US3122412A - Production of fibres of acrylonitrile polymers - Google Patents

Production of fibres of acrylonitrile polymers Download PDF

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Publication number
US3122412A
US3122412A US45558A US4555860A US3122412A US 3122412 A US3122412 A US 3122412A US 45558 A US45558 A US 45558A US 4555860 A US4555860 A US 4555860A US 3122412 A US3122412 A US 3122412A
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US
United States
Prior art keywords
yarn
filaments
ketone
treated
drawn
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 - Lifetime
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US45558A
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English (en)
Inventor
Menault Jacques Andre Armand
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.)
Crylor SA
Original Assignee
Crylor SA
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Filing date
Publication date
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Publication of US3122412A publication Critical patent/US3122412A/en
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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
    • D02J1/221Preliminary treatments
    • 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

Definitions

  • acrylonitrile polymers are meant acrylonitrile homopolymer as well as copolymers and grafted polymers containing from 85% to 100% of acrylonitrile and up to 15 of one or more copolymerisable ethylenic compounds, and mixtures of such polymers.
  • undrawn filaments filaments made by dry or wet spinning before they have undergone their complete drawing. They may have undergone a treatment for the extraction of the solvent employed in their spinning, for example by washing, and/or a preliminary drawing. Depending upon the subsequent use for which they are intended, these filaments are combined in groups to form either yarns of relatively low count, which will be employed as continuous yarns, or tows of higher count which will thereafter be cut or cracked to obtain staple fibre. it is these filaments combined in groups of variable size which are treated in accordance with the invention and then drawn.
  • the treatment or treatments of the invention can be carried out at any desired instant between the extrusion of the filaments and their final drawing.
  • the filaments may be passed through a bath containing a ketone immediately after they leave the spinning zone, or the spinning solvent can be extracted by one or more washings with a ketone, or one or more immersions in a ketone may be effected before or after elimination of the solvent by known means, or a number of these treaments may be carried out in conjunction.
  • the treatment or treatments according to the invention may be effected either continuously or discontinuously, if desired after a preliminary drawing.
  • the duration of the treatment or treatments of the invention may vary within wide limits. In any case, it must be suiiicient to ensure good contact of the filaments with the ketone. For example, in the case of the discontinuous immersion of a larger or compact wound package of filaments, the duration of the immersion must be sufficient to ensure contact of the ketone with all the filaments as far as the centre of the package. An immersion duration of from to 30 minutes is then generally preferred. If the filaments are continuously passed through the bath containing the ketone, a virtually instantaneous contact may be sufiicient in the case of a gr up of filaments of relatively low count.
  • an oiling agent soluble in the ketone such as a condensation product of ethylene oxide with a fatty alcohol, an alkyl higher fatty acid ester such as butyl stearate, etc.
  • the final drawing may be carried out by known means.
  • One of the main advantages of the present invention resides in the fact that owing to the greatly improved drawing properties of the treated yarns it is possible to increase the extent of the drawing, and therefore the tenacity of the drawn yarn, while maintaining its flexibility and elongation.
  • the maximum degree of drawing i.e. the degree of drawing above which breakage of the yarn occurs, is considerably higher than in the case of an untreated yarn.
  • the laws governing the tension during drawing are fundamentally modified.
  • the tension necessary for the drawing is substantially independent of the extent of the drawing, while in the case of the untreated yarn the tension necessary increases with the extent of drawing.
  • an undrawn yarn treated entirely with a ketone, such for example as acetone, from the time of its extrusion, and thus in a completely dry state possesses before drawing a high elongation at ambient temerature, as also great flexibility, while an untreated yarn has very low elongation and has no flexibility, so that it is rendered brittle in the course of the manipulations.
  • Another advantage of the process is that it makes it possible to draw a treated yarn to the same extent as an untreated yarn but with greater safety, i.e. without the risk or" the formation of hairs on the yarn as a result of the rupture of a number of filaments during the drawing.
  • Example I A polyacrylonitrile yarn obtained by dry spinning a solution of polyacrylonitrile in dimethylfcrmamide is washed with water in order to remove the residual solvent and then immersed at room temperature for 10 minutes in a bath of diethylketone containing 1% of a condensation product of ethylene oxide with a fatty alcohol, calculated on the weignt of yarn immersed. It is thereafter drawn in steam at a temperature of 98 C.
  • This yarn can be readily drawn to twelve times its origi nal length, wln'le a comparison specimen not washed with diethylketone cannot easily be drawn beyond 6.5 times its original length.
  • the final tenacity of the yarn treated with diethylketone is considerably greater than that of the comparison specimen, though its elongation is substantially the same.
  • Example 11 A copolymer yarn containing by wei ht of acrylontirlle and 10% by weight of vinyl dimethylaminoethyl eti er obtained by dry spinning is treated just bei is first twice washed with water.
  • Example IV A yarn obtained by dry spinning a mixture of 85% by weight of polyacrylonitrile and 15% by weight of polyvinyl acetate is treated just before it leaves the spinning cell with an aqueous liquid in accordance wtih the aforesaid French Patent 1,052,539.
  • the yarn obtained has a Water content of 100% of its dry weight. It is successively treated in three acetone baths at room temperature.
  • the water content of the yarn varies as follows:
  • the third bath contains 1% of a condensation prodnot of ethylene oxide with a fatty alcohol, calculated on the weight of the treated yarn.
  • the yarn thus obatined can readily be drawn to 12 times its original length, while a yarn treated in the same way, but with Water instead of acetone, can only with difficulty be drawn to more than 8 times its original length.
  • Example V A tow of polyacrylonitrile obtained by wet spinning It is pre-drawn by 10% of its initial length, whereafter it is immersed for minutes at room temperature in a methylethylketone bath containing 1% of butyl stearate calculated on the weight of the tow treated. It is thereafter readily drawn by a factor of 10, while a similar tow, treated only with water, can be drawn only with difficulty by more than 7 times its original length.
  • Example VI A polyacrylonitrile yarn obtained by dry spinning is treated with acetone just before it leaves the spinning cell. t is collected in a perforated pot, which is thereafter successively immersed in three acetone baths for 10 minutes in each bath, the last bath containing 0.8% of a condensation product of ethylene oxide with a fatty alcohol, calculated on the weight of the treated yarn.
  • the yarn is thereafter readily drawn at elevated tem* perature to 11 times its initial length, while an identical yarn, which has undergone treatments with water instead of acetone, can only with difiiculty be drawn to more than 7 times its original length. Even in the cold state before the drawing, the yarn treated with acetone possesses a drawing capacity higher than 3, while that of a comparison yarn treated with water is only 1.5 under the same conditions.
  • Example VII A polyacrylonitrile yarn obtained by dry spinning is first washed in counter-current with water in order to remove the residual solvent. It is collected in a perforated pot, which is thereafter successively immersed in two baths containing of acetone and 30% of water for 10 minutes in each bath.
  • the yarn thus treated can be readily drawn at elevated temperature to 11.5 times its original length, while a comparison yarn only washed with water and not treated with the acetone-water bath can only with difilculty be drawn to more than 6.8 times its original length.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Artificial Filaments (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
US45558A 1959-07-30 1960-07-27 Production of fibres of acrylonitrile polymers Expired - Lifetime US3122412A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR801528A FR1240653A (fr) 1959-07-30 1959-07-30 Perfectionnement à l'obtention de fibres en polymères à base d'acrylonitrile

Publications (1)

Publication Number Publication Date
US3122412A true US3122412A (en) 1964-02-25

Family

ID=8717738

Family Applications (1)

Application Number Title Priority Date Filing Date
US45558A Expired - Lifetime US3122412A (en) 1959-07-30 1960-07-27 Production of fibres of acrylonitrile polymers

Country Status (7)

Country Link
US (1) US3122412A (es)
CH (1) CH386617A (es)
DE (1) DE1186977B (es)
ES (1) ES259995A1 (es)
FR (1) FR1240653A (es)
GB (1) GB954553A (es)
NL (1) NL254391A (es)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3491179A (en) * 1967-01-03 1970-01-20 American Cyanamid Co Preparation of acrylonitrile polymer fibers
US3925524A (en) * 1972-06-22 1975-12-09 Celanese Corp Process for the production of carbon filaments
US4013753A (en) * 1973-10-09 1977-03-22 Bayer Aktiengesellschaft Process for the production of spontaneously crimping polyacrylonitrile composite fibres with improved crimp properties

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2579451A (en) * 1948-12-31 1951-12-18 Du Pont Polymeric materials
US2589294A (en) * 1948-02-26 1952-03-18 Goodrich Co B F Vinylidene cyanide polymers and polymer products
US2768868A (en) * 1953-03-27 1956-10-30 Du Pont Improving the dyeing uniformity and thermostability of undrawn acrylonitrile polymer filaments by applying steam under pressure
US2916348A (en) * 1956-08-21 1959-12-08 American Cyanamid Co Production of polyacrylonitrile filaments

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB720380A (en) * 1952-01-10 1954-12-15 British Celanese Improvements in the manufacture of filamentary material from copolymers of acrylonitrile and vinylidene chloride
DE961288C (de) * 1953-08-03 1957-04-04 Glanzstoff Ag Verfahren zum Aufrauhen und Mattieren von Faeden aus Polyaethylenterephthalaten

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2589294A (en) * 1948-02-26 1952-03-18 Goodrich Co B F Vinylidene cyanide polymers and polymer products
US2579451A (en) * 1948-12-31 1951-12-18 Du Pont Polymeric materials
US2768868A (en) * 1953-03-27 1956-10-30 Du Pont Improving the dyeing uniformity and thermostability of undrawn acrylonitrile polymer filaments by applying steam under pressure
US2916348A (en) * 1956-08-21 1959-12-08 American Cyanamid Co Production of polyacrylonitrile filaments

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3491179A (en) * 1967-01-03 1970-01-20 American Cyanamid Co Preparation of acrylonitrile polymer fibers
US3925524A (en) * 1972-06-22 1975-12-09 Celanese Corp Process for the production of carbon filaments
US4013753A (en) * 1973-10-09 1977-03-22 Bayer Aktiengesellschaft Process for the production of spontaneously crimping polyacrylonitrile composite fibres with improved crimp properties

Also Published As

Publication number Publication date
NL254391A (es)
CH386617A (fr) 1965-01-15
GB954553A (en) 1964-04-08
ES259995A1 (es) 1960-12-01
DE1186977B (de) 1965-02-11
FR1240653A (fr) 1960-09-09

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