Patent US4259478A successfully refreshed from Google Patents.
US4259478A
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Process for preparing high molecular weight copolyesters
Assignee: Eastman Chemical Co
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Filing: 1979-12-14
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Granted: 1981-03-31
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Expires: 1999-12-14
Abstract
Abstract Disclosed is a process for preparing linear, high molecular weight copolyesters from either (A) polyesters or copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent ethylene glycol or (B) copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3, the process comprising heating the polymer in the presence of 1,4-cyclohexanedimethanol to glycolize the polymer, distilling out ethylene glycol from the glycolysis mixture, and polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units. The process provides a fast polymerization rate and the polymers so produced can be used in the manufacture of plastics, fibers, films and other shaped objects having good physical properties.
Inventors
- 👤 Winston J. Jackson, Jr.
- 👤 Herbert F. Kuhfuss
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 09:19
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
189 words
Process for preparing linear, high molecular weight copolyesters from polymers selected from the group consisting of (A) polyesters or copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent ethylene glycol and (B) copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3, said process comprising (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 2
Dependent Claim
189 words
Process for preparing linear, high molecular weight copolyesters from polymers selected from the group consisting of (A) polyesters or copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent ethylene glycol and (B) copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3, said process comprising (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 3
Dependent Claim
16 words
Process according to claim 1 wherein said polymer has an inherent viscosity of at least 0.6.
Claim 4
Dependent Claim
19 words
Process according to claim 2 wherein said polymer has an inherent viscosity of from about 0.4 to about 0.7.
Claim 5
Dependent Claim
33 words
Process according to claim 1 wherein said polymer is heated to a temperature of about 275° C. in step (b) and maintained at such temperature for a time of at least 5 minutes.
Claim 6
Dependent Claim
133 words
Process for preparing linear, high molecular weight copolyesters from polyesters or copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent ethylene glycol which comprises (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 7
Dependent Claim
133 words
Process for preparing linear, high molecular weight copolyesters from polyesters or copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent ethylene glycol which comprises (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 8
Dependent Claim
45 words
Process according to claim 5 wherein the acid component of said polyester or copolyester comprises from about 70 to about 99.5 mole percent terephthalic acid and from about 30 to about 0.5 mole percent of an aliphatic, alicyclic or aromatic dicarboxylic acid other than terephthalic.
Claim 9
Dependent Claim
46 words
Process according to claim 5 wherein the diol component of said polyester or copolyester comprises from about 70 to about 99.5 mole percent of ethylene glycol and from about 30 to about 0.5 mole percent of another aliphatic glycol having from 2 to 8 carbon atoms.
Claim 10
Dependent Claim
147 words
Process for preparing linear, high molecular weight copolyesters from copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3, said process comprising (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 11
Dependent Claim
147 words
Process for preparing linear, high molecular weight copolyesters from copolyesters, the acid component of which consists of at least 70 mole percent terephthalic acid and the diol component of which consists of at least 70 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3, said process comprising (a) heating said polymer to a temperature of from about 200° C. to about 290° C. in the presence of about 3 mole percent to an amount equivalent to the mole percent of ethylene glycol of 1,4-cyclohexanedimethanol to thereby glycolize said polymer, (b) distilling out at least a portion of the ethylene glycol from the glycolysis mixture, and (c) polycondensing the glycolysis mixture to form a copolyester of which at least a portion of ethylene glycol units are replaced by 1,4-cyclohexanedimethanol units and the inherent viscosity is at least 0.4.
Claim 12
Dependent Claim
45 words
Process according to claim 8 wherein the acid component of said polyester or copolyester comprises from about 70 to about 99.5 mole percent terephthalic acid and from about 30 to about 0.5 mole percent of an aliphatic, alicyclic or aromatic dicarboxylic acid other than terephthalic.
Claim 13
Dependent Claim
60 words
Process according to claim 8 wherein the diol component of said polyester or copolyester comprises from about 70 to about 99.5 mole percent of a mixture of ethylene glycol and 1,4-cyclohexanedimethanol in a mole ratio of from 20:80 to 97:3 and from about 30 to about 0.5 mole percent of another aliphatic glycol having from 2 to 8 carbon atoms.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-03-30 | 1984-09-29 | 1985-03-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-03-30 | 1988-09-29 | 1989-03-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-03-30 | 1992-09-29 | 1993-03-31 | $7700.00 | Window Closed / Lapsed |