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UST869015I4 - Defensive publication - Google Patents

Defensive publication Download PDF

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Publication number
UST869015I4
UST869015I4 US869015DH UST869015I4 US T869015 I4 UST869015 I4 US T869015I4 US 869015D H US869015D H US 869015DH US T869015 I4 UST869015 I4 US T869015I4
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US
United States
Prior art keywords
defensive publication
solutions
room temperature
polyester
polyesters
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
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Publication of UST869015I4 publication Critical patent/UST869015I4/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/09Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
    • C08J3/091Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
    • C08J3/093Halogenated hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16Dicarboxylic acids and dihydroxy compounds
    • C08G63/18Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
    • C08G63/199Acids or hydroxy compounds containing cycloaliphatic rings
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02Polyesters derived from dicarboxylic acids and dihydroxy compounds

Definitions

  • a process for providing room temperature-stable solutions of the high trans isomer content polyesters which process comprises dissolving the polyester in a chlorinated hydrocarbon having a boiling point of up to about 100 C. under superatmospheric pressure and at an elevated temperature sufi'icient to dissolve the polyester and then slowly cooling the resulting solution to room temperature while maintaining the solution under superatmospheric pressure.
  • chlorinated hydrocarbon solvents having boiling points falling below 100 C. is important in the acquisition of room temperature-stable solutions of the high trans content polyesters for use of other solvents in the process, although solubilizing the polyester, fails to provide room temperaturestable solutions.
  • the preferred chlorinated hydrocarbon solvents are methylene chloride, chloroform and mixtures thereof.
  • the temperature employed for dissolution of the polyester is usually in excess of 100 0., most often 150 C.
  • the pressure employed throughout the process may vary over a wide range of from about 100 pounds per square inch (p.s.i.) on up depending on the temperature, solvent, reaction vessel volume and other variable factors.
  • the maximum concentration of polyester in the chlorinated hydrocarbon which will remain dissolved at room temperature when processed in accordance with the invention is about 10% w./w. Preferably, the concentration is up to about 6% w./w.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

DEFENSIVE PUBLICATION UNITED STATES PATENT OFFICE Published at the request of the applicant or owner in accordance with the Notice of Dec. 16, 1969, 869 O.G. 687. The abstracts of Defensive Publication applications are identified by distinctly numbered series and are arranged chronologically. The heading of each abstract indicates the number of pages of specification, including claims and sheets of drawings contained in the application as originally filed. The files of these applications are available to the public for inspection and reproduction may be purchased for 30 cents a sheet.
Defensive Publication applications have not been examined as to the merits of alleged invention. The Patent Oifice makes no assertion as to the novelty of the disclosed subject matter.
PUBLISHED DECEMBER 16, 1969 869 O.G. 714i T869,015 STABLE SOLUTIONS OF POLYESTERS OF TER- EPHTHALIC ACID AND 2,2,4,4-TETRAMETHYL- 1,3 'CYCLOBUTANEDIOL (HIGH TRANS CONTENT) Max F. Meyer, Jr., Robert L. Combs, and Willis C. Wooten, Jr., all of PD. Box 511, Kingsport, Tenn.
Filed Aug. 11, 1969, Ser. No. 849,155 Int. Cl. C08g 51/30 U.S. Cl. 260--33.8 No Drawing. 10 Pages Specification Polyesters of terephthalic acid and 2,2,4,4-tetramethylcyclbutanediol having a trans isomer content of at least about 65%, not only are incapable of being processed in the melt without degradation but unlike the polyesters of cis form cannot be put eifectively into solutions which are stable at room temperature, that is, solutions which remain solutions at room temperature for a reasonable period of time. A process has been found for providing room temperature-stable solutions of the high trans isomer content polyesters which process comprises dissolving the polyester in a chlorinated hydrocarbon having a boiling point of up to about 100 C. under superatmospheric pressure and at an elevated temperature sufi'icient to dissolve the polyester and then slowly cooling the resulting solution to room temperature while maintaining the solution under superatmospheric pressure. The use of chlorinated hydrocarbon solvents having boiling points falling below 100 C. is important in the acquisition of room temperature-stable solutions of the high trans content polyesters for use of other solvents in the process, although solubilizing the polyester, fails to provide room temperaturestable solutions. The preferred chlorinated hydrocarbon solvents are methylene chloride, chloroform and mixtures thereof. The temperature employed for dissolution of the polyester is usually in excess of 100 0., most often 150 C. The pressure employed throughout the process may vary over a wide range of from about 100 pounds per square inch (p.s.i.) on up depending on the temperature, solvent, reaction vessel volume and other variable factors. The maximum concentration of polyester in the chlorinated hydrocarbon which will remain dissolved at room temperature when processed in accordance with the invention is about 10% w./w. Preferably, the concentration is up to about 6% w./w.
US869015D 1969-08-11 1969-08-11 Defensive publication Pending UST869015I4 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US84915569A 1969-08-11 1969-08-11

Publications (1)

Publication Number Publication Date
UST869015I4 true UST869015I4 (en) 1969-12-16

Family

ID=25305192

Family Applications (1)

Application Number Title Priority Date Filing Date
US869015D Pending UST869015I4 (en) 1969-08-11 1969-08-11 Defensive publication

Country Status (1)

Country Link
US (1) UST869015I4 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0745628A2 (en) * 1995-05-31 1996-12-04 Shell Internationale Researchmaatschappij B.V. Copolyester composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0745628A2 (en) * 1995-05-31 1996-12-04 Shell Internationale Researchmaatschappij B.V. Copolyester composition
EP0745628A3 (en) * 1995-05-31 1997-05-02 Shell Int Research Copolyester composition

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