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GB1006040A - Production of polyacrylonitrile fibres - Google Patents

Production of polyacrylonitrile fibres

Info

Publication number
GB1006040A
GB1006040A GB22174/64A GB2217464A GB1006040A GB 1006040 A GB1006040 A GB 1006040A GB 22174/64 A GB22174/64 A GB 22174/64A GB 2217464 A GB2217464 A GB 2217464A GB 1006040 A GB1006040 A GB 1006040A
Authority
GB
United Kingdom
Prior art keywords
dried
filaments
stretched
sodium thiocyanate
aqueous sodium
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
GB22174/64A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Japan Exlan Co Ltd
Original Assignee
Japan Exlan Co Ltd
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 by Japan Exlan Co Ltd filed Critical Japan Exlan Co Ltd
Publication of GB1006040A publication Critical patent/GB1006040A/en
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/18Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/28Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/38Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising unsaturated nitriles as the major constituent

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Artificial Filaments (AREA)

Abstract

1,006,040. Polyacrylonitrile filaments. JAPAN EXLAN CO. Ltd. May 28, 1964 [June 5, 1963], No. 22174/64. Heading B5B. In the wet-spinning of polyacrylonitrile filaments, the coagulated polyacrylonitrile filaments containing a proportion by weight of solvent not exceeding 1À5 times the dry weight of polymer are dried until their water content is less than 1À5 times the weight of said solvent, the dried filaments stretched in a medium which will not appreciably extract said solvent, and the stretched filaments washed and dried. Homopolymers of acrylonitrile, copolymers of acrylonitrile with other olefinic monomers, block polymers, graft polymers and mixtures of said polymers may be used. Specified monomers include vinyl acetates vinyl esters of other monocarboxylic acids, acrylic acid, acrylic esters such as methyl acrylate and ethyl acrylate; methacrylic acid, methacrylic esters such as methyl methacrylate; vinyl chloride, vinylidene chloride, styrene, methacrylonitrile, vinylidene cyanide, vinyl pyridine and its substituted derivaties, other vinyl-substituted nitrogen-containing heterocyclic compounds such as vinyl imidazole; aliphatic and aromatic sulphonic acids having an unsaturated bond such as styrene sulphonic acid, allyl sulphonic acid and methallyl sulphonic acid and monoolefinic monomers capable of copolymerizing with acrylonitrile. Pigments, anti-colouring agents, stabilizers, plasticers and other conventional additives may be added to the polymer. The spinning solvent may be an organic solvent having a boiling point higher than that of water, e.g. N,N-dimethyl formamide, N,N,-dimethylacetamide, ethylene carbonate and dimethyl sulphoxide, or a concentrated aqueous solution of an inorganic salt, e.g. sodium thiocyanate, calcium thiocyanate, sodium perchlorate, calcium perchlorate, zinc chloride or lithium chloride. Coagulating baths specified include dilute aqueous solutions of the spinning solvent or non-solvents for the polymer and coagulation may be effected at room temperature. Stretching is preferably effected in hot air and washing in water. Crimping, application of finishing agents and cutting are then carried out, and the fibres dried. In Examples: (1) an acrylonitrile/ methyl acrylate/methacryl sulphonic acid copolymer is dissolved in 46% aqueous sodium thiocyanate and spun into 12% aqueous sodium thiocyanate at 20‹ C. The coagulated filaments are immersed in 4% aqueous sodium thiocyanate, removed, dried in air at 50‹ C., stretched in hot air, washed in cold water and dried at 150‹ C. (2) Coagulated gel filaments made as in (1) are immersed in 5% aqueous sodium thiocyanate, removed, dried, stretched in hot water, washed in hot water and dried at 105‹ C. (3) An acrylonitrile/methyl acrylate copolymer is dissolved in 50% aqueous sodium thiocyanate and spun into 75% aqueous sodium thiocyanate at 15‹ C. The coagulated filaments are dried at 50‹ C., stretched in hot air at 105‹ C., washed in cold water and dried at 105‹ C. (4) Dried gel filaments made as in (2) but before being subjected to stretching are stretched while being heated between infra-red lamps, washed with water and dried at 105‹ C. In general, stretch ratios of 5À3-9À9 and stretching temperatures of 60-200‹ C. are used. Filaments so made are dense, have a smooth surface, circular cross-section and a silk-like touch and lustre.
GB22174/64A 1963-06-05 1964-05-28 Production of polyacrylonitrile fibres Expired GB1006040A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2944563 1963-06-05

Publications (1)

Publication Number Publication Date
GB1006040A true GB1006040A (en) 1965-09-29

Family

ID=12276305

Family Applications (1)

Application Number Title Priority Date Filing Date
GB22174/64A Expired GB1006040A (en) 1963-06-05 1964-05-28 Production of polyacrylonitrile fibres

Country Status (7)

Country Link
US (1) US3399260A (en)
BE (1) BE646691A (en)
DE (1) DE1494623A1 (en)
FR (1) FR1397075A (en)
GB (1) GB1006040A (en)
LU (1) LU46167A1 (en)
NL (1) NL6405582A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113758887A (en) * 2021-08-20 2021-12-07 北京化工大学 Method for screening extractants and testing residual solvent dimethyl sulfoxide in polyacrylonitrile precursors
CN116024674A (en) * 2021-10-26 2023-04-28 中国石油化工股份有限公司 Method for preparing polyacrylonitrile nascent fiber by gel spinning and nascent fiber thereof

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3485913A (en) * 1965-10-20 1969-12-23 Toho Beslon Co New method of manufacturing acrylic fibers and the related products
JPS52870A (en) * 1975-06-24 1977-01-06 Kureha Chemical Ind Co Ltd Method of prevention or recovery of whitening of formed product of acrylonitrile polymer due to absorption of water

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697023A (en) * 1950-04-29 1954-12-14 Eastman Kodak Co Spinning acrylonitrile
US2948581A (en) * 1955-12-20 1960-08-09 American Cyanamid Co Method of producing a synthetic fiber
US2984912A (en) * 1958-08-14 1961-05-23 American Cyanamid Co Art of producing filamentary polyacrylonitrile
NL245712A (en) * 1958-11-24 1900-01-01
US3052512A (en) * 1960-06-14 1962-09-04 American Cyanamid Co Art of producing polyacrylonitrile filamentary materials
US3101245A (en) * 1960-08-18 1963-08-20 American Cyanamid Co Production of polyacrylonitrile fibers
BE629770A (en) * 1962-03-19

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113758887A (en) * 2021-08-20 2021-12-07 北京化工大学 Method for screening extractants and testing residual solvent dimethyl sulfoxide in polyacrylonitrile precursors
CN113758887B (en) * 2021-08-20 2022-11-29 北京化工大学 Method for screening extracting agent and testing residual solvent dimethyl sulfoxide in polyacrylonitrile protofilament
CN116024674A (en) * 2021-10-26 2023-04-28 中国石油化工股份有限公司 Method for preparing polyacrylonitrile nascent fiber by gel spinning and nascent fiber thereof

Also Published As

Publication number Publication date
FR1397075A (en) 1965-04-23
US3399260A (en) 1968-08-27
BE646691A (en) 1964-10-19
DE1494623A1 (en) 1969-07-03
LU46167A1 (en) 1972-01-01
NL6405582A (en) 1964-12-07

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