GB737222A - Improvements in the production of filamentary materials of acrylonitrile polymers - Google Patents

Improvements in the production of filamentary materials of acrylonitrile polymers

Info

Publication number
GB737222A
GB737222A GB15728/53A GB1572853A GB737222A GB 737222 A GB737222 A GB 737222A GB 15728/53 A GB15728/53 A GB 15728/53A GB 1572853 A GB1572853 A GB 1572853A GB 737222 A GB737222 A GB 737222A
Authority
GB
United Kingdom
Prior art keywords
solvent
filaments
yarn
air
polymer
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
GB15728/53A
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.)
Celanese Corp
Original Assignee
Celanese Corp
Celanese Corp of America
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 Celanese Corp, Celanese Corp of America filed Critical Celanese Corp
Publication of GB737222A publication Critical patent/GB737222A/en
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
    • D02J1/222Stretching in a gaseous atmosphere or in a fluid bed
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/04Dry spinning methods
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/28Stretching filaments in gas or steam

Abstract

A solution of polyacrylonitrile or of an acrylonitrile copolymer containing at least 85 per cent of acrylonitrile is extruded into an evaporative medium to form one or more filaments; the filaments are caused to travel in contact with the evaporative medium until their solvent content has fallen to 20-40 per cent; the surfaces of the filaments are thoroughly wetted with a liquid which is a non-solvent for the polymer but is miscible with the solvent, and the residual solvent is removed while preventing any substantial lengthwise shrinkage of the filaments. The non-solvent which is applied to the filaments may be water, and it may contain a <PICT:0737222/IV (a)/1> <PICT:0737222/IV (a)/2> anti-static agent or textile lubricant. Hot water may be used to remove residual solvent from the filaments. The solvent-free filaments may be stretched to increase their tenacity, and afterwards they may be relaxed by heating them, e.g. by means of hot air, while allowing them to shrink, so as to improve their elongation at break. The solvent for the polymer may be N,N - dimethyl - formamide, gamma - butyrolactone, N-formyl-pyrrolidone, dimethyl sulphone, sulpholane, fumaronitrile or cyclic ethylene carbonate. The concentration of the polymer in the solution is preferably between 10 and 30 per cent. The heated solution may be forced through a bed of sand or other finely-divided material just before it reaches the spinning jet. This not only filters the solution but serves to disperse and homogenize solvent-polymer gel particles which might otherwise cause uneven or broken filaments. The liquid with which the filaments are wetted may be water containing an anti-static agent such as an inorganic salt or amine salt of a higher fatty alcohol sulphate or phosphate, or a salt of a quaternary ammonium compound, or a polyethylene glycol, or it may be water containing a textile lubricant such as a mineral oil, a higher fatty alcohol, olive oil, oxidized pea-nut oil or an alkylated phenol such as di-t.-amyl phenol. The stretching of the washed filaments or yarns may be effected by passing them under tension through super-heated steam at a temperature above 140 DEG C. and preferably below, but no more than 30 DEG C. below, the tacky point of the polymer. Stretching may be effected in one or more stages. The subsequent relaxation treatment may be effected by heating skeins of the stretched yarn for a few minutes in air at 140 DEG C., or by passing the yarn through a chamber in which a temperature of 140-250 DEG C. is maintained. As shown in Fig. 1, a solution of acrylonitrile polymer is extruded through the jet 8 into a spinning cell 3. Air from a blower 13 is passed through a heater 14 and then through inlet pipes 11, 12 into the cell. After passing down the cell, the air with evaporated solvent is removed through outlet 15. The extrusion speed, air speed and temperature are adjusted so that the filaments 24 still contain 20-40 per cent of solvent when they reach the ring guide 16. The resulting yarn passes in contact with roll 17 and is wetted with water from trough 18. The wet yarn is fed by rolls 19, 20 to the ring spinner 23 and perforated bobbin 22. It may subsequently be washed free from solvent while still wound on the bobbin. For the stretching operation, the yarn 40 (Fig. 2) is passed first in contact with the wick 30, which applies to it an anti-static agent, and then round forwarding roll 32 on which it may be heated by the device 34. It is forwarded at a constant speed to the heating cabinet 35 through which superheated steam is continuously passed. The yarn is drawn from the cabinet by roll 38 which is rotated at such a speed as to stretch the yarn to the desired degree. The air entering the spinning cell may be at 124 DEG C. and the walls of the cell may be heated by circulating oil at 250 DEG C. in the jacket 4 (Fig. 1) so that the temperature of the air near the bottom of the cell is about 220 DEG C. Specification 737,258 is referred to.
GB15728/53A 1952-06-07 1953-06-08 Improvements in the production of filamentary materials of acrylonitrile polymers Expired GB737222A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US292274A US2761754A (en) 1952-06-07 1952-06-07 Process for the production of acrylonitrile polymer fibers

Publications (1)

Publication Number Publication Date
GB737222A true GB737222A (en) 1955-09-21

Family

ID=23123966

Family Applications (2)

Application Number Title Priority Date Filing Date
GB1238/54A Expired GB737258A (en) 1952-06-07 1953-06-08 Improvements in the manufacture of fibres from acrylonitrile polymers by dry-spinning methods
GB15728/53A Expired GB737222A (en) 1952-06-07 1953-06-08 Improvements in the production of filamentary materials of acrylonitrile polymers

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB1238/54A Expired GB737258A (en) 1952-06-07 1953-06-08 Improvements in the manufacture of fibres from acrylonitrile polymers by dry-spinning methods

Country Status (2)

Country Link
US (1) US2761754A (en)
GB (2) GB737258A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106757467A (en) * 2016-11-23 2017-05-31 上海斯瑞科技有限公司 A kind of superhigh molecular weight polyethylene fibers and preparation method thereof
US10472737B2 (en) 2015-06-25 2019-11-12 Manuel Torres Martinez Extrusion head for generating filaments, extrusion installation and method using said extrusion head
US10633769B2 (en) 2014-12-19 2020-04-28 Manuel Torres Martinez Method for producing filaments of polyacrylonitrile and extrusion head for carrying out said method

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2888317A (en) * 1953-04-10 1959-05-26 Du Pont Production of polyacrylonitrile filaments of high uniform density
BE540074A (en) * 1954-07-27
US2839354A (en) * 1956-03-22 1958-06-17 Celanese Corp Spinning
US2975022A (en) * 1958-05-20 1961-03-14 Du Pont Process for preparing acrylonitrile fibers
BE581751A (en) * 1958-08-18
US3194862A (en) * 1961-12-18 1965-07-13 Eastman Kodak Co Acrylonitrile spinning solutions and method of producing filaments therefrom
US3496263A (en) * 1965-07-21 1970-02-17 Asahi Chemical Ind Process for the recovery of n,n-dimethylformamides of n,n - dimethylacetamides from waste gases in the dry spinning of polyacrylonitrile by water contact and condensing
US3485913A (en) * 1965-10-20 1969-12-23 Toho Beslon Co New method of manufacturing acrylic fibers and the related products
US3502756A (en) * 1969-03-17 1970-03-24 Celanese Corp Process for dry spinning polybenzimidazoles
DE2502195C2 (en) * 1975-01-21 1983-12-29 Bayer Ag, 5090 Leverkusen Process for the production of acrylic fibers or threads
DE3308657A1 (en) * 1983-03-11 1984-09-20 Bayer Ag, 5090 Leverkusen CONTINUOUS PROCESS FOR PRODUCING POLYACRYLNITRILE FIBERS AND FIBERS
US5262110A (en) * 1992-07-31 1993-11-16 Eastman Kodak Company Apparatus and method for spinning filaments
JP6105203B2 (en) * 2009-02-17 2017-03-29 テイジン・アラミド・ビー.ブイ. Process for producing filament yarns from aromatic polyamides
CN113549974B (en) * 2021-09-22 2021-12-07 南通铭朗建筑机械有限公司 Local oxidation coating treatment device for machining of building machinery parts

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR722631A (en) * 1930-09-09 1932-03-22 Process and apparatus for the manufacture of artificial filaments, ribbons, etc., by extruding solutions of cellulose esters or ethers
FR741912A (en) * 1931-09-29 1933-02-23
NL55019C (en) * 1938-11-10
US2558732A (en) * 1947-09-04 1951-07-03 American Cyanamid Co Method of producing staple fiber from polymers and copolymers of acrylonitrile
US2607751A (en) * 1948-03-02 1952-08-19 Du Pont Acrylonitrile polymer dissolved in a dicarboxylic acid anhydride
US2622003A (en) * 1949-10-27 1952-12-16 American Viscose Corp Method of making shaped articles of an acrylonitrile polymer
US2615198A (en) * 1949-04-06 1952-10-28 Du Pont Spinning apparatus and method
US2605502A (en) * 1949-10-05 1952-08-05 Celanese Corp Preparation of filamentary material
US2564308A (en) * 1950-02-14 1951-08-14 Francis A Nagel Surface treatment of molds

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10633769B2 (en) 2014-12-19 2020-04-28 Manuel Torres Martinez Method for producing filaments of polyacrylonitrile and extrusion head for carrying out said method
US10472737B2 (en) 2015-06-25 2019-11-12 Manuel Torres Martinez Extrusion head for generating filaments, extrusion installation and method using said extrusion head
CN106757467A (en) * 2016-11-23 2017-05-31 上海斯瑞科技有限公司 A kind of superhigh molecular weight polyethylene fibers and preparation method thereof

Also Published As

Publication number Publication date
GB737258A (en) 1955-09-21
US2761754A (en) 1956-09-04

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