C07C27/16

Trans-metallated MOF catalyst

A metal organic framework comprising zinc (II) ions and second metal ions, such as iron (II) ions, cobalt (II) ions, and copper (II) ions as nodes or clusters and coordinated 1,3,5-benzenetricarboxylic acid struts or linkers between them forming a porous coordination network in the form of polyhedral crystals that are isostructural to HKUST-1. Transmetallation processes for producing the metal organic frameworks, as well as methods for applications of the metal organic frameworks as catalysts, specifically catalysts for the oxidation of cyclic hydrocarbons, such as toluene, cyclohexane, and methylcyclohexane.

TRANS-METALLATED MOF CATALYST

A metal organic framework comprising zinc (II) ions and second metal ions, such as iron (II) ions, cobalt (II) ions, and copper (II) ions as nodes or clusters and coordinated 1,3,5-benzenetricarboxylic acid struts or linkers between them forming a porous coordination network in the form of polyhedral crystals that are isostructural to HKUST-1. Transmetallation processes for producing the metal organic frameworks, as well as methods for applications of the metal organic frameworks as catalysts, specifically catalysts for the oxidation of cyclic hydrocarbons, such as toluene, cyclohexane, and methylcyclohexane.

TRANS-METALLATED MOF CATALYST

A metal organic framework comprising zinc (II) ions and second metal ions, such as iron (II) ions, cobalt (II) ions, and copper (II) ions as nodes or clusters and coordinated 1,3,5-benzenetricarboxylic acid struts or linkers between them forming a porous coordination network in the form of polyhedral crystals that are isostructural to HKUST-1. Transmetallation processes for producing the metal organic frameworks, as well as methods for applications of the metal organic frameworks as catalysts, specifically catalysts for the oxidation of cyclic hydrocarbons, such as toluene, cyclohexane, and methylcyclohexane.

IRIDIUM-BASED CATALYST AND PREPARATION METHOD THEREFOR, AND HYDROFORMYLATION METHOD
20240336545 · 2024-10-10 ·

Provided in the present invention is an iridium-based catalyst, which is characterized in that the chemical structural formula of the iridium-based catalyst is:

##STR00001## wherein Ph is a phenyl, R is a methyl or an ethyl, and X is one or more of CH.sub.3CO.sub.2, NO.sub.3, Cl, BF.sub.4, PF.sub.6 and SbF.sub.6. In the present invention, a rhodium-based catalyst in the prior art is replaced with the iridium-based catalyst, such that the reaction cost is reduced, and the yield of reactants is increased.

IRIDIUM-BASED CATALYST AND PREPARATION METHOD THEREFOR, AND HYDROFORMYLATION METHOD
20240336545 · 2024-10-10 ·

Provided in the present invention is an iridium-based catalyst, which is characterized in that the chemical structural formula of the iridium-based catalyst is:

##STR00001## wherein Ph is a phenyl, R is a methyl or an ethyl, and X is one or more of CH.sub.3CO.sub.2, NO.sub.3, Cl, BF.sub.4, PF.sub.6 and SbF.sub.6. In the present invention, a rhodium-based catalyst in the prior art is replaced with the iridium-based catalyst, such that the reaction cost is reduced, and the yield of reactants is increased.

Method for olefin hydroformylation using iridium-based catalyst

Provided in the present invention is an iridium-based catalyst, which is characterized in that the chemical structural formula of the iridium-based catalyst is: ##STR00001## wherein Ph is a phenyl, R is a methyl or an ethyl, and X is one or more of CH.sub.3CO.sub.2, NO.sub.3, Cl, BF.sub.4, PF.sub.6 and SbF.sub.6. In the present invention, a rhodium-based catalyst in the prior art is replaced with the iridium-based catalyst, such that the reaction cost is reduced, and the yield of reactants is increased.

Method for olefin hydroformylation using iridium-based catalyst

Provided in the present invention is an iridium-based catalyst, which is characterized in that the chemical structural formula of the iridium-based catalyst is: ##STR00001## wherein Ph is a phenyl, R is a methyl or an ethyl, and X is one or more of CH.sub.3CO.sub.2, NO.sub.3, Cl, BF.sub.4, PF.sub.6 and SbF.sub.6. In the present invention, a rhodium-based catalyst in the prior art is replaced with the iridium-based catalyst, such that the reaction cost is reduced, and the yield of reactants is increased.

Metal organic frameworks as catalysts and hydrocarbon oxidation methods thereof

A metal organic framework comprising zinc (II) ions and second metal ions, such as iron (II) ions, cobalt (II) ions, and copper (II) ions as nodes or clusters and coordinated 1,3,5-benzenetricarboxylic acid struts or linkers between them forming a porous coordination network in the form of polyhedral crystals that are isostructural to HKUST-1. Transmetallation processes for producing the metal organic frameworks, as well as methods for applications of the metal organic frameworks as catalysts, specifically catalysts for the oxidation of cyclic hydrocarbons, such as toluene, cyclohexane, and methylcyclohexane.

Metal organic frameworks as catalysts and hydrocarbon oxidation methods thereof

A metal organic framework comprising zinc (II) ions and second metal ions, such as iron (II) ions, cobalt (II) ions, and copper (II) ions as nodes or clusters and coordinated 1,3,5-benzenetricarboxylic acid struts or linkers between them forming a porous coordination network in the form of polyhedral crystals that are isostructural to HKUST-1. Transmetallation processes for producing the metal organic frameworks, as well as methods for applications of the metal organic frameworks as catalysts, specifically catalysts for the oxidation of cyclic hydrocarbons, such as toluene, cyclohexane, and methylcyclohexane.

Method of producing C2-C4 carbonyl compounds

The invention relates to a method of producing carbonyl compounds, more particularly C.sub.2-C.sub.4 ketones and aldehydes. The method is based on the gas-phase oxidation by nitrous oxide of C.sub.2-C.sub.4 alkane-olefin mixtures, such as a butane-butylene fraction or a propane-propylene fraction, obtained by thermal and/or catalytic cracking, to produce C.sub.2-C.sub.4 ketones and aldehydes. The process is carried out under continuous flow conditions at a temperature of 300-550 C. and pressure of 1-100 atm, without prior isolation of individual olefins from the fractionation products and in the absence of a catalyst. The process provides for high productivity, high overall selectivity for ketones and aldehydes, and explosion-safe operation.