 · 2019-03-07 ·

A catalyst for use in the thermocatalytic conversion of biomass contains alumina from aluminum chlorohydrate, phosphated kaolin and a calcined phosphated zeolite ZSM-5. The catalyst may be prepared by adding a slurry of particles of the calcined phosphated zeolite ZSM-5 to phosphoric acid and kaolin and then adding to the resulting product the aluminum chlorohydrate. The particles are then spray dried and calcined.

Exhaust gas purification apparatus

A exhaust gas purification apparatus is provided with; a substrate having a wall-flow structure and including entry-side cells, exit-side cells, and a porous partition; a first catalyst region formed in small diameter pores having relatively small pore diameters among internal pores in the partition; and a second catalyst region formed in large diameter pores having relatively large pore diameters among the internal pores in the partition. The first catalyst region contains a support and any one or two species of precious metal selected from Pt, Pd, and Rh loaded on the support, while the second catalyst region contains a support and any one or two species of precious metal selected from Pt, Pd, and Rh loaded on the support and other than at least the precious metal present in the first catalyst region.