US4086212A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Poly(ethylene/alkylene) terephthalates which crystallize rapidly
Assignee: Bayer AG
•
Filing: 1976-02-17
•
Granted: 1978-04-25
•
Expires: 1996-02-17
Abstract
Abstract Terephthalic copolyesters, the diol component of which mainly consists of ethylene glycol units, crystallize more rapidly than pure polyethylene terephthalate and can be moulded in a way comparable to polybutylene terephthalate.
Inventors
- 👤 Peter Bier
- 👤 Rudolf Binsack
- 👤 Hugo Vernaleken
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 23:17
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/02; C08G63/12; C08G63/16; C08G63/18; C08G63/181; C08G63/183; C08G63/78
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
152 words
A process for the production of thermoplastic terephthalic acid copolyesters which crystallize more rapidly than polyethylene terephthalate homopolymer comprising (1) esterifying or transesterifying an acid component consisting of (a) at least 90 mol % of terephthalic acid and dimethyl terephthalic acid ester, and (b) up to 10 mol % of other aliphatic and aromatic dicarboxylic acids and acid esters with (2) 1.05 to 2.04 equivalents of a diol component consisting of (a) 90 to 99.5 mol % of ethylene glycol, and (b) 10 to 0.5 mol % of 2,2-diethylpropane-1,3-diol at (3) a temperature of between 150° and 250° C in the presence of esterification or transesterification catalysts, and (4) polycondensing the initial reaction products at a temperature between 200 and 300° under reduced pressure in the presence of an esterification catalyst, wherein the 2,2-diethylpropane-1,3-diol is added to the reaction mixture after substantially all of the acid component has been reacted to di(2-hydroxyethyl)ester.
Claim 2
Dependent Claim
152 words
A process for the production of thermoplastic terephthalic acid copolyesters which crystallize more rapidly than polyethylene terephthalate homopolymer comprising (1) esterifying or transesterifying an acid component consisting of (a) at least 90 mol % of terephthalic acid and dimethyl terephthalic acid ester, and (b) up to 10 mol % of other aliphatic and aromatic dicarboxylic acids and acid esters with (2) 1.05 to 2.04 equivalents of a diol component consisting of (a) 90 to 99.5 mol % of ethylene glycol, and (b) 10 to 0.5 mol % of 2,2-diethylpropane-1,3-diol at (3) a temperature of between 150° and 250° C in the presence of esterification or transesterification catalysts, and (4) polycondensing the initial reaction products at a temperature between 200 and 300° under reduced pressure in the presence of an esterification catalyst, wherein the 2,2-diethylpropane-1,3-diol is added to the reaction mixture after substantially all of the acid component has been reacted to di(2-hydroxyethyl)ester.
Claim 3
Dependent Claim
8 words
The product of the process of claim 1.
Claim 4
Dependent Claim
34 words
The process of claim 1 wherein the 2,2-diethylpropane-1,3-diol is added to the reaction mixture after formation of a polyethylene terephthalate prepolymer with a degree of polymerization greater than 4 but before the polycondensation step.
Claim 5
Dependent Claim
82 words
A highly crystalline unbranched linear thermoplastic terephthalic acid copolyester which crystallizes more rapidly than polyethylene terephthalate homopolymer which consists of (1) an acid component consisting of (a) at least 90 mol % of terephthalic acid and dimethyl terephthalic acid ester and (b) up to 10 mol % of other aliphatic and aromatic dicarboxylic acids and acid esters, and (2) a diol component consisting of (a) 90 to 99.5 mol % of ethylene glycol, and (b) 10 to 0.5 mol % of 1,4-butane-diol.
Claim 6
Dependent Claim
82 words
A highly crystalline unbranched linear thermoplastic terephthalic acid copolyester which crystallizes more rapidly than polyethylene terephthalate homopolymer which consists of (1) an acid component consisting of (a) at least 90 mol % of terephthalic acid and dimethyl terephthalic acid ester and (b) up to 10 mol % of other aliphatic and aromatic dicarboxylic acids and acid esters, and (2) a diol component consisting of (a) 90 to 99.5 mol % of ethylene glycol, and (b) 10 to 0.5 mol % of 1,4-butane-diol.
References Cited (Backward Citations)
GB985936A
Cited
GB1118538A
Cited
US3714126A
Cited
US3592876A
Cited
GB1268442A
Cited
US3498952A
Cited
US3678128A
Cited
US3789031A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-04-24 | 1981-10-24 | 1982-04-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-24 | 1985-10-24 | 1986-04-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-24 | 1989-10-24 | 1990-04-25 | $7700.00 | Window Closed / Lapsed |