GB614625A - Improvements in the production of condensation polymers - Google Patents

Improvements in the production of condensation polymers

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Publication number
GB614625A
GB614625A GB1272744A GB1272744A GB614625A GB 614625 A GB614625 A GB 614625A GB 1272744 A GB1272744 A GB 1272744A GB 1272744 A GB1272744 A GB 1272744A GB 614625 A GB614625 A GB 614625A
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GB
United Kingdom
Prior art keywords
mass
reaction mass
heating
heated
infra
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.)
Expired
Application number
GB1272744A
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Individual
Original Assignee
Individual
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Publication date
Application filed by Individual filed Critical Individual
Priority to GB1272744A priority Critical patent/GB614625A/en
Publication of GB614625A publication Critical patent/GB614625A/en
Expired legal-status Critical Current

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Classifications

    • 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
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/04Preparatory processes
    • 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
    • C08G63/78Preparation processes
    • C08G63/785Preparation processes characterised by the apparatus used

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyamides (AREA)

Abstract

<PICT:0614625/III/1> Linear condensation polymers are produced by heating a polymer-forming reaction mass by infra-red radiation while the mass is in the form of a thin layer, preferably of a thickness less than 0.025 in. The mass is heated and allowed to cool in an inert atmosphere, for example nitrogen or hydrogen. Polyamides, e.g. polyhexamethylene adipamide, polyesters and nitrogen-containing polymers may be prepared (see Group IV (a)). The reaction mass may be in the form of a fine powder or brought to a liquid or semi-liquid condition by adding a solvent or non-solvent, e.g. phenol, cresols, or xylenols. To assist in p uniform heating, the support for the mass may be vibrated, and its surface may be blackened. In the apparatus shown, the reaction mass is fed from a hopper 23 on to a travelling band 21 in a chamber 20, and formed into a thin layer by an adjustable blade 31. Heating is effected by infra-red lamps 33, and the surface behind the lamps may be coated with a reflecting material, e.g. gold or aluminium; gas-heated refractory materials may also be used for the heating. The temperature of the reaction mass is raised to 200-300 DEG C., preferably 220-270 DEG C., the product cooled while passing through the left-hand part of the chamber 20, and removed from the band by a blade 34; inert gas is introduced at 36 and leaves at 37. The process may also be carried out in an apparatus (Figs. 1 and 2, not shown) comprising tiers of chambers in which shallow trays containing the reaction mass are supported on rollers.ALSO:Linear condensation polymers are produced by heating a polymer-forming reaction mass by infra-red radiation, while the mass is in the form of a thin layer, preferably of a thickness less than 0.025 in. The mass is heated and allowed to cool in an inert atmosphere, for example nitrogen or hydrogen. Polyamides may be prepared according to Specifications 601,123, 610,304 and 610,311; from aminocaproic acid or higher homologues of this acid; or from dicarboxylic acids (or their esters and amides) and diamines. Suitable acids are adipic, suberic, sebacic, brassylic, paraphenylene di-acetic and terephthalic acids; suitable amines are tetramethylene, pentamethylene, hexamethylene, and decamethylene diamines; paraxylylene and metaphenylene diamines; and piperazine. Polyesters may be prepared from dihydroxy compounds (e.g. tetramethylene and hexamethylene glycols) and the dicarboxylic acids listed above; or from hydroxycarboxylic acids. Nitrogen-containing polymers may be prepared according to Specifications 612,609 and 613,020. The reaction mass may be in the form of a fine powder or brought to a liquid or semi-liquid condition by adding a solvent or non-solvent, e.g. phenol, cresols, or xylenols. In the production of polyhexamethylene adipamide from hexamethylene di-ammonium adipate mixed with xylenol, the reaction product is purified by dissolving in formic acid and pouring into acetone. The reaction mass is heated by infra-red lamps or gas-heated refractory material to the required temperature (e.g. 200 DEG -300 DEG C., and preferably 220 DEG -270 DEG C.) on shallow trays in a chamber, or spread on a travelling band which passes through the chamber (see Groups III and XI).
GB1272744A 1944-07-04 1944-07-04 Improvements in the production of condensation polymers Expired GB614625A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1272744A GB614625A (en) 1944-07-04 1944-07-04 Improvements in the production of condensation polymers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1272744A GB614625A (en) 1944-07-04 1944-07-04 Improvements in the production of condensation polymers

Publications (1)

Publication Number Publication Date
GB614625A true GB614625A (en) 1948-12-20

Family

ID=10009981

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1272744A Expired GB614625A (en) 1944-07-04 1944-07-04 Improvements in the production of condensation polymers

Country Status (1)

Country Link
GB (1) GB614625A (en)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2913433A (en) * 1955-12-28 1959-11-17 Du Pont Polyamides from hydrocarbon substituted piperazines and carboxyclic dicarboxylic acid
US2918454A (en) * 1954-08-16 1959-12-22 Ethyl Corp Condensation polymers
US2987507A (en) * 1957-11-26 1961-06-06 California Research Corp Preparation of nylon polymers
US3006899A (en) * 1957-02-28 1961-10-31 Du Pont Polyamides from reaction of aromatic diacid halide dissolved in cyclic nonaromatic oxygenated organic solvent and an aromatic diamine
US3061592A (en) * 1958-02-01 1962-10-30 Bayer Ag Process for the production of polyamides from cyclic lactams in pearly form
US3079219A (en) * 1960-12-06 1963-02-26 Du Pont Process for wet spinning aromatic polyamides
US3094511A (en) * 1958-11-17 1963-06-18 Du Pont Wholly aromatic polyamides
US3109835A (en) * 1958-10-08 1963-11-05 Allied Chem Process for producing ultrahigh viscosity polycaprolactam
US3130180A (en) * 1957-09-18 1964-04-21 Glanzstoff Ag Continuous method and apparatus for the production of polyhexamethylene adipamide
US3133138A (en) * 1958-12-19 1964-05-12 Du Pont Stretching and heat crystallization of poly(meta-phenylene isophthalamide) fibers
US3218297A (en) * 1960-07-01 1965-11-16 Monsanto Co Continuous process for the polymerization of aqueous solutions of hexa-methylene ammonium adipate using frusto-conical annular films of same
US3232909A (en) * 1960-10-20 1966-02-01 Celanese Corp Solid state polymerization of polyamideforming reactants under autogenous pressure
US3260703A (en) * 1964-09-08 1966-07-12 Monsanto Co Condensation polymer finishing process
US3287323A (en) * 1963-04-25 1966-11-22 Du Pont Process for the production of a highly orientable, crystallizable, filamentforming polyamide
US3296217A (en) * 1964-06-01 1967-01-03 Monsanto Co Continuous polymerization process for polyamide preparation
US3322728A (en) * 1963-06-17 1967-05-30 Du Pont Sulfonyl aromatic polyamides
US3342782A (en) * 1967-01-30 1967-09-19 Eastman Kodak Co Polyester prepolymers and processes for their manufacture
US3349062A (en) * 1966-07-21 1967-10-24 Du Pont Halogenated aromatic polyamides
US3379695A (en) * 1963-12-17 1968-04-23 Chemische Werke Witten Gmbh Process for the preparation of polyamides in finely grained form
US3535285A (en) * 1967-02-28 1970-10-20 Hoechst Ag After-condensation of polycondensation polymers in an electrical high frequency field
US4408036A (en) * 1980-03-26 1983-10-04 Stamicarbon Bv Preparation of polytetramethylene adipamide
US4446304A (en) * 1980-03-26 1984-05-01 Stamicarbon B.V. Highly stable nylon 4,6 objects
US4460762A (en) * 1980-03-26 1984-07-17 Stamicarbon B.V. Preparation of high molecular polytetramethylene adipamide
US4546171A (en) * 1981-11-26 1985-10-08 Toray Industries, Inc. Method for continuous polycondensation of higher aliphatic ω-amino acid particles
US4755590A (en) * 1985-11-11 1988-07-05 Ceskoslovenska Akademie Ved Method for postpolymerization of polyamide granules after polymerization in melt and an equipment for performing this method

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2918454A (en) * 1954-08-16 1959-12-22 Ethyl Corp Condensation polymers
US2913433A (en) * 1955-12-28 1959-11-17 Du Pont Polyamides from hydrocarbon substituted piperazines and carboxyclic dicarboxylic acid
US3006899A (en) * 1957-02-28 1961-10-31 Du Pont Polyamides from reaction of aromatic diacid halide dissolved in cyclic nonaromatic oxygenated organic solvent and an aromatic diamine
US3130180A (en) * 1957-09-18 1964-04-21 Glanzstoff Ag Continuous method and apparatus for the production of polyhexamethylene adipamide
US2987507A (en) * 1957-11-26 1961-06-06 California Research Corp Preparation of nylon polymers
US3061592A (en) * 1958-02-01 1962-10-30 Bayer Ag Process for the production of polyamides from cyclic lactams in pearly form
US3109835A (en) * 1958-10-08 1963-11-05 Allied Chem Process for producing ultrahigh viscosity polycaprolactam
US3094511A (en) * 1958-11-17 1963-06-18 Du Pont Wholly aromatic polyamides
US3133138A (en) * 1958-12-19 1964-05-12 Du Pont Stretching and heat crystallization of poly(meta-phenylene isophthalamide) fibers
US3218297A (en) * 1960-07-01 1965-11-16 Monsanto Co Continuous process for the polymerization of aqueous solutions of hexa-methylene ammonium adipate using frusto-conical annular films of same
US3232909A (en) * 1960-10-20 1966-02-01 Celanese Corp Solid state polymerization of polyamideforming reactants under autogenous pressure
US3079219A (en) * 1960-12-06 1963-02-26 Du Pont Process for wet spinning aromatic polyamides
US3287323A (en) * 1963-04-25 1966-11-22 Du Pont Process for the production of a highly orientable, crystallizable, filamentforming polyamide
US3322728A (en) * 1963-06-17 1967-05-30 Du Pont Sulfonyl aromatic polyamides
US3379695A (en) * 1963-12-17 1968-04-23 Chemische Werke Witten Gmbh Process for the preparation of polyamides in finely grained form
US3296217A (en) * 1964-06-01 1967-01-03 Monsanto Co Continuous polymerization process for polyamide preparation
US3260703A (en) * 1964-09-08 1966-07-12 Monsanto Co Condensation polymer finishing process
US3349062A (en) * 1966-07-21 1967-10-24 Du Pont Halogenated aromatic polyamides
US3342782A (en) * 1967-01-30 1967-09-19 Eastman Kodak Co Polyester prepolymers and processes for their manufacture
US3535285A (en) * 1967-02-28 1970-10-20 Hoechst Ag After-condensation of polycondensation polymers in an electrical high frequency field
US4408036A (en) * 1980-03-26 1983-10-04 Stamicarbon Bv Preparation of polytetramethylene adipamide
US4446304A (en) * 1980-03-26 1984-05-01 Stamicarbon B.V. Highly stable nylon 4,6 objects
US4460762A (en) * 1980-03-26 1984-07-17 Stamicarbon B.V. Preparation of high molecular polytetramethylene adipamide
US4546171A (en) * 1981-11-26 1985-10-08 Toray Industries, Inc. Method for continuous polycondensation of higher aliphatic ω-amino acid particles
US4755590A (en) * 1985-11-11 1988-07-05 Ceskoslovenska Akademie Ved Method for postpolymerization of polyamide granules after polymerization in melt and an equipment for performing this method

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