EP0466868A1 - Procede et dispositif de filage rapide de monofilaments et monofilaments fabriques par ce procede. - Google Patents

Procede et dispositif de filage rapide de monofilaments et monofilaments fabriques par ce procede.

Info

Publication number
EP0466868A1
EP0466868A1 EP91903030A EP91903030A EP0466868A1 EP 0466868 A1 EP0466868 A1 EP 0466868A1 EP 91903030 A EP91903030 A EP 91903030A EP 91903030 A EP91903030 A EP 91903030A EP 0466868 A1 EP0466868 A1 EP 0466868A1
Authority
EP
European Patent Office
Prior art keywords
monofilaments
friction
friction surface
friction element
monofilament
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.)
Granted
Application number
EP91903030A
Other languages
German (de)
English (en)
Other versions
EP0466868B1 (fr
Inventor
Klaus Fischer
Halim Baris
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.)
ExNex AG
Original Assignee
Rhone Poulenc Viscosuisse SA
Societe de la Viscose Suisse SA
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=4185113&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0466868(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Rhone Poulenc Viscosuisse SA, Societe de la Viscose Suisse SA filed Critical Rhone Poulenc Viscosuisse SA
Publication of EP0466868A1 publication Critical patent/EP0466868A1/fr
Application granted granted Critical
Publication of EP0466868B1 publication Critical patent/EP0466868B1/fr
Anticipated expiration legal-status Critical
Revoked legal-status Critical Current

Links

Classifications

    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/12—Stretch-spinning methods
    • D01D5/16—Stretch-spinning methods using rollers, or like mechanical devices, e.g. snubbing pins
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913—Rod, strand, filament or fiber
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913—Rod, strand, filament or fiber
    • Y10T428/298—Physical dimension

Definitions

  • the present invention relates to a method for high-speed spinning a family of thermoplastic monofilaments with a single titer of 1 to 30 dtex and a device for carrying out the method, as well as the monofilaments produced thereafter.
  • Fine monofilaments up to about 33 dtex are spun at spinning speeds of less than 1000 m / min, cooled with blown air, wound up and drawn separately in a second operation at about 750 m / min.
  • the object of the invention is to provide a process for the production of fine monofilaments which achieves and / or improves the properties of known monofilaments without a separate stretching process at high winding speeds.
  • Another object is to vary the method in such a way that desired properties of the monofilaments can be achieved by the setting parameters of the device.
  • the above-mentioned object is achieved in that the melt-spun monofilaments are passed directly over a friction element during the cooling by means of blown air ", then are spin-prepared and wound up.
  • the winding speed is 3000 to 6000 m / min., Preferably 4000 to 5000 m / min.
  • thermoplastics such as all kinds of polyesters, polyamides, in particular those known as nylon 66 or nylon 6, and also polyacrylic, polyvinylidene fluoride, made of polyethylene or polypropylene.
  • the device for carrying out the method essentially consists of a friction element which is arranged between the spinneret and the device for the preparation application.
  • the friction element is preferably fork-shaped formed, rotatable and movable in its distance from the spinneret.
  • the two opposite friction surfaces, an upper friction surface and a lower friction surface are arranged axially parallel.
  • a friction element which has been set and fixed once at a distance from the spinneret can be rotated about its axis continuously or in fixed steps in such a way that a desired tension can be provided on the thread lying between the friction surfaces.
  • the gradual adjustment has the advantage that the desired positions can be precisely re-adjusted at any time and a constant, reproducible thread tension is guaranteed.
  • the friction element can consist of a plurality of pins which have a cylindrical but also an oval surface. However, other bodies with curved surfaces can also be used.
  • a distance of the friction elements from the spinneret that is 20 to 280 cm, depending on the desired final titer of the monofilament.
  • the twist angle ⁇ between the thread path and the common axis of the friction element surfaces should be 0 to 40 degrees of angle and the wrap angle of the friction element / monofilament should be 50 "to 150 *.
  • the monofilament produced by the process should also meet the following conditions. a) an elongation of 20-45% b) a strength of 36-60 cN / tex c) a cooking shrinkage of 2-15% d) an irregularity of ⁇ 1% Uster and e) a uniform and round cross-section.
  • the invention is to be illustrated schematically on the basis of a drawing.
  • Fig. 1 The arrangement of the friction elements according to the invention in the region of a blow shaft with several monofilaments.
  • a spinneret is shown schematically at 1 in FIG.
  • a friction element 3 is arranged between the spinneret 1 and a winder 7.
  • the height of the friction element 3, as indicated by arrows, is adjustable.
  • the friction element 3 consists of a friction surface 4 and a friction surface 5, which are arranged around an axis 8.
  • the friction element 3 is rotatable so that a monofilament 2 or a family of monofilaments which is passed between the friction surface 4 and the friction surface 5 and which is represented by the monofilaments 2 and 2 'delimiting the thread family are subjected to a frictional force can.
  • a device 6 for applying a spin finish is provided between the friction element 3 and the winder 7.
  • Fig. 2 the rotatability of the friction element is indicated by arrows.
  • Fig. 2a the monofilament 2 passes between the friction surface 4 and the friction surface 5.
  • Figure 2b the friction element 3 and the friction surfaces 4 and 5 are shown in side view.
  • FIG. 3 the height adjustment of the Reib comprise ⁇ 3 as a whole unit and that of the friction surface 5 compared to 4 is indicated by the double arrows.
  • Fig. 3a the thread leads between the frosted surface 4 and the friction surface 5.
  • Figure 3b is a side view of Figure 3a.
  • Fig. 4b is a side view of Fig. 4a.
  • a group of threads emerges from the spinneret 1, consisting of the monofilaments 2, 2 'delimiting the group, which run parallel through the friction element at high speed and are stretched over the friction surface 4 and the friction surface 5 by means of the winder 7.
  • a suitable spin preparation 6 is applied on the path between the friction element 3 and the winder 7. If necessary, a godet can also be arranged between the friction element and the winder.
  • the resulting monofilament is a finished product for further processing.
  • Polyester with a Vl of 74 dl / g and a melt temperature of approx. 287 * C is extruded through a spinneret 1 x 6 / 0.33 / 4D and drawn off at a speed of 5000 m / min and blowing air with 0.25 - 0.4 m / s cooled.
  • the distance between the spinneret and the friction element is 30-160 cm, depending on the titer.
  • a spinning preparation is applied to the thread at a distance of h + 40 cm.
  • the adjustment of the friction elements (Fig. 2) was carried out in three different stages, 0 ⁇ , 20 * and 40 °, measured against the direction of the thread. The measurement results are shown in Table 1. (Winding speed 5000 m / min)
  • the wrap angle is (friction element according to FIG. 2) when in position
  • Table 2 shows the yarn parameters of a test with a winding speed of 4000 m / min. summarized. Other spinning conditions as in Example 1.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Prostheses (AREA)
  • Artificial Filaments (AREA)

Abstract

Dans ce procédé pour le filage rapide simultané de plusieurs monofilaments ayant un titre de 1 à 30 dtex, les monofils sont refroidis par soufflage d'air, levés sur un frottoir et bobinés directement. Le dispositif se compose d'un frottoir (3) avec des surfaces de frottement parallèles (4, 5). Le frottoir (3) se déplace dans le sens de la hauteur et peut pivoter pour régler le frottement entre ce frottoir et un monofil (2) ou un groupe de monofils. Le monofilament produit possède une résistance de 36 à 60 cN/tex, un allongement de 20 à 40 % et un retrait à la cuisson de 2 à 15 %.
EP91903030A 1990-02-05 1991-02-05 Procede de filage rapide de monofilaments et monofilaments fabriques par ce procede Revoked EP0466868B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CH35490 1990-02-05
CH354/90 1990-02-05
PCT/CH1991/000027 WO1991011547A1 (fr) 1990-02-05 1991-02-05 Procede et dispositif de filage rapide de monofilaments et monofilaments fabriques par ce procede

Publications (2)

Publication Number Publication Date
EP0466868A1 true EP0466868A1 (fr) 1992-01-22
EP0466868B1 EP0466868B1 (fr) 1996-01-24

Family

ID=4185113

Family Applications (1)

Application Number Title Priority Date Filing Date
EP91903030A Revoked EP0466868B1 (fr) 1990-02-05 1991-02-05 Procede de filage rapide de monofilaments et monofilaments fabriques par ce procede

Country Status (8)

Country Link
US (2) US5266254A (fr)
EP (1) EP0466868B1 (fr)
JP (1) JPH04506550A (fr)
KR (1) KR920701536A (fr)
BR (1) BR9104410A (fr)
CA (1) CA2049989A1 (fr)
DE (1) DE59107297D1 (fr)
WO (1) WO1991011547A1 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995001471A1 (fr) * 1993-07-02 1995-01-12 Rhone-Poulenc Viscosuisse S.A. Procede de production de monofilaments antisalissure et antiabrasion et leur utilisation
DE4336097A1 (de) * 1993-10-22 1995-04-27 Bayer Ag Kontinuierliches Verfahren zum Schmelzspinnen von monofilen Fäden
DE19600090A1 (de) * 1996-01-03 1997-07-10 Bayer Faser Gmbh Verfahren und Vorrichtung zur Herstellung von schmelzgesponnenen Monofilen
US20030050692A1 (en) * 2000-12-22 2003-03-13 Avantec Vascular Corporation Delivery of therapeutic capable agents
DE102009042229A1 (de) * 2009-09-18 2011-04-14 Oerlikon Textile Gmbh & Co. Kg Vorrichtung zum Schmelzspinnen, Behandeln und Aufwickeln eines multifilen Fadens

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE511735A (fr) * 1951-03-14
US3511905A (en) * 1967-08-22 1970-05-12 Viscose Suisse Soc Process for the preparation of synthetic polymer filaments
US3899562A (en) * 1970-04-15 1975-08-12 Vickers Zimmer Ag Process for the production of mixed yarns
US3715421A (en) * 1970-04-15 1973-02-06 Viscose Suisse Soc D Process for the preparation of polyethylene terephthalate filaments
DE2347801A1 (de) * 1973-09-22 1975-04-10 Metallgesellschaft Ag Verfahren zur herstellung vororientierter endlosfaeden
JPS52137022A (en) * 1976-05-12 1977-11-16 Teijin Ltd Production of synthetic fibers
DE2840988C2 (de) * 1978-09-21 1986-01-23 Akzo Gmbh, 5600 Wuppertal Verfahren zur Herstellung von Monofilen
JPS5545644A (en) * 1978-09-29 1980-03-31 Microbial Chem Res Found 6'-c-alkyl-3'-deoxykanamycin b or 6'-c-alkyl-3',4'-dideoxykanamycin b and their preparation
DE3173948D1 (en) * 1980-02-18 1986-04-10 Ici Plc Process for forming a continuous filament yarn from a melt spinnable polyethylene terephthalat and novel polyester yarns produced by the process
EP0095712B2 (fr) * 1982-05-28 1993-06-23 Asahi Kasei Kogyo Kabushiki Kaisha Fibres en téréphtalate de polyéthylène pouvant être aisément teintes, et procédé pour leur fabrication
JPS59125904A (ja) * 1982-12-27 1984-07-20 Teijin Ltd 分繊用ポリエステルマルチフイラメントの製造法
FR2540893B1 (fr) * 1983-02-16 1985-11-08 Rhone Poulenc Fibres Procede simplifie de filage de polyamide a grande vitesse
DD273291A1 (de) * 1983-06-30 1989-11-08 Ulrich Worreschk Anordnung zur erhoehung der kristallitorientierung in schnellgesponnenen polyesterfaeden
JPH0674526B2 (ja) * 1984-04-10 1994-09-21 株式会社クラレ 紡糸直結延伸ポリエステル糸の製造法
IN166291B (fr) * 1984-09-27 1990-04-07 Norddeutsche Faserwerke Gmbh
DE3534079C2 (de) * 1984-09-27 1986-08-07 Norddeutsche Faserwerke GmbH, 2350 Neumünster Verfahren zum Herstellen von Glattgarn
JPS6228404A (ja) * 1985-07-26 1987-02-06 シ−サ−　スマ−　パクハ 合成材料の前延伸モノフイラメント糸の製造法
DE3609209A1 (de) * 1986-03-19 1987-09-24 Akzo Gmbh Verfahren zur herstellung schmelzgesponnener und molekularorientierend verstreckter, kristalliner filamente
DE3823337A1 (de) * 1987-07-18 1989-01-26 Barmag Barmer Maschf Verfahren zum herstellen von glattgarn
JPH01111011A (ja) * 1987-10-23 1989-04-27 Unitika Ltd ナイロン４６繊維の製造方法
DE3819913A1 (de) * 1988-06-11 1989-12-21 Davy Mckee Ag Verfahren zur herstellung gleichmaessiger poy-filamente
US5087401A (en) * 1988-11-24 1992-02-11 Toray Industries, Inc. Process for preparing polyester filamentary material
US5171504A (en) * 1991-03-28 1992-12-15 North Carolina State University Process for producing high strength, high modulus thermoplastic fibers

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9111547A1 *

Also Published As

Publication number Publication date
KR920701536A (ko) 1992-08-12
US5431999A (en) 1995-07-11
BR9104410A (pt) 1992-04-21
EP0466868B1 (fr) 1996-01-24
JPH04506550A (ja) 1992-11-12
DE59107297D1 (de) 1996-03-07
CA2049989A1 (fr) 1991-08-06
US5266254A (en) 1993-11-30
WO1991011547A1 (fr) 1991-08-08

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