Exxonmobil Chemical Patents Inc.

Mobil Oil Corporation

Exxonmobil Oil Corporation

Badger Licensing LLC

Other

William Alois Weber

Stephen Harold Brown

Jose G Santiesteban

Zhaozhong Jiang

J Scott Buchanan

Reuel Shinnar

Francis S Bryan

Richard Henry Schlosberg

David H Olson

Robert A Ware

Larry Arthur Green

Robert James Saxton

Charles Morris Smith

Robert A Crane, Jr

John Scott Buchanan

Hye-Kyung Cho Timken

David Lawrence Stern

Jane C Cheng

Mark F Mathias

Robert A Crane

Ronald Joseph Cimini

David Anthony Stachelczyk

Walter R Cade

Keith Holroyd Kuechler

Wenyih Frank Lai

Doron Levin

Jeffrey S Beck

Ajit Bhaskar Dandekar

Rene B LaPierre

Hye Kyung Cho Timken

John Richard Shutt

Jane Chi-Ya Cheng

Khushrav E Nariman

Michael Alan Steckel

Michael Alan Better

Frank Lai

Jane Chi Ya Cheng

An oligomerization process in which hydrocarbon feedstocks are contacted with a hydrotreating catalyst in the absence of hydrogen and in the liquid phase. The catalyst is a heterogeneous catalyst selected from supported reduced metals, metals oxides, metal sulfides and combinations thereof. Preferred catalysts include mixed nickel and molybdenum oxides or mixed cobalt and molybdenum oxides. The process also oligomerizes sulfur compounds so that sulfur containing feedstocks can be treated without deactivating the catalysts.

Conversion of unsaturated chemicals to oligomers

An integrated process for the production of a dialkyl carbonate and a diol from an alkylene oxide, carbon dioxide and an aliphatic monohydric alcohol is described in which an alkylene oxide is first reacted with carbon dioxide in the presence of a halogen-free carbonation catalyst to provide a corresponding cyclic carbonate and the cyclic carbonate is then reacted with an aliphatic monohydric alcohol in the presence of the carbonation catalyst and/or a transesterification catalyst and recycling the carbonation catalyst to provide a corresponding dialkyl carbonate and diol, wherein the dialkyl carbonate product exhibits a halogen concentration of about 5 ppm or less.

Low corrosive integrated process for preparing dialkyl carbonates

In a process for converting C+ aromatic hydrocarbons to lighter aromatic products a feed comprising C+ aromatic hydrocarbons is contacted under transalkylation reaction conditions with a catalyst composition comprising (i) a first molecular sieve selected from the group consisting of ZSM-12, mordenite and a porous crystalline inorganic oxide material having an X-ray diffraction pattern including d-spacing maxima at 12.4&#xb1;0.25, 6.9&#xb1;0.15, 3.57&#xb1;0.07 and 3.42&#xb1;0.07; and (ii) a second molecular sieve having a constraint index ranging from 3 to 12. At least the first molecular sieve has a hydrogenation component associated therewith and the first and second molecular sieves are contained in the same catalyst bed. The C+ aromatic hydrocarbons are converted under the transalkylation reaction conditions to a reaction product containing xylene.

Using a catalyst having two different zeolites for transalkylation of a C9+ aromatic feed

A process for the production of a dialkyl carbonate and a diol, such as dimethyl carbonate and ethylene glycol, by reacting a feed containing a cyclic carbonate, a hydroxy alkyl carbonate and an aliphatic monohydric alcohol in the presence of a transesterification catalyst is described. In another aspect, a process is described which is particularly useful for producing unsymmetric dialkyl carbonates, such as ethyl methyl carbonate.

Process for the production of unsymmetric and/or symmetric dialkyl carbonates and diols

A process for the disproportionation of cumene is disclosed which comprises the step of contacting a feed containing cumene, under disproportionation conditions, with a catalyst comprising a molecular sieve, preferably TEA-mordenite. The contacting step disproportionates at least part of the cumene in the feed to provide a disproportionation effluent containing benzene and a mixture of diisopropylbenzene isomers. The effluent is then recovered and contains, prior to any separation step, less 1% of ortho-diisopropylbenzene by weight of the total diisopropylbenzene content of said effluent, less than 1 wt % of n-propylbenzene, less than 5 wt % of triisopropylbenzenes and less than 5 wt % of disproportionation products other than benzene and diisopropylbenzenes.

Production of diisopropylbenzene by disproportion of cumene in the presence of a TEA-mordenite catalyst

Heavy aromatics processing

An integrated process for the production of a dialkyl carbonate and a diol from an alkylene oxide, carbon dioxide and an aliphatic monohydric alcohol is described in which an alkylene oxide is first reacted with carbon dioxide in the presence of a homogeneous carbonation catalyst to provide a corresponding cyclic carbonate and the cyclic carbonate is then reacted with an aliphatic monohydric alcohol in the presence of the homogeneous carbonation catalyst and/or a heterogeneous transesterification catalyst and recycling the homogeneous carbonation catalyst to provide a corresponding dialkyl carbonate and diol.

Integrated process for preparing dialkyl carbonates with a circulating catalyst

The present invention provides a process for producing a monoalkylated aromatic compound, particularly cumene, comprising the step of contacting a polyalkylated aromatic compound with an alkylatable aromatic compound under at least partial liquid phase conditions and in the presence of a transalkylation catalyst to produce the monoalkylated aromatic compound, wherein the transalkylation catalyst comprises a mixture of at least two different crystalline molecular sieves, wherein each of said molecular sieves is selected from zeolite beta, zeolite Y, mordenite and a material having an X-ray diffraction pattern including d-spacing maxima at 12.4&#xb1;0.25, 6.9&#xb1;0.15, 3.57&#xb1;0.07 and 3.42&#xb1;0.07 Angstrom.

Alkylaromatics production

Production of diisopropylbenzene

A process for treating methane-containing natural gas is provided which comprises: i) converting methane to methanol at or near a site of natural gas production; ii) transporting the methanol to a refinery remote from said site of production, said refinery producing ethylene and propylene and comprising an alkylation unit which can utilize a propylene feed; and iii) converting said methanol to gasoline boiling range fuel product and petrochemicals, including ethylene, propylene, butenes and xylenes.

Process for integrating a methanol conversion unit with an FCC unit

Growing community of inventors

Burlington, NJ, United States of America

William Alois Weber