US4133800A
Expired / Lapsed
US
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Polyester production
Assignee: Imperial Chemical Industries Ltd
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Filing: 1976-11-15
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Granted: 1979-01-09
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Expires: 1996-11-15
Abstract
Abstract Polyesters, e.g. polyethylene terephthalate, are produced by a direct esterification process. The esterification is performed in the presence of a germanium dioxide polycondensation catalyst dissolved in an alkaline ethylene glycol solution. The alkali in the catalyst solution acts as the softening point stabilizer. An antimony polycondensation catalyst is also employed.
Inventors
- 👤 Robert P. L. V. Taubinger
- 👤 Robert B. Rashbrook
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 19:18
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78; C08G63/82; C08G63/83; C08G63/85; C08G63/86
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
229 words
In a process for the production of a linear aromatic polyester which comprises: (a) esterifying at least one aromatic dicarboxylic acid with ethylene glycol at an elevated temperature and in the presence of an alkali metal hydroxide; (b) polycondensing the product of (a), without isolation, under reduced pressure and in the presence of antimony trioxide in amount 100 to 1,000 parts per million by weight of the dicarboxylic acid originally present and triphenyl phosphate stabilizer; the improvement which comprises carrying out step (a) in the presence of a solution of germanium dioxide in an alkali metal hydroxide and a diol having its hydroxyl groups attached to adjacent carbon atoms, the amount of germanium dioxide being 10 to 200 parts per million by weight based on the amount of dicarboxylic acid present at the start of the reaction and the amount of the alkali metal hydroxide is at least one equivalent per mole of the germanium dioxide, said antimony trioxide being added to the product of (a) after completion of the esterification reaction and the amount of said alkali metal hydroxide is: (i) greater than the equivalent per mole of germanium dioxide; (ii) greater than 0.5 gram equivalents per million grams of the dicarboxylic acid; (iii) less than the greater of twice the equivalent per mole of germanium dioxide and 2.5 gram equivalents per million grams of the dicarboxylic acid.
Claim 2
Dependent Claim
229 words
In a process for the production of a linear aromatic polyester which comprises: (a) esterifying at least one aromatic dicarboxylic acid with ethylene glycol at an elevated temperature and in the presence of an alkali metal hydroxide; (b) polycondensing the product of (a), without isolation, under reduced pressure and in the presence of antimony trioxide in amount 100 to 1,000 parts per million by weight of the dicarboxylic acid originally present and triphenyl phosphate stabilizer; the improvement which comprises carrying out step (a) in the presence of a solution of germanium dioxide in an alkali metal hydroxide and a diol having its hydroxyl groups attached to adjacent carbon atoms, the amount of germanium dioxide being 10 to 200 parts per million by weight based on the amount of dicarboxylic acid present at the start of the reaction and the amount of the alkali metal hydroxide is at least one equivalent per mole of the germanium dioxide, said antimony trioxide being added to the product of (a) after completion of the esterification reaction and the amount of said alkali metal hydroxide is: (i) greater than the equivalent per mole of germanium dioxide; (ii) greater than 0.5 gram equivalents per million grams of the dicarboxylic acid; (iii) less than the greater of twice the equivalent per mole of germanium dioxide and 2.5 gram equivalents per million grams of the dicarboxylic acid.
Claim 3
Dependent Claim
22 words
A method according to claim 1, in which terephthalic acid is esterified with ethylene glycol and then polycondensed to give polyethylene terephthalate.
Claim 4
Dependent Claim
227 words
In a process for the production of polyethylene terephthalate which comprises: (a) esterifying terephthalic acid with ethylene glycol at an elevated temperature and in the presence of sodium hydroxide; (b) polycondensing the product of (a), without isolation, under reduced pressure and in the presence of antimony trioxide in amount 100 to 1,000 parts per million by weight of the terephthalic acid originally present and triphenyl phosphate stabilizer; the improvement which comprises carrying out step (a) in the presence of a solution of germanium dioxide in sodium hydroxide and ethylene glycol, the amount of germanium dioxide being 10 to 200 parts per million by weight based on the amount of terephthalic acid present at the start of the reaction and the amount of the sodium hydroxide is at least 38.2 parts by weight per 100 parts by weight of the germanium dioxide, said antimony trioxide being added to the product of (a) after completion of the esterification reaction and the amount of said sodium hydroxide is: (i) greater than 38.2 parts by weight per 100 parts by weight of germanium dioxide; (ii) greater than 20 parts by weight per million parts by weight of the terephthalic acid; (iii) less than the greater of 76.4 parts by weight per 100 parts by weight of germanium dioxide and 100 parts by weight per million parts by weight of terephthalic acid.
Claim 5
Dependent Claim
227 words
In a process for the production of polyethylene terephthalate which comprises: (a) esterifying terephthalic acid with ethylene glycol at an elevated temperature and in the presence of sodium hydroxide; (b) polycondensing the product of (a), without isolation, under reduced pressure and in the presence of antimony trioxide in amount 100 to 1,000 parts per million by weight of the terephthalic acid originally present and triphenyl phosphate stabilizer; the improvement which comprises carrying out step (a) in the presence of a solution of germanium dioxide in sodium hydroxide and ethylene glycol, the amount of germanium dioxide being 10 to 200 parts per million by weight based on the amount of terephthalic acid present at the start of the reaction and the amount of the sodium hydroxide is at least 38.2 parts by weight per 100 parts by weight of the germanium dioxide, said antimony trioxide being added to the product of (a) after completion of the esterification reaction and the amount of said sodium hydroxide is: (i) greater than 38.2 parts by weight per 100 parts by weight of germanium dioxide; (ii) greater than 20 parts by weight per million parts by weight of the terephthalic acid; (iii) less than the greater of 76.4 parts by weight per 100 parts by weight of germanium dioxide and 100 parts by weight per million parts by weight of terephthalic acid.
References Cited (Backward Citations)
GB782036A
Cited
GB1091234A
Cited
SU382275A3
Cited
US3651017A
Cited
GB1197004A
Cited
US3795639A
Cited
DE2164348A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-01-08 | 1982-07-10 | 1983-01-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-01-08 | 1986-07-10 | 1987-01-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-01-08 | 1990-07-10 | 1991-01-09 | $7700.00 | Window Closed / Lapsed |