US4194038A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Poly(ester-carbonates) from dicarboxylic acid chlorides
Assignee: Honeywell International Inc
•
Filing: 1979-01-25
•
Granted: 1980-03-18
•
Expires: 1999-01-25
Abstract
Abstract A process for poly(ester-carbonates) from dihydric phenols, especially bisphenol A; aromatic or cycloaliphatic dicarboxylic acids, especially terephthalic acid; and phosgene as carbonate precursor wherein a reaction of the acid and phosgene is carried out in a first stage forming dicarboxylic acid chloride; and then phosgene and bisphenol A are added in separate streams, simultaneously during most of the second or condensation stage. Thereby only one kettle is required for carrying out the complete polymer production.
Inventors
- 👤 Josefina T. Baker
- 👤 Robert S. Cooke
- 👤 Stylianos Sifniades
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 17:05
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/64
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
290 words
In a process for production of poly(ester-carbonate) of dihydric phenol and of aromatic or cycloaliphatic dicarboxylic acid from a reaction mixture containing dichloride of at least one such acid, dissolved in a chlorinated hydrocarbon solvent inert under the reaction conditions having from 1 to 6 carbon atoms and from 1 to 4 chlorine atoms, said process employing a tertiary nitrogen base, having pK b in aqueous solution at 25° C. in the range 7-11, to catalyze condensation of such dihydric phenol with said dichloride and with phosgene employed as carbonate precursor, and to serve as HCl acceptor for the HCl generated in said condensation reactions; the improvement which comprises: (1) Feeding at least one such dihydric phenol into said dichloride solution at temperature in the range 0°-100° C., said dichloride solution containing at the start of said condensation reaction, phosgene in the range between 10% and 50% of the stoichiometric proportion of phosgene: total dihydric phenol required for formation of the poly(ester-carbonate) final product with the desired mol ratio in the range 1.00:0.05 up to 1.00:0.70 of dihydric phenol:dichloride residues; (2) Concurrently with the feeding of dihydric phenol, agitating the reaction mixture and feeding phosgene in a separate stream thereto, until all dihydric phenol for the reaction has been added and at least 80% but not over 97% of the stoichiometrically required phosgene for reaction with all hydroxyl groups has been added; (3) Maintaining during the feeding of dihydric phenol, at least a 10% molar excess of tertiary nitrogen base over that required by stoichiometry; (4) Then allowing time for the condensation reaction forming poly(ester-carbonate) to come essentially to completion while the phosgene added is being brought at least to the stoichiometrically required quantity for reaction with all hydroxyl groups.
Claim 2
Dependent Claim
290 words
In a process for production of poly(ester-carbonate) of dihydric phenol and of aromatic or cycloaliphatic dicarboxylic acid from a reaction mixture containing dichloride of at least one such acid, dissolved in a chlorinated hydrocarbon solvent inert under the reaction conditions having from 1 to 6 carbon atoms and from 1 to 4 chlorine atoms, said process employing a tertiary nitrogen base, having pK b in aqueous solution at 25° C. in the range 7-11, to catalyze condensation of such dihydric phenol with said dichloride and with phosgene employed as carbonate precursor, and to serve as HCl acceptor for the HCl generated in said condensation reactions; the improvement which comprises: (1) Feeding at least one such dihydric phenol into said dichloride solution at temperature in the range 0°-100° C., said dichloride solution containing at the start of said condensation reaction, phosgene in the range between 10% and 50% of the stoichiometric proportion of phosgene: total dihydric phenol required for formation of the poly(ester-carbonate) final product with the desired mol ratio in the range 1.00:0.05 up to 1.00:0.70 of dihydric phenol:dichloride residues; (2) Concurrently with the feeding of dihydric phenol, agitating the reaction mixture and feeding phosgene in a separate stream thereto, until all dihydric phenol for the reaction has been added and at least 80% but not over 97% of the stoichiometrically required phosgene for reaction with all hydroxyl groups has been added; (3) Maintaining during the feeding of dihydric phenol, at least a 10% molar excess of tertiary nitrogen base over that required by stoichiometry; (4) Then allowing time for the condensation reaction forming poly(ester-carbonate) to come essentially to completion while the phosgene added is being brought at least to the stoichiometrically required quantity for reaction with all hydroxyl groups.
Claim 3
Dependent Claim
45 words
In the process of claim 1: employing, as the principal dihydric phenol, bisphenol A, and as the principal dicarboxylic acid, terephthalic acid; and employing as tertiary nitrogen base, one having pK b in aqueous solution at 25° C. in the range between 7 and 9.
Claim 4
Dependent Claim
139 words
In the process of claim 2: employing dichloromethane as the inert solvent and pyridine as the tertiary nitrogen base; providing in the terephthaloyl chloride solution at the start of the condensation reaction between phenolic hydroxyl groups and phosgene, a quantity of phosgene in the range between 20% and 40% of the stoichiometric proportion of phosgene:total bisphenol A required for formation of the poly(ester-carbonate) final product having mol ratio of bisphenol A:terephthalate:carbonate residues of 1.0:0.5:0.5; feeding bisphenol A to the terephthaloyl chloride solution in total molar proportion of about 1:0.5 of bisphenol A:terephthaloyl chloride and feeding phosgene thereto in at least the stoichiometric quantity to produce said final product; maintaining temperatures between 15° and 50° C. and maintaining an excess of base in the reaction mixture of at least 30% over that required to react with hydrogen chloride being formed.
Claim 5
Dependent Claim
22 words
In the process of claim 1: employing as the principal dihydric phenol, bisphenol A and as the principal dicarboxylic acid, isophthalic acid.
Claim 6
Dependent Claim
22 words
In the process of claim 1: employing as the principal dihydric phenol, bisphenol A and as the principal dicarboxylic acid, cyclohexane-1,4-dicarboxylic acid.
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) | 1983-03-18 | 1983-09-17 | 1984-03-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-03-18 | 1987-09-17 | 1988-03-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-03-18 | 1991-09-17 | 1992-03-18 | $7700.00 | Window Closed / Lapsed |