B01J2231/646

MESOPOROUS AND MACROPOROUS NICKEL-BASED CATALYST HAVING A MEDIAN MACROPORE DIAMETER OF BETWEEN 50 NM AND 200 NM AND ITS USE WITH REGARD TO HYDROGENATION

Disclosed are a supported catalyst, its method of preparation and use in hydrogenation methods, which catalyst contains an oxide substrate that is for the most part calcined aluminum and an active phase that contains nickel, with the nickel content between 5 and 65% by weight in relation to the total mass of the catalyst, with the active phase not containing a metal from group VIB, the nickel particles having a diameter that is less than or equal to 20 nm, the catalyst having a median mesopore diameter of between 14 nm and 30 nm, a median macropore diameter of between 50 and 200 nm, a mesopore volume that is measured by mercury porosimetry that is greater than or equal to 0.40 mL/g, and a total pore volume that is measured by mercury porosimetry that is greater than or equal to 0.42 mL/g.

Organosilica materials and uses thereof

Methods of preparing organosilica materials, which are a polymer comprising of at least one independent cyclic polyurea monomer of Formula ##STR00001##
wherein each R.sup.1 is a Z.sup.1OZ.sup.2Z.sup.3SiZ.sup.4 group, wherein each 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 unit; each Z.sup.2 and Z.sup.3 independently represent a hydroxyl group, a C.sub.1-C.sub.4 alkyl group, a C.sub.1-C.sub.4 alkoxy group or an oxygen atom bonded to a silicon atom of another monomer unit; and each Z.sup.4 represents a C.sub.1-C.sub.8 alkylene group bonded to a nitrogen atom of the cyclic polyurea are provided herein. Methods of preparing and processes of using the organosilica materials, e.g., for gas separation, color removal, etc., are also provided herein.

Coating methods using organosilica materials and uses thereof

Methods for coating a substrate with a coating including an adsorbent material and a binder comprising an organosilica material which is a polymer comprising independent units of Formula [Z.sup.3Z.sup.4SiCH.sub.2].sub.3 (I), wherein each Z.sup.3 represents a hydroxyl group, a C.sub.1-C.sub.4 alkoxy group or an oxygen atom bonded to a silicon atom of another unit or an active site on the substrate and each Z.sup.4 represents a hydroxyl group, a C.sub.1-C.sub.4 alkoxy group, a C.sub.1-C.sub.4 alkyl group, an oxygen atom bonded to a silicon atom of another unit or an active site on the substrate are provided. Methods of gas separation are also provided.

Methods of separating aromatic compounds from lube base stocks

Methods are provided herein for separating an aromatic compound from a lube base stock by contacting a lube base stock containing an aromatic compound with an organosilica material.

Methods for selectively hydrogenating substituted arenes with supported organometallic catalysts

Methods for selectively hydrogenating substituted arenes with a supported organometallic hydrogenating catalyst are provided. An exemplary method includes contacting a substituted arene-containing reaction stream with hydrogen in the presence of a supported organometallic hydrogenating catalyst under reaction conditions effective to selectively hydrogenate the substituted arenes to the cis isomer with high selectivity. In this method, the supported organometallic hydrogenating catalyst includes a catalytically active organometallic species and a Brnsted acidic sulfated metal oxide support.

UNSUPPORTED HYDROGENATION CATALYST, ITS PREPARATION AND APPLICATION THEREOF
20240399351 · 2024-12-05 ·

Disclosed is an unsupported hydrogenation catalyst, its preparation and application thereof. The unsupported hydrogenation catalyst is composed of a complex formed by bonding a metal central atom or central ion with an organic ligand through coordination bond, wherein the metal is selected from the group consisting of Group VB metals, Group VIB metals, Group VIII metals, Group IB metals or combinations thereof that have a hydrogenation activity. The organic ligand comprises a hydrocarbyl moiety and a coordinating group, and forms a coordination bond with the metal central atom or central ion through an oxygen atom. The unsupported hydrogenation catalyst can be used for hydrogenation reaction of hydrocarbons, and has high oil solubility, dispersibility and hydrogenation activity.

OLEFIN POLYMERIZATION CATALYST SYSTEM COMPRISING MESOPOROUS ORGANOSILICA SUPPORT

A catalyst system comprising a combination of: 1) one or more catalyst compounds having at least one nitrogen linkage and at least one oxygen linkage to a transition metal; 2) a support comprising an organosilica material, which is a mesoporous organosilica material; and 3) an optional activator. Useful catalysts include ONNO-type transition metal catalysts, ONYO-Type transition metal catalysts, and/or oxadiazole transition metal catalysts. The organosilica material is a polymer of at least one monomer of Formula [z0Z2 SiCH2]3(1), where Z.sup.1 represents a hydrogen atom, a C.sub.1-C.sub.4alkyl 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.4alkoxy group, a C.sub.1-C.sub.6alkyl 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.

A 6-substituted Chiral Pure Difluoropiperidine Quinazoline Derivative And Its Preparation Method
20250092015 · 2025-03-20 ·

The present disclosure discloses a preparation method for 6-substituted chiral pure difluoropiperidine quinazoline derivative, in particular the 6-substituted chiral pure difluoropiperidine quinazoline derivative shown in Formula (I).

##STR00001##

The preparation method provided by the present disclosure is characterized by high chiral selectivity, high yield, and good process stability, which is of great significance for further production scale-up and commercialization of said solid drugs.

NANOHYBRID CATALYST FOR HYDROGENATION REACTIONS

A nanohybrid material includes a plurality of gold nanohybrid particles having formula (I). The gold nanohybrid particles have a gold nanoparticle (AuNPs) core and a shell of at least one fatty acid derivative at least partially disposed around the AuNPs core. The AuNPs core has a cuboidal shape and an average particle size of 20 to 60 nanometers (nm). Each R.sub.1, and R.sub.2 are independently selected from the group consisting of a hydrgon atom, and a fatty acid hydrocarbon chain having 16 to 22 carbon atoms. R.sub.3 is selected from the group consisting of a hydrogen atom, an alkyl, an alkoxy, an optionally substituted alkoxy having 1 to 10 carbon atoms, and an optionally substituted alkoxyalky.

##STR00001##

Catalytic hydrogenation using complexes of base metals with tridentate ligands

Complexes of cobalt and nickel with tridentate ligand PNHP.sup.R are effective for hydrogenation of unsaturated compounds. Cobalt complex [(PNHP.sup.Cy)Co(CH.sub.2SiMe.sub.3)]BAr.sup.F.sub.4 (PNHP.sup.Cy=bis[2-(dicyclohexylphosphino)ethyl]amine, BAr.sup.F.sub.4=B(3,5-(CF.sub.3).sub.2C.sub.6H.sub.3).sub.4)) was prepared and used with hydrogen for hydrogenation of alkenes, aldehydes, ketones, and imines under mild conditions (25-60 C., 1-4 atm H.sub.2). Nickel complex [(PNHP.sup.Cy)Ni(H)]BPh.sub.4 was used for hydrogenation of styrene and 1-octene under mild conditions. (PNP.sup.Cy)Ni(H) was used for hydrogenating alkenes.