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US4350805A
Expired / Lapsed
US
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Process for the preparation of poly(ester-carbonates)
Assignee: Eastman Chemical Co
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Filing: 1980-11-17
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Granted: 1982-09-21
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Expires: 2000-11-17
Abstract
Abstract Process for preparation of poly(ester-carbonates) from aromatic diol bis(alkylcarbonates) and esters of dicarboxylic, and/or carboxylate-carbonate esters of hydroxy acids by suitably heating the reactants in the presence of a suitable polymerization catalyst.
Inventors
- 👤 Winston J. Jackson, Jr.
- 👤 William R. Darnell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 14:29
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/64
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
298 words
Process for preparation of a high molecular weight poly(ester-carbonate) comprising (a) preparing a reaction mixture of (1) an aromatic diol bis(alkylcarbonate) (A) having the general formula ##STR12## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Ar is the aromatic residue remaining after removal of hydroxyl groups from an aromatic diol, (2) 0 to 47.5 mole percent of at least one ester of at least one dicarboxylic acid (B) having the general formula ##STR13## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Y is the residue remaining after removal of the carboxyl groups from an aliphatic, cycloaliphatic or aromatic dicarboxylic acid, (3) 0 to 80 mole percent of at least one mixed carboxylate-carbonate ester of at least one aromatic hydroxy acid (C) having the general formula ##STR14## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Z is the residue remaining after removal of the hydroxyl and carboxyl groups from meta- or para-oriented aromatic hydroxy carboxylic acids, and (4) a catalytic amount of an ester exchange and polymerization catalyst, wherein the molar percentages of (A)+(B)+(C)=100%, the molar percentage of (A) is at least 5 percentile units greater than the molar percentage of (B); the molar percentage of (B) or the molar percentage of (C) may be 0, but the molar percentage of (B)+ the molar percentage of (C) is at least 5% of the total reactants, (b) heating the reaction mixture to a temperature sufficient to keep the reaction mixture molten and to distill away dialkyl carbonate condensation by-product, and (c) reducing pressure for a time sufficient to further remove dialkyl carbonate condensation product and to increase the molecular weight of the polymer.
Claim 2
Dependent Claim
298 words
Process for preparation of a high molecular weight poly(ester-carbonate) comprising (a) preparing a reaction mixture of (1) an aromatic diol bis(alkylcarbonate) (A) having the general formula ##STR12## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Ar is the aromatic residue remaining after removal of hydroxyl groups from an aromatic diol, (2) 0 to 47.5 mole percent of at least one ester of at least one dicarboxylic acid (B) having the general formula ##STR13## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Y is the residue remaining after removal of the carboxyl groups from an aliphatic, cycloaliphatic or aromatic dicarboxylic acid, (3) 0 to 80 mole percent of at least one mixed carboxylate-carbonate ester of at least one aromatic hydroxy acid (C) having the general formula ##STR14## wherein R is the same or different and selected from alkyl groups containing 1-8 carbon atoms and Z is the residue remaining after removal of the hydroxyl and carboxyl groups from meta- or para-oriented aromatic hydroxy carboxylic acids, and (4) a catalytic amount of an ester exchange and polymerization catalyst, wherein the molar percentages of (A)+(B)+(C)=100%, the molar percentage of (A) is at least 5 percentile units greater than the molar percentage of (B); the molar percentage of (B) or the molar percentage of (C) may be 0, but the molar percentage of (B)+ the molar percentage of (C) is at least 5% of the total reactants, (b) heating the reaction mixture to a temperature sufficient to keep the reaction mixture molten and to distill away dialkyl carbonate condensation by-product, and (c) reducing pressure for a time sufficient to further remove dialkyl carbonate condensation product and to increase the molecular weight of the polymer.
Claim 3
Dependent Claim
27 words
Process of claim 1 wherein said catalyst is selected from compounds of titanium, tin, lead, or alkaline earth compounds used in combination with antimony or germanium compounds.
Claim 4
Dependent Claim
11 words
Process of claim 2 wherein said catalyst is a titanium compound.
Claim 5
Dependent Claim
27 words
Process of claim 3 wherein said catalyst is tetraisopropyltitanate and the catalyst concentration is about 50 to 250 parts per million metal based on theoretical polymer yield.
Claim 6
Dependent Claim
39 words
Process of claim 1 wherein a prepolymer is prepared, comminuted, crystallized and further polymerized in the solid state at a temperature of about 265° C. or more but at least 10° C. below the melting point of the polymer.
References Cited (Backward Citations)
US3335111A
Cited
DE2435507A1
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-09-20 | 1986-03-22 | 1986-09-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-09-20 | 1990-03-22 | 1990-09-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-09-20 | 1994-03-22 | 1994-09-21 | $7700.00 | Window Closed / Lapsed |