US4077945A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for making linear polyesters from ethylene glycol and terephthalic acid
Assignee: LL Plant Engineering AG
•
Filing: 1977-04-18
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Granted: 1978-03-07
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Expires: 1997-04-18
Abstract
Abstract A batch process for esterifying ethylene glycol and terephthalic acid at elevated temperature and pressure in which a part of the ethylene glycol required for the complete esterification reaction is placed in an autoclave and heated under pressure, and the remainder of the glycol is added to said heated glycol in the form of a paste with terephthalic acid. Preferably the glycol initially present in the autoclave amounts to 0.3 to 0.8 moles per mole of terephthalic acid while the glycol added as a paste amounts to 1.4 to 0.9 moles per mole of terephthalic acid. The glycol initially in the autoclave may be glycol reclaimed from the mixture volatilized during the reaction and may contain up to 20% water, preferably 2-6% water.
Inventors
- 👤 Helmut Heinze
- 👤 Eberhard Hackel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 05:09
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/78; C08G63/02; C08G63/12; C08G63/16; C08G63/18; C08G63/181; C08G63/183
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
170 words
A process for making linear polyesters by discontinuous direct esterification of ethylene glycol and terephthalic acid at molar ratios of 1.1:1 to 2.0:1, in which at the beginning of the esterification reaction heated glycol is placed in the reaction vessel and the terephthalic acid is fed into the glycol, followed by polycondensation of the esterification product, the improvement comprising: maintaining 0.1 to 1.4 moles of the glycol required for the esterification reaction per mole of the terephthalic acid at a temperature above 200° C at superatmospheric pressure in the said reaction vessel and in the substantial absence of terephthalic acid, preparing a terephthalic acid paste containing 1.9 to 0.6 moles of ethylene glycol per mole of terephthalic acid, initiating esterification by feeding said paste to said heated glycol in the reaction vessel over a period of time and under agitation, esterifying the resulting mixture at a temperature of between 200° to 290° C and a pressure of between 1 and 15 atmospheres, and lowering the pressure as the reaction proceeds.
Claim 2
Dependent Claim
170 words
A process for making linear polyesters by discontinuous direct esterification of ethylene glycol and terephthalic acid at molar ratios of 1.1:1 to 2.0:1, in which at the beginning of the esterification reaction heated glycol is placed in the reaction vessel and the terephthalic acid is fed into the glycol, followed by polycondensation of the esterification product, the improvement comprising: maintaining 0.1 to 1.4 moles of the glycol required for the esterification reaction per mole of the terephthalic acid at a temperature above 200° C at superatmospheric pressure in the said reaction vessel and in the substantial absence of terephthalic acid, preparing a terephthalic acid paste containing 1.9 to 0.6 moles of ethylene glycol per mole of terephthalic acid, initiating esterification by feeding said paste to said heated glycol in the reaction vessel over a period of time and under agitation, esterifying the resulting mixture at a temperature of between 200° to 290° C and a pressure of between 1 and 15 atmospheres, and lowering the pressure as the reaction proceeds.
Claim 3
Dependent Claim
58 words
The process of claim 1 in which said part of the glycol amounts to 0.3 to 0.8 mole per mole of terephthalic acid, the glycol in the paste amounts to 1.4 to 0.9 moles per mole of terephthalic acid, the esterification temperature is between 240° and 270° C and the esterification pressure is between 4 and 8 atmospheres
Claim 4
Dependent Claim
18 words
The process of claim 1 in which said part of the glycol contains from 0.1 to 20% water.
Claim 5
Dependent Claim
18 words
The process of claim 3 in which said part of the glycol contains from 2 to 6% water.
Claim 6
Dependent Claim
30 words
The process of claim 1 in which, during the esterification reaction, additional glycol is fed into the reaction vessel in amounts up to 500 g/hr per Kg of terephthalic acid.
Claim 7
Dependent Claim
25 words
The process of claim 1 in which said polycondensation is carried out in the same reaction vessel to a degree of from 3 to 20.
References Cited (Backward Citations)
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US3655729A
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US3689461A
Cited
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Cited
US3892798A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-03-06 | 1981-09-05 | 1982-03-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-03-06 | 1985-09-05 | 1986-03-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-03-06 | 1989-09-05 | 1990-03-07 | $7700.00 | Window Closed / Lapsed |