Exxonmobil Chemical Patents Inc.

Exxonmobil Research and Engineering Company

Exxonmobil Technology and Engineering Company

Timothy D Shaffer

Pamela Jean Wright

Michael F McDonald, Jr

Robert Norman Webb

Jo Ann M Canich

David Y Chung

Kevin Richard Squire

Kun Wang

John Scott Buchanan

David T Ferrughelli

Randall David Partridge

Michael Gerard Matturro

Arnold Lustiger

Huaxing Zhou

Scott Thomas Milner

Richard Dwight Hembree

James Richardson Lattner

Abhimanyu Onkar Patil

Donald N Schulz

Limin Song

Sunny Jacob

Jay L Reimers

Steven Lawrence Suib

John F Walzer, Jr

Man Kit Ng

James Peter Stokes

Suzzy C Ho

Anastasios I Skoulidas

Benjamin A McCool

Adriana S Silva

Victor DeFlorio

David Michael Fiscus

Yu Feng Wang

Thomas T Sun

Alexander I Norman

Partha Nandi

Johannes Matthieu Soulages

Joel Edward Schmieg

Krishnan Sankaranarayanan

Michael F Mcdonald

Scott T Milner

Deborah J Davis

Joseph N Christopher

Deborah Jean Davis

Srinivasan Rajagopalan

Madhavi Vadlamudi

Richard Cheng-Ming Yeh

George Akehurst

Beth A Winsett

Stephen M Wood

John A Clark

Leming Gu

Joseph A Maier

George Skic

August W Bosse

Yunlong Zhang

Jordan N Metz

J Davis Deborah

Robert N Webb

Adam H Scott

Richard C M Yeh

Ozcan Altintas

Michael F Mc Donald

Yuan-Ju R Chen

James P Stokes

Milind B Ajinkya

Benjamin A Mccool

Joel E Schmieg

Processes for chemically treating polyaromatic feedstock to form aromatic-containing oligomers or polymers are provided. The processes are characterized by treatment of a plurality of different polyaromatic hydrocarbon molecules and/or polyheterocyclic molecules present in polyaromatic feedstock with a first reagent so as to functionalize the molecules. Further treatment in a second step affords oligomeric or polymeric products which may be crosslinked. The products may be thermoplastic or thermoset materials and may find use in, for example, infrastructure applications, composites, fillers, fire retardants and 3-D printing materials.

Processes for functionalization and polymerization of polyaromatic feedstock

In some embodiments, the present disclosure provides a composition comprising 1) about 97.5 wt % to about 99.9 wt % of a first polyethylene having a density of about 0.91 g/cmto about 0.94 g/cm, and a melt strength of about 10 mN or greater; and 2) about 0.1 wt % to about 2.5 wt % of a second polyethylene having an Mw of about 500,000 g/mol or more. In some embodiments, the composition is a film. In some embodiments, the present disclosure provides a method of making a composition comprising blending a first polyethylene of any embodiment described herein and a second polyethylene of any embodiment described herein.

Enhanced processability of LLDPE by addition of ultra-high molecular weight density polyethylene

Processes and systems for producing olefin epoxides with three or more carbon atoms by oxidation of the corresponding branched hydrocarbons using oxygen are disclosed. An example process for producing olefin epoxides may include oxidizing a branched alkane to produce at least an organic hydroperoxide. The example process may further include epoxidizing a branched alkene by a catalytic reaction with least a portion of the organic hydroperoxide to produce at least an olefin epoxide and an alcohol. The example process may further include converting at least a portion of the alcohol to either additional branched alkane and/or additional branched alkene.

Process and system to make olefin epoxides

A method may include: oxidizing iso-butane with oxygen to produce t-butyl hydroperoxide and t-butyl alcohol; dehydrating at least a portion of the t-butyl alcohol to produce di-tert-butyl ether and isobutylene; epoxidizing at least a portion of the isobutylene with the t-butyl hydroperoxide to produce isobutylene oxide and t-butyl alcohol; and carbonylating at least a portion of the isobutylene oxide with carbon monoxide to produce pivalolactone.

The present disclosure relates to methods for preparing materials from heavy feedstocks. In particular, the disclosure provides a chemical process to convert heavy feedstocks with predominant polyaromatic hydrocarbon molecules or species, including the residues of petrochemical refining or extraction, into thermoset or thermoplastic materials that can be used alone or as a component in a composite material.

Methods for preparing materials from polyaromatic heavy feedstocks

A system for producing a functionalized olefinic-based polymer, the system comprising a polymerization zone for producing an olefinic-based polymer comprising a mixing section, a deliquifying section, and a quenching section, wherein at least one section of the polymerization zone has a defined cross-sectional area that continually decreases from a first end to a second end of said section; a devolatilization zone comprising a kneader or extruder, wherein said devolatilization zone is downstream of said polymerization zone and in fluid communication with said polymerization zone; and a functionalization zone downstream of said devolatilization zone and in fluid communication with said devolatilization zone.

System and process for the production of functionalized olefinic-based polymer

This disclosure describes a new route to acrylate esters via direct catalytic partial oxidation of allyl ether using heterogeneous manganese oxide catalysts. The method involves forming allyl acrylate by contacting allyl ether, where the allyl ether is in solution with a solvent, with one or more oxidants in the presence of a mesoporous manganese oxide (MnOx) catalyst. Oxygen or peroxide can be used as the oxidant. The yield of and selectivity for acrylate ester can be very high, and process efficiency is improved over current processes.

Direct catalytic partial oxidation of allyl ether

Copolymer are formed by polymerizing Cto Cisoolefin monomers and alkyl-styrene monomers. The method comprises first providing feed streams into a reactor. The various feed streams provide monomers, a polar diluent or polar diluent mixture, and a catalyst system into the reactor. In the reactor, the feed streams contact one another so that the monomers form a polymer in a stable slurry, wherein the amount of polymer in the slurry yields a slurry concentration greater than 22 wt %. The ratio of moles of polymer formed per mole initiator is in the range of 0.25 to 4.0 moles polymer per mole of initiator.

Methods of production of alkylstyrene/isoolefin polymers

The present invention is directed to a membrane for ethanol and aromatics separation that is stable in an alcohol containing environment. The membrane is a polyether epoxy resin having an aliphatic substituted epoxide. The invention also teaches a method to control the flux and selectivity of the membrane.

Ethanol stable polyether epoxy based membrane for ethanol and aromatics separation

Method of reducing fouling in an elastomer polymerization process that includes providing a reactor capable of housing an industrial-scale elastomer polymerization reaction, and applying a mechanical force to the reactor so as to create a vibration in at least one wall of the reactor, in which fouling is reduced in the reactor. In one embodiment the reaction is an industrial scale butyl polymerization reaction and the reactor is a butyl polymerization reactor.

Mitigation of elastomer reactor fouling using mechanical vibration

The disclosure provides for a process and polymerization system to produce isoolefin polymers () utilizing polymorphogenates () in the catalyst system to control polydispersity (MWD). The disclosure also provides a catalyst system () comprising a plurality of active catalyst complex species () formed by combination of a Lewis acid (), an initiator () and a polymorphogenate (), as well as polymers made using the catalyst system or process. The polymorphogenate () can promote or mimic the formation of different active catalyst complex species () having different polymerization rates, i.e. different rates of propagation, chain transfer, or termination, as observed by different polydispersities resulting from the presence of relatively different proportions of the polymorphogenate.

Polydispersity-controlled isoolefin polymerization with polymorphogenates

Provided for herein is a process to produce an essentially homogeneous single liquid phase hydrocarbon-rubber cement from a polymer slurry comprising a hydrocarbon-rubber, a diluent, and unreacted monomer(s), the process comprising:

Process to produce a hydrocarbon rubber cement utilizing a hydrofluorocarbon diluent

The present invention is directed to a membrane for aromatics separation that is stable in an alcohol containing environment. The polymeric membrane is a epoxy amine based membrane.

Ethanol stable epoxy amine based membrane for aromatics separation

The present invention relates to an in-line method for generating comonomer from monomer, such as ethylene. The comonomer generated is directly transported, without isolation or storage, to a polyethylene polymerization reactor. The in-line method includes the steps of providing an in-line comonomer synthesis reactor and a downstream gas/liquid phase separator prior to the polymerization reactor; feeding ethylene monomer and a catalyst in a solvent and/or diluent to the comonomer synthesis reactor; reacting the ethylene monomer and the catalyst in solvent and/or diluent under reaction conditions to produce an effluent stream including ethylene monomer and comonomer; passing the effluent stream from the comonomer synthesis reactor to the downstream gas/liquid phase separator to separate a gas stream from a bottom stream, wherein the gas stream is a mixture of ethylene monomer and comonomer; and passing the gas stream to the polymerization reactor to provide the necessary comonomer input.

In-line process for generating comonomer

Methods for producing elastomers or elastomeric compositions are provided. One or more Cto Cisoolefins and one or more comonomers can be polymerized in the presence of a diluent comprising one or more hydrofluorocarbons to provide a slurry comprising polymer product, unreacted monomer and the diluent. The slurry can be extruded to separate at least a portion of the diluent from the polymer product. The separated diluent can be recycled for polymerizing the one or more Cto Cisoolefins.

Separation of polymer slurries

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Hackettstown, NJ, United States of America

Timothy D Shaffer