The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jul. 25, 2023

Filed:

Dec. 17, 2019
Applicant:

Eastman Chemical Company, Kingsport, TN (US);

Inventors:

Anne-Martine Sherbeck Jackson, Kingsport, TN (US);

Rachel Elizabeth McLendon, Kingsport, TN (US);

Bruce Roger DeBruin, Gray, TN (US);

Michael Paul Ekart, Kingsport, TN (US);

Dale Milton Blakely, Kingsport, TN (US);

Robert Todd Harris, Johnson City, TN (US);

Assignee:

Eastman Chemical Company, Kingsport, TN (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C08G 63/199 (2006.01); C08G 63/183 (2006.01); C08G 63/66 (2006.01);
U.S. Cl.
CPC ...
C08G 63/199 (2013.01); C08G 63/183 (2013.01); C08G 63/66 (2013.01);
Abstract

Process for preparing copolyesters by introducing TPA, EG, and CHDM at an EG:TPA molar ratio of 2.3:1 to 2.7:1 into a reaction zone; reacting TPA with EG and CHDM at a temperature of at least 250° C. and pressure of up to 40 psi to form a first esterification product; passing the first esterification product to a reaction zone; esterifying the first esterification product at a temperature of at least 250° C. and pressure of up to 20 psi to form a second esterification product, passing the second esterification product to a reaction zone; polycondensing the second esterification product in the presence of a catalyst to form a prepolymerization product; passing the prepolymerization product to one or more reaction zones; and polycondensing the prepolymerization product in the presence of the catalyst to form a copolyester comprising 1.0 wt % or less of DEG, without requiring the use of DEG-suppressing additives.


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