Provided is a NaY molecular sieve and a method for preparing the NaY molecular sieve, an HY molecular sieve and a method for preparing the HY molecular sieve, a hydrocracking catalyst, and a hydrocracking method. The average grain diameter of the NaY molecular sieve is 2-5 m, and the sum of pore volumes of pores in 1-10 nm diameter accounts for 70-90% of the total pore volume of the NaY molecular sieve. The HY molecular sieve obtained from the large-grain NaY molecular sieve can be used as an acidic component in the hydrocracking catalyst. When the hydrocracking catalyst containing the HY molecular sieve is applied in the hydrocracking reaction of heavy oils that contain macromolecules, it can provide better cracking activity and product selectivity in the hydrocracking reaction.

Carbide-derived carbons are provided that have high dynamic loading capacity for high vapor pressure gasses such as H.sub.2S, SO.sub.2, or NH.sub.3. The carbide-derived carbons can have a plurality of metal chloride or metallic nanoparticles entrapped therein. Carbide-derived carbons are provided by extracting a metal from a metal carbide by chlorination of the metal carbide to produce a porous carbon framework having residual metal chloride nanoparticles incorporated therein, and annealing the porous carbon framework with H.sub.2 to remove residual chloride by reducing the metal chloride nanoparticles to produce the metallic nanoparticles entrapped within the porous carbon framework. The metals can include Fe, Co, Mo, or a combination thereof. The carbide-derived carbons are provided with an ammonia dynamic loading capacity of 6.9 mmol g.sup.1 to 10 mmol g.sup.1 at a relative humidity of 0% RH to 75% RH.

Processes for converting a hydrocarbon reactant into an alcohol compound and/or a carbonyl compound are disclosed in which the hydrocarbon reactant and a supported transition metal catalystcontaining molybdenum, tungsten, or vanadiumare irradiated with a light beam at a wavelength in the UV-visible spectrum, optionally in an oxidizing atmosphere, to form a reduced transition metal catalyst, followed by hydrolyzing the reduced transition metal catalyst to form a reaction product containing the alcohol compound and/or the carbonyl compound.

The present disclosure relates to a ZIF-8 metal-organic framework catalyst composite including: a ZIF-8 metal-organic framework in a metal-organic framework; and water molecules provided inside the ZIF-8 metal-organic framework.

A method for producing a nitrogen-modified mesoporous and dendritic carbon material includes preparing a carbon precursor comprising a metal acetylide. The carbon precursor is mixed with a nitrogen precursor to form a starter mixture. Thereafter, a first heat treatment of the starter mixture is carried out at a temperature in the range of 40 to 80? C. under vacuum to form a metal inclusion compound. In a next step, a second heat treatment is carried out at a temperature in the range of 120 to 220? C. to produce an intermediate by decomposing the metal inclusion compound under a vacuum. The intermediate is treated to remove the metal, and finally consolidation of the treated intermediate is carried out by a third heat treatment at a temperature in the range of 200 to 1000? C. under vacuum or in an inert gas atmosphere to obtain the nitrogen-modified mesoporous and dendritic carbon material. Also described is a nitrogen-modified mesoporous and dendritic carbon material and a fuel cell comprising the carbon material.

The disclosed technology provides processes for producing hydrogen that is renewable, has negative carbon intensity, and is associated with net water production. The hydrogen is economically, environmentally, and socially superior to conventional hydrogen via steam reforming of natural gas or electrolysis of water. Some variations provide a process for manufacturing carbon-negative hydrogen and optionally activated carbon, comprising: feeding biomass into a first heated vessel or zone to generate dried biomass and a first recovered water stream; feeding the dried biomass into a second heated vessel or zone to pyrolyze the dried biomass, generating a biocatalyst and a biogas; feeding the biocatalyst, the first recovered water stream, and biogas to a third heated vessel or zone for biocatalytic conversion, thereby generating H.sub.2, CO, and optionally activated carbon; and recovering the hydrogen. The H.sub.2 is carbon-negative hydrogen characterized by a carbon intensity less than 0 kg CO.sub.2e per metric ton H.sub.2.

A process for selective partial hydrogenation of conjugated diene compounds includes at least one, preferably terminal, diene function and at least one additional carbon-carbon double bond, the process including reacting the conjugated diene compounds with hydrogen in the presence of an iridium-NHC based catalyst. The disclosure also relates to a reaction mixture that can be obtained at the end of the process. The disclosure also relates to the use of the reaction mixture.

Provided is a process for producing satisfactory particles held in porous silica. The process comprises (a) the step of preparing porous silica, (b) the step of bringing the porous silica into contact with a liquid which contains either a metal or a compound that has the metal as a component element and infiltrating the liquid into the pores of the porous silica, and (c) the step of subjecting, after the step (b), the impregnated porous silica to a heat treatment to thereby form fine particles comprising the metal or the metal compound in the pores of the porous silica. When porous silica is synthesized by hydrolyzing an alkoxysilane in a solvent-free system, it is possible to synthesize porous silica having a fine pore diameter. Use of this porous silica as a template facilitates formation of particles (e.g., W, Cu, Cr, Mn, Fe, Co, or Ni or an oxide of any of these metals) that show peculiar properties not observed in the bulk material.

A catalyst system comprising a combination of: 1) an activator; 2) one or more metallocene catalyst compounds; 3) a support comprising an organosilica material, which may be a mesoporous organosilica material. The organosilica material may be a polymer of at least one monomer of Formula [Z.sup.1OZ.sup.2SiCH.sub.2].sub.3 (I), where Z.sup.1 represents a hydrogen atom, a C.sub.1-C.sub.4 alkyl group, or a bond to a silicon atom of another monomer and Z.sup.2 represents a hydroxyl group, a C.sub.1-C.sub.4 alkoxy group, a C.sub.1-C.sub.6 alkyl group, or an oxygen atom bonded to a silicon atom of another monomer. This invention further relates to processes to polymerize olefins comprising contacting one or more olefins with the above catalyst system.

Disclosed herein are base metal catalyst devices for removing ozone, volatile organic compounds, and other pollutants from an air flow stream. A catalyst device includes a housing, a solid substrate disposed within the housing, and a catalyst layer disposed on the substrate. The catalyst layer includes a first base metal catalyst at a first mass percent, a second base metal catalyst at a second mass percent, and a support material impregnated with at least one of the first base metal catalyst or the second base metal catalyst.