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US4055534A Expired / Lapsed US ⏱️ 0.0 years remaining

Upgraded aromatic polyester material in powder form

Assignee: Horizons Inc
•
Filing: 1975-11-14
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Granted: 1977-10-25
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Expires: 1995-11-14
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Abstract

Abstract A process for upgrading polyesters derived from aromatic dicarboxylic acids which comprises reaction of the polyester material (both virgin and scrap) in an aprotic polar solvent with any of the following: A. diisocyanates represented by the general formula R(NCO) 2 with difunctional reagents in which the functionality is selected from --OH, --NH and/or --COOH; and, B. isocyanate terminated polymers alone or with the above difunctional reagents. The invention also includes stabilization of the products obtained from the above, with organic phosphites. The polyester products, whether or not stabilized, are found to be upgraded with respect to both molecular weight and processability as compared with the starting material and are readily recoverable in powder form which is most desirable for subsequent use.

Inventors

  • 👤 Arthur H. Gerber

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 22:59
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/42; C08G18/4205; C08G18/08; C08G18/0838; C08G18/0842; C08G18/0847; C08G18/0852; C08G18/10; C08G18/4009

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 229 words
A process for preparing a polyester in powder form by upgrading the molecular weight of an aromatic polyester or a mixture of aromatic polyesters with an initial molecular weight of about 10,000 to a product possessing a relative viscosity of at least 1.8 as measured in m-cresol at 31° C. which comprises: reacting said polyester with at least one reagent selected from the group consisting of (1) diisocyanates represented by the formula R(NCO) 2 and at least one difunctional compound in which the functionality is selected from the group consisting of --OH, --NH, --COOH and mixtures thereof; and (2) the reaction products of said diisocyanate and said difunctional compound alone or with at least one other difunctional compound; effecting said reaction in a polar aprotic solvent at temperatures of 100°-180° C., the relative proportions of the reactants being such that the total number of equivalents of isocyanate groups is substantially equal to the total number of equivalents of --OH, --NH, and/or --COOH reactive sites present in the polyester and difunctional compounds, the difunctional compound being present in the amount of 1 to 50 percent by weight based on the weight of said polyester, and R represents a divalent number selected from the group consisting of alkylene, cycloalkylene, alkenylene, cycloalkenylene, arylalkylene, arylene, biarylene, and all the R groups are not required to be the same and thereafter removing said solvent.
Claim 2
Dependent Claim 229 words
A process for preparing a polyester in powder form by upgrading the molecular weight of an aromatic polyester or a mixture of aromatic polyesters with an initial molecular weight of about 10,000 to a product possessing a relative viscosity of at least 1.8 as measured in m-cresol at 31° C. which comprises: reacting said polyester with at least one reagent selected from the group consisting of (1) diisocyanates represented by the formula R(NCO) 2 and at least one difunctional compound in which the functionality is selected from the group consisting of --OH, --NH, --COOH and mixtures thereof; and (2) the reaction products of said diisocyanate and said difunctional compound alone or with at least one other difunctional compound; effecting said reaction in a polar aprotic solvent at temperatures of 100°-180° C., the relative proportions of the reactants being such that the total number of equivalents of isocyanate groups is substantially equal to the total number of equivalents of --OH, --NH, and/or --COOH reactive sites present in the polyester and difunctional compounds, the difunctional compound being present in the amount of 1 to 50 percent by weight based on the weight of said polyester, and R represents a divalent number selected from the group consisting of alkylene, cycloalkylene, alkenylene, cycloalkenylene, arylalkylene, arylene, biarylene, and all the R groups are not required to be the same and thereafter removing said solvent.
Claim 3
Dependent Claim 30 words
The process of claim 1 wherein the polar aprotic solvent is selected from the group consisting of sulfolane, 3-methyl sulfolane, N-methylpyrrolidone, nitrobenzene, nitrotoluene, dimethyl sulfoxide, trimethylene sulfone, and mixtures thereof.
Claim 4
Dependent Claim 10 words
The process of claim 2 wherein the solvent is sulfolane.
Claim 5
Dependent Claim 10 words
The process of claim 2 wherein the solvent is N-methylpyrrolidinone.
Claim 6
Dependent Claim 24 words
The process of claim 1 wherein the diisocyanate and the difunctional compound are reacted with one another, prior to reaction with the polyester resin.
Claim 7
Dependent Claim 21 words
The process of claim 1 in which the diisocyanate is added to a solution of said polyester and said difunctional compound.
Claim 8
Dependent Claim 31 words
The process of claim 6 which includes in addition heating the solution of polyester and difunctional compound at 100°-180° C for a period of 0.5-10 hours prior to addition of diisocyanate.
Claim 9
Dependent Claim 10 words
Upgraded polyester polymers produced by the process of claim 1.
Claim 10
Dependent Claim 21 words
The polymers of claim 8 wherein the polyester to be upgraded has been prepared from terephthalic acid or an ester thereof.
Claim 11
Dependent Claim 14 words
The polymers of claim 9 wherein the polyester to be upgraded is poly(ethylene terephthalate).
Claim 12
Dependent Claim 15 words
The polymers of claim 9 in which the polyester to be upgraded is poly(butylene terephthalate).
Claim 13
Dependent Claim 16 words
Upgraded polymers produced by the process of claim 1 in which the diisocyanate is 4,4'-dicyclohexylmethane diisocyanate.
Claim 14
Dependent Claim 36 words
Upgraded polymers produced by the process of claim 1 in which the difunctional reagent is a hydroxyl terminated polyester of molecular weight 500 to 6000 and comprises 5 to 25 percent by weight on polyester resin.
Claim 15
Dependent Claim 50 words
Upgraded polymers produced by the process of claim 1 in which the difunctional reagent is selected from a hydroxyl or carboxy terminated polymer derived from butadiene, acrylonitrile, styrene or mixtures thereof and has a molecular weight 500 to 6000 and comprises 5 to 25 percent by weight on polyester resin.
Claim 16
Dependent Claim 24 words
The upgraded polymers produced by the process of claim 1 and which have been stabilized with 0.5 to 5 percent of an organic phosphite.
Claim 17
Dependent Claim 35 words
Upgraded polymers produced by the process of claim 1 in which the difunctional reagent is a hydroxyl terminated polyether of molecular weight 500 to 6000 and comprises 5 to 25% by weight on polyester resin.

References Cited (Backward Citations)

US2981712A Cited
US3142650A Cited
US3377308A Cited
US3344121A Cited
US3386942A Cited
US3642703A Cited
US3573251A Cited
US3668173A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-10-24 1981-04-25 1981-10-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-10-24 1985-04-25 1985-10-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-10-24 1989-04-25 1989-10-25 $7700.00 Window Closed / Lapsed

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