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US4126592A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of polyesters having stabilized melt viscosity in the presence of aromatic poly(carbonates)

Assignee: General Electric Co
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Filing: 1976-12-16
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Granted: 1978-11-21
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Expires: 1996-12-16
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Abstract

Abstract The melt viscosity of high molecular weight linear polyesters is stabilized in the presence of aromatic (poly-)carbonates by adding a minor proportion of a non-volatile monofunctional ester-forming compound to a mixture of glycol and terephthalate or isophthalate reactants and heating the resulting mixture. The products of the process are suitable for conversion to compositions with aromatic (poly-)carbonates, especially flame retarded such compositions, where stabilized melt viscosity during fabrication is critical.

Inventors

  • 👤 Willem F. H. Borman
  • 👤 Frank N. Liberti

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 15:44
CPC Classifications
C; C08; C08L; C08L67/00; C08L67/08; C08G; C08G63/00; C08G63/02; C08G63/12; C08G63/16; C08G63/20; C08G63/46; C08K; C08K3/00; C08K3/18; C08K3/20; C08K3/22; C08K5/00; C08L69/00; Y; Y10; Y10S; Y10S260/00; Y10S260/24

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 152 words
A process for producing a high molecular weight linear thermoplastic polyester resin which is melt viscosity-stabilized in the presence of an aromatic carbonate or (poly-)carbonate, said polyester resin being selected from the group consisting of polymeric glycol terephthalate and isophthalate esters having repeating units of the general formula: ##STR4## wherein n is a whole number of from 2 to 10, mixtures of such esters, said process comprising (i) adding a small, effective amount of a relatively non-volatile monofunctional ester-forming compound to an esterification mixture comprising the corresponding glycol and terephthalic or isophthalic acid or a reactive derivative thereof and heating the mixture under polyesterification conditions until formation of said melt viscosity stabilized polyester is substantially complete, and (ii) intimately blending the melt viscosity stabilized polyester resin with a flame retardant amount of a flame retardant additive comprising an aromatic (poly-) carbonate to produce a flame retarded polyester composition with stable melt viscosity.
Claim 2
Dependent Claim 152 words
A process for producing a high molecular weight linear thermoplastic polyester resin which is melt viscosity-stabilized in the presence of an aromatic carbonate or (poly-)carbonate, said polyester resin being selected from the group consisting of polymeric glycol terephthalate and isophthalate esters having repeating units of the general formula: ##STR4## wherein n is a whole number of from 2 to 10, mixtures of such esters, said process comprising (i) adding a small, effective amount of a relatively non-volatile monofunctional ester-forming compound to an esterification mixture comprising the corresponding glycol and terephthalic or isophthalic acid or a reactive derivative thereof and heating the mixture under polyesterification conditions until formation of said melt viscosity stabilized polyester is substantially complete, and (ii) intimately blending the melt viscosity stabilized polyester resin with a flame retardant amount of a flame retardant additive comprising an aromatic (poly-) carbonate to produce a flame retarded polyester composition with stable melt viscosity.
Claim 3
Dependent Claim 13 words
A process as defined in claim 1 wherein said polyester is poly(1,4-butylene terephthalate).
Claim 4
Dependent Claim 20 words
A process as defined in claim 1 wherein said non-volatile monofunctional ester-forming organic compound contains only carbon, hydrogen, and oxygen.
Claim 5
Dependent Claim 27 words
A process as defined in claim 3 wherein the monofunctional ester-forming groups in said organic compound is a carboxyl group, a carboalkoxyl group or a hydroxyl group.
Claim 6
Dependent Claim 14 words
A process as defined in claim 4 wherein said organic compound is stearic acid.
Claim 7
Dependent Claim 14 words
A process as defined in claim 4 wherein said organic compound is oleic acid.
Claim 8
Dependent Claim 17 words
A process defined in claim 4 wherein said organic compound is methyl ester of hydrogenated wood rosin.
Claim 9
Dependent Claim 22 words
A process as defined in claim 4 wherein said organic compound is a partially hydrogenated alcohol prepared by reduction of wood rosin.
Claim 10
Dependent Claim 17 words
A process as defined in claim 4 wherein said organic compound is a fully hydrogenated wood rosin.
Claim 11
Dependent Claim 35 words
A process as defined in claim 1 wherein said monofunctional ester-forming organic compound is present in an amount of from about 0.1 to about 15% by weight based on the total weight of said mixture.
Claim 12
Dependent Claim 35 words
A process as defined in claim 10 wherein said monofunctional ester-forming organic compound is present in an amount of from about 0.5 to about 12% by weight based on the total weight of said mixture.
Claim 13
Dependent Claim 195 words
A process for producing a high molecular weight linear polyester resin which is melt viscosity-stabilized in the presence of an aromatic carbonate or (poly-) carbonate, said polyester resin being selected from the group consisting of polymeric glycol terephthalate and isophthalate esters having repeating units of the general formula: ##STR5## wherein n is a whole number of from 2 to 10, and mixtures of such esters, said process comprising (i) adding from 0.1 to 15% by weight of relatively non-volatile monofunctional ester-forming compound selected from among oleic acid, methyl oleate, stearic acid, methyl stearate, palmitic acid, methyl palmitate, octadecyl alcohol, hexadecyl alcohol, a methyl ester of hydrogenated wood rosin, a partially hydrogenated alcohol obtained by reduction of wood rosin and a fully hydrogenated wood rosin to an esterification mixture comprising the corresponding glycol and terephthalic or isophthalic acid or a reactive derivative thereof and heating the mixture under polyesterification conditions until formation of said melt viscosity stabilized polyester is substantially complete, and (ii) intimately blending melt viscosity stabilized polyester resin with a flame retardant amount of a flame retardant additive comprising an aromatic (poly-) carbonate to produce a flame retarded polyester composition with stable melt viscosity.
Claim 14
Dependent Claim 195 words
A process for producing a high molecular weight linear polyester resin which is melt viscosity-stabilized in the presence of an aromatic carbonate or (poly-) carbonate, said polyester resin being selected from the group consisting of polymeric glycol terephthalate and isophthalate esters having repeating units of the general formula: ##STR5## wherein n is a whole number of from 2 to 10, and mixtures of such esters, said process comprising (i) adding from 0.1 to 15% by weight of relatively non-volatile monofunctional ester-forming compound selected from among oleic acid, methyl oleate, stearic acid, methyl stearate, palmitic acid, methyl palmitate, octadecyl alcohol, hexadecyl alcohol, a methyl ester of hydrogenated wood rosin, a partially hydrogenated alcohol obtained by reduction of wood rosin and a fully hydrogenated wood rosin to an esterification mixture comprising the corresponding glycol and terephthalic or isophthalic acid or a reactive derivative thereof and heating the mixture under polyesterification conditions until formation of said melt viscosity stabilized polyester is substantially complete, and (ii) intimately blending melt viscosity stabilized polyester resin with a flame retardant amount of a flame retardant additive comprising an aromatic (poly-) carbonate to produce a flame retarded polyester composition with stable melt viscosity.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-11-20 1982-05-22 1982-11-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-11-20 1986-05-22 1986-11-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-11-20 1990-05-22 1990-11-21 $7700.00 Window Closed / Lapsed

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