Eastman Chemical Company

Damon Ray Billodeaux

Daniel Latham Terrill

Thomas James Devon

Kenneth Wayne Hampton, Jr

Jerome Leonard Stavinoha, Jr

Adam Scott Howard

Brian David McMurray

James Lon Little

Xianchun Wu

Daryl Bitting

David Eugene Slivensky

Neil Warren Boaz

Bruce Roger DeBruin

Charles Edwan Sumner, Jr

Robert Thomas Hembre

Brent Alan Tennant

Matthew Allen Boone

Stephanie Kay Clendennen

Chad Johnson

Kristof Moonen

Kim Dumoleijn

Vasudev R Bhonde

Robert Scott Huss

Stijn Simonne Paul Van De Vyver

Kenny Randolph Parker

Scott Donald Barnicki

David William Norman

Michael Gary Polasek

Jonathan Michael Penney

Robert Jacks Sharpe

Joseph Alexander Deloach

Curtis Schilling, Iii

Pinguan Zheng

Carey Dan Ashcroft

Melissa Dawn Page

Jennifer Lynn Cogar

Manik Lal Saha

Cornelius Johannes Hermans

Magnus Alexander Pauly

Michelle Nicole Tuttle

Chad A Johnson

Disclosed is the use of glycol ether aryl ester plasticizers as viscosity reducing agents in plastisols comprising di(2-ethylhexyl) terephthalate, 1,2-cyclohexane dicarboxylic acid diisononyl ester, or diisononyl phthalate as the primary plasticizer. The glycol ether aryl ester plasticizers improve viscosity and viscosity stability while maintaining or improving plastisol properties such as Shore A Hardness and fusion time.

Glycol ether aryl ester plasticizer

A pyrolysis method and system are provided that enhances the production of C3 and C4 alkanes in the resulting pyrolysis effluent. More particularly, the disclosed pyrolysis method and system may be configured to enhance the production of C3 and C4 alkanes due to the use of certain pyrolysis catalysts and more intense pyrolysis conditions.

Pyrolysis method and system for recycled waste

Methods and systems are provided for the conversion of waste plastics into various useful downstream recycle-content products. More particularly, the present system and method involves integrating a pyrolysis facility with a cracker facility by introducing at least a stream of r-pyrolysis gas into the cracker facility. In the cracker facility, the r-pyrolysis gas may be separated to form one or more recycle content products, and can enhance the operation of the facility.

Chemical recycling of plastic-derived streams to a cracker separation zone with enhanced separation efficiency

Processes are disclosed for preparing carboxylic acids from organic esters, the processes comprising contacting an ester with water in the presence of an acid catalyst and a homogenizing solvent at conditions effective to form a carboxylic acid. The homogenizing solvent is present in an amount sufficient to form a single-phase reaction mixture comprising the ester, water, and homogenizing solvent. The homogenizing solvent may be selected from acetonitrile, dimethyl sulfoxide, and 1,4-dioxane.

Processes for producing carboxylic acids

Compositions from the chemical recycling of plastic-derived streams and uses thereof

An efficient process useful for the self-condensation of aliphatic aldehydes is provided, catalyzed by dialkylammonium carboxylate salts. In particular, the invention provides a facile method for the preparation of 2-ethyl hexenal via the self-condensation of butyraldehyde using various dialkylammonium carboxylates, e.g., diisopropylammonium acetate or dimethylammonium acetate, as catalyst. Additionally, residual nitrogen arising from the catalyst can be reduced to −100 ppm levels in the product via a simple washing procedure. The invention provides a process for preparing alkenals under conditions which limit the formation of undesired impurities and high-boiling oligomeric substances.

Self-condensation of aldehydes

The invention provides branched trialkylamine oxides with improved properties. The trialkylamine oxides of the invention produced from branched trialkylamines, in one embodiment, can be made using certain branched C10-12 enals and aldehydes. The invention also provides an trialkylamine oxide having the formula: wherein R5, R6 and R7 are independently at least one of C3H7, C2H5, CH3, or H, or mixtures thereof; and wherein R5 and R6 are not H at the same time. In one embodiment, the trialkylamine oxides of the invention can be useful in making various products, for example, as surfactants.

Branched trialkyl amine oxides

The surfactants which can be produced from the trialkylamine intermediates include the quaternary ammonium compounds of formula: 

Branched trialkyl quaternary ammonium compounds

The oxidation of isobutyraldehyde produces isobutyric acid and byproducts, such as isopropyl formate. A process of reducing the isopropyl formate byproduct and other byproducts in the oxidation of isobutyraldehyde is described. The process uses a carbonyl compound, such as acetone, to reduce byproduct levels in the resulting product. Process for use of static mixers in oxidation reactions of aldehydes are also provided.

Aldehyde oxidation processes

The invention is comprised of a coalescent and non-ionic surfactant blend additive for use in water-based architectural coating formulations. The dual-function blend is produced by reacting 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate with ethylene oxide in the presence of a basic catalyst and separating the desired ethoxylated coalescent and non-ionic surfactant blend from the reaction product.

Coalescent and non-ionic surfactant blend

A process for making a cyclic compounds such as cyclic acetal or cyclic ketones by feeding aldehyde or ketone compounds and polyhydroxyl compounds to a reaction zone at a molar ratio of polyhydroxyl compounds to aldehyde or ketone compounds of at least 3:1, reacting these compounds in the presence of a solid acid such as an acidic ion exchange resin, to generate a liquid reaction mixture without separating water from the reaction mixture as it is being formed in the reaction mixture, withdrawing the liquid reaction mixture from the reaction zone as a liquid product stream, and feeding the liquid reaction product stream to a distillation column to separate cyclic acetal compounds from unreacted polyhydroxyl compounds, and optionally recycling back the unreacted polyhydroxyl compounds to the reaction zone. The process produces cyclic acetal compounds in yields of at least 90% with long catalyst life. The process is also suitable to make cyclic ketals from ketone compounds.

Production of cyclic acetals or ketals using solid acid catalysts

A liquid composition containing at least 2 mole % of water, at least 50 mole % of polyhydroxyl compounds, at least 3 mole % of cyclic compounds, and at least 0.01 mole % of a homogeneous acid catalyst. The mole percentages are based on the moles of all liquids in the composition. The liquid composition optionally contains up to 20 mole % of carbonyl compounds, based on the number of moles of the cyclic compounds. The cumulative amount of any other liquid ingredient in the liquid composition does not exceed 10 mole %. The cyclic compounds include cyclic acetals, cyclic ketals, or a combination thereof. The liquid composition is derived from a process for making cyclic compounds by feeding aldehyde or ketone compounds and polyhydroxyl compounds to a reaction vessel at a molar ratio of polyhydroxyl compounds to aldehyde or ketone compounds of at least 3:1, reacting these compounds in the presence of a homogeneous acid catalyst to generate a liquid phase homogeneous reaction mixture containing the acid catalyst without separating water from the reaction mixture as it is being formed in the reaction mixture, withdrawing the liquid phase homogeneous reaction mixture from the reaction vessel as a liquid product stream, and feeding the liquid reaction product stream to a distillation column to separate cyclic acetal or ketal compounds from unreacted polyhydroxyl compounds.

Production of cyclic acetals or ketals using liquid-phase acid catalysts

A liquid phase hydrogenolysis of acetal compounds, such as cyclic acetals and cyclic ketals, is disclosed. The acetal compounds are fed to a reaction zone and reacted in the presence of a noble metal catalyst supported on a carbon or silica support to make hydroxy mono-ether compounds in high selectivity, without the necessity of using acidic co-catalysts such as phosphorus containing acids or stabilizers such as hydroquinone.

Production of hydroxy ether hydrocarbons by liquid phase hydrogenolysis of cyclic acetals or cyclic ketals

Catalyst compositions of alumina supports containing palladium and nickel are selective in a vapor phase hydrogenolyzis reaction to convert cyclic acetal compounds and/or cyclic ketal compounds in the presence of hydrogen to their corresponding hydroxy ether hydrocarbon reaction products.

Nickel modified catalyst for the production of hydroxy ether hydrocarbons by vapor phase hydrogenolysis of cyclic acetals and ketals

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Longview, TX, United States of America

Damon Ray Billodeaux