US4143094A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for production of saturated, high-molecular weight polyesters
Assignee: Huels AG
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Filing: 1977-03-25
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Granted: 1979-03-06
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Expires: 1997-03-25
Abstract
Abstract A process for the production of pol-(butylene terephthalate) of sufficiently high molecular weight for subsequent extrusion processing without the need of a solid phase post-condensation and at polycondensation pressures greater than now in general use. Polycondensation is carried out in the presence of small amounts of copolymers of an α-olefin or styrene with free or esterified maleic acid or anhydride.
Inventors
- 👤 Klaus Burzin
- 👤 Jorn Ruter
- 👤 Roland Feinauer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 07:26
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78; C08G63/82; C08G63/87
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
220 words
In a two-stage process for the production of saturated, high-molecular weight polyesters whose acid component consists at least 70 molar percent of terephthalic acid and whose diol component consists at least 70 molar percent of 1,4-butanediol wherein the first stage is an interesterification reaction conducted at 150°-250° C. in the presence of an interesterification catalyst and wherein the second stage is a polycondensation reaction conducted at 200°-300° C. at reduced pressure in the presence of a polycondensation catalyst, the improvement which comprises conducting the polycondensation reaction in the presence of 0.005 - 2% by weight, based on the terephthalic acid, of a compound of the general formula ##STR2## having a molecular weight of 1,000 - 1,000,000 wherein a and b are each positive integers from 1 to 100; n is a positive integer from 10 to 10,000; R 1 and R 2 are each hydrogen, alkyl of 1-12 carbon atoms or phenyl; and R 3 and R 4 are each hydrogen, alkyl or hydroxy-alkyl of 1-4 carbon atoms, said compound either being added before the interesterification reaction, or during the interesterification reaction up to the beginning of the polycondensation reaction or, when the compound is a free acid, at any time up to the end of the polycondensation reaction, or said compound being formed during the interesterification or polycondensation reaction.
Claim 2
Dependent Claim
220 words
In a two-stage process for the production of saturated, high-molecular weight polyesters whose acid component consists at least 70 molar percent of terephthalic acid and whose diol component consists at least 70 molar percent of 1,4-butanediol wherein the first stage is an interesterification reaction conducted at 150°-250° C. in the presence of an interesterification catalyst and wherein the second stage is a polycondensation reaction conducted at 200°-300° C. at reduced pressure in the presence of a polycondensation catalyst, the improvement which comprises conducting the polycondensation reaction in the presence of 0.005 - 2% by weight, based on the terephthalic acid, of a compound of the general formula ##STR2## having a molecular weight of 1,000 - 1,000,000 wherein a and b are each positive integers from 1 to 100; n is a positive integer from 10 to 10,000; R 1 and R 2 are each hydrogen, alkyl of 1-12 carbon atoms or phenyl; and R 3 and R 4 are each hydrogen, alkyl or hydroxy-alkyl of 1-4 carbon atoms, said compound either being added before the interesterification reaction, or during the interesterification reaction up to the beginning of the polycondensation reaction or, when the compound is a free acid, at any time up to the end of the polycondensation reaction, or said compound being formed during the interesterification or polycondensation reaction.
Claim 3
Dependent Claim
20 words
A process according to claim 1, wherein said compound is a copolymer of maleic acid with styrene or an α-olefin.
Claim 4
Dependent Claim
21 words
A process according to claim 1, wherein said compound is an alkanol-esterified copolymer of maleic acid with styrene or an α-olefin.
Claim 5
Dependent Claim
15 words
A process according to claim 1, wherein 0.05-1% by weight of said compound is employed.
Claim 6
Dependent Claim
15 words
A process according to claim 1, wherein said compound is added before the interesterification reaction.
Claim 7
Dependent Claim
21 words
A process according to claim 1, wherein the polycondensation reaction is conducted at an absolute pressure of greater than 1 millibar.
Claim 8
Dependent Claim
13 words
A process according to claim 6, wherein said pressure is about 5-40 millibars.
Claim 9
Dependent Claim
51 words
A process according to claim 1 wherein the compound has a molecular weight of 10,000 - 200,000; a and be each are positive integers from 20-80; n is a positive integer from 200 - 8,000; and R 1 and R 2 are each hydrogen, alkyl of 1-6 carbon atoms, or phenyl.
Claim 10
Dependent Claim
13 words
A process according to claim 6, wherein said pressure is about 10-25 millibars.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-03-05 | 1982-09-04 | 1983-03-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-03-05 | 1986-09-04 | 1987-03-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-03-05 | 1990-09-04 | 1991-03-06 | $7700.00 | Window Closed / Lapsed |