C07C15/24

Anti-foulant formulation for compressors
10745345 · 2020-08-18 · ·

Disclosed are compositions and methods for preventing or reducing polymer formation and polymer deposition in equipment used in petrochemical processes. An antifoulant composition includes a combination of one or more antioxidants; one or more antipolymerants; one or more dispersants; and one or more solvents. A method of preventing or reducing fouling of process equipment used in an industrial process is also described. The method includes introducing into the process equipment an antifoulant composition, the antifoulant composition comprising a combination of one or more antioxidants; one or more antipolymerants; one or more dispersants; and one or more solvents.

Anti-foulant formulation for compressors
10745345 · 2020-08-18 · ·

Disclosed are compositions and methods for preventing or reducing polymer formation and polymer deposition in equipment used in petrochemical processes. An antifoulant composition includes a combination of one or more antioxidants; one or more antipolymerants; one or more dispersants; and one or more solvents. A method of preventing or reducing fouling of process equipment used in an industrial process is also described. The method includes introducing into the process equipment an antifoulant composition, the antifoulant composition comprising a combination of one or more antioxidants; one or more antipolymerants; one or more dispersants; and one or more solvents.

Desulfurization and Sulfur Tolerant Hydrogenation Processes of Hydrocarbon Feedstocks
20200231882 · 2020-07-23 ·

The present invention relates to the use of adsorbents comprising zinc oxide nanowires decorated with catalytically active metal particles for the removal of sulfur from hydrocarbon feedstocks, including the desulfurization of diesel fuels and the deep desulfurization of natural gas, and to the use of decorated zinc oxide nanowire adsorbents for the hydrogenation of naphthalene selectively to tetralin in the presence of sulfur compounds. The adsorbent comprises nickel metal particles or nickel-zinc alloy particles deposited on zinc oxide nanowires.

Desulfurization and Sulfur Tolerant Hydrogenation Processes of Hydrocarbon Feedstocks
20200231882 · 2020-07-23 ·

The present invention relates to the use of adsorbents comprising zinc oxide nanowires decorated with catalytically active metal particles for the removal of sulfur from hydrocarbon feedstocks, including the desulfurization of diesel fuels and the deep desulfurization of natural gas, and to the use of decorated zinc oxide nanowire adsorbents for the hydrogenation of naphthalene selectively to tetralin in the presence of sulfur compounds. The adsorbent comprises nickel metal particles or nickel-zinc alloy particles deposited on zinc oxide nanowires.

Oxygen-free direct conversion of methane and catalysts therefor

A process of methane catalytic conversion produces olefins, aromatics, and hydrogen under oxygen-free, continuous flowing conditions. Such a process has little coke deposition and realizes atom-economic conversion. Under the conditions encountered in a fixed bed reactor (i.e. reaction temperature: 750-1200 C.; reaction pressure: atmospheric pressure; the weight hourly space velocity of feed gas: 1000-30000 ml/g/h; and fixed bed), conversion of methane is 8-50%. The selectivity of olefins is 30-90%. And selectivity of aromatics is 10-70%. The catalyst for this methane conversion has a SiO.sub.2-based matrix having active species that are formed by confining dopant metal atoms in the lattice of the matrix.

Oxygen-free direct conversion of methane and catalysts therefor

A process of methane catalytic conversion produces olefins, aromatics, and hydrogen under oxygen-free, continuous flowing conditions. Such a process has little coke deposition and realizes atom-economic conversion. Under the conditions encountered in a fixed bed reactor (i.e. reaction temperature: 750-1200 C.; reaction pressure: atmospheric pressure; the weight hourly space velocity of feed gas: 1000-30000 ml/g/h; and fixed bed), conversion of methane is 8-50%. The selectivity of olefins is 30-90%. And selectivity of aromatics is 10-70%. The catalyst for this methane conversion has a SiO.sub.2-based matrix having active species that are formed by confining dopant metal atoms in the lattice of the matrix.

AN APPROACH TO A BOTTOM-UP SYNTHESIS OF NANOCARBONS
20200148541 · 2020-05-14 ·

Provided is a method for the synthesis of a -conjugated system from oligofurans, under conditions involving cycloaddition.

AN APPROACH TO A BOTTOM-UP SYNTHESIS OF NANOCARBONS
20200148541 · 2020-05-14 ·

Provided is a method for the synthesis of a -conjugated system from oligofurans, under conditions involving cycloaddition.

POLYFUNCTIONAL CATALYSTS
20200031735 · 2020-01-30 ·

Embodiments of the present disclosure describe catalysts, methods of preparing catalysts, methods of forming hydrocarbons using the catalysts, and the like.

POLYFUNCTIONAL CATALYSTS
20200031735 · 2020-01-30 ·

Embodiments of the present disclosure describe catalysts, methods of preparing catalysts, methods of forming hydrocarbons using the catalysts, and the like.