GB1230991A - - Google Patents

Info

Publication number
GB1230991A
GB1230991A GB2483667A GB1230991DA GB1230991A GB 1230991 A GB1230991 A GB 1230991A GB 2483667 A GB2483667 A GB 2483667A GB 1230991D A GB1230991D A GB 1230991DA GB 1230991 A GB1230991 A GB 1230991A
Authority
GB
United Kingdom
Prior art keywords
filament
dispersion
component
core
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
GB2483667A
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 filed Critical
Publication of GB1230991A publication Critical patent/GB1230991A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • D01D11/00Other features of manufacture
    • D01D11/06Coating with spinning solutions or melts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/05Filamentary, e.g. strands
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/304Extrusion nozzles or dies specially adapted for bringing together components, e.g. melts within the die
    • 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
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • D01D5/34Core-skin structure; Spinnerette packs therefor

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Multicomponent Fibers (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

1,230,991. Composite filaments. O.-B. RASMUSSEN. 29 May, 1968 [30 May, 1967], No. 24836/67. Heading B5B. [Also in Division D1] A filament comprises a core of a substantially homogeneous polymer material A and, as a coat, a fine dispersion in the stretched state of at least two mutually incompatible polymer materials B and C, B being compatible with A and bonded to A at the interface of the core and the coat, C being easily removable, and B forming a fibrous structure having an average fibre diameter not exceeding 10Á, the fibres on the average being arranged around the core in a helical orientation. Preferably, component B is in the form of crystal whiskers, has a higher melting range than component A, and has a higher modulus of elasticity than component A. Suitably component A is a copolymer containing a major proportion of the segments from which component B is formed, and thus A may be an elastomeric polyurethane copolymer and component B a compatible polyurethane homopolymer. Alternatively, A may be a polyamide copolymer and B a polyamide homopolymer. The filament is made by extruding a continuous filament of a filament-forming substantially homogeneous polymer material A, applying to the surface of said filament, while it is being extruded, a coating material consisting of a fine dispersion of at least two mutually incompatible polymer materials B and C, B being compatible with A and capable of adhering thereto, C being easily removable, and subjecting said coated filament, while still in a fluid or semi-fluid state, to simultaneous stretching and twisting. B and C may be mixed at random to a fine dispersion, which is extruded through one channel system and A extruded through another channel system, the two polymer streams united in a rotating nozzle designed to apply the dispersion as a coating on a core of A, the coated filament hauled off by means not following the rotation of said nozzle, and the filament solidified by cooling. Thus in Fig. 2, 1 is a rotating nozzle, 2 a static part for feeding a polymer A and 3 a static inlet part for the polymer dispersion (B+C). Polymer A is fed through channel 4, which is connected to one extruder, whereas the polymer dispersion is fed through channel 5 connected to another extruder. Channel 5 widens out to a ring-formed chamber 6, which is in connection with a series of channels 7 arranged in star-form in the rotating part. The dispersion is thus coated upon the core material in the chamber 8. During the passage through channels 5, 6, 7 and 8, the dispersion is strongly drawn and thus acquires a fibre-like structure in the melted state. The filament is hauled off from the nozzle by rollers which do not follow the rotation of 1, and thus the structure of the stretched dispersion is arranged helically. Air cooling is applied to solidify the component B of the dispersion immediately after the extrusion, and the cooling effect is so controlled that the crystallization of B takes place when A has only been stretched to a very small extent, whereas a deep drawdown of the core A is allowed after the crystallization of B. Fig. 1 shows the structure of a filament formed from a composite filament by removal of C, e.g. by dissolution, and shows the fibrous sponge or network formed material B twisted around the core material A. The meshes of the network or sponge formed by B may be very open because of the drawing-down of the core A. In the example, A is a copolymer of polyhexamethylene adipamide and polycaprolactam in a copolymerization ratio of 40/60, B is polycaprolactam homopolymer, and C is polyethylene. The relative proportions of A, B and C are 50: 50:10. B and C are first dry-blended, then mixed in a planetary screw extruder from which the dispersion is fed to the device of Fig. 2. Component A is fed to the die by means of a normal extruder. The diameter of the orifice of the extruder is 0À5 mm., and the filament is drawn-down to a diameter of 0À08 mm., while the copolymer is still molten. The final product has a twist of about 1 rotation per cm.
GB2483667A 1967-05-30 1967-05-30 Expired GB1230991A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2483667 1967-05-30

Publications (1)

Publication Number Publication Date
GB1230991A true GB1230991A (en) 1971-05-05

Family

ID=10217998

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2483667A Expired GB1230991A (en) 1967-05-30 1967-05-30

Country Status (5)

Country Link
US (1) US3651195A (en)
DE (1) DE1760518A1 (en)
DK (1) DK117312B (en)
FR (1) FR1568499A (en)
GB (1) GB1230991A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4814131A (en) * 1987-07-02 1989-03-21 Atlas Sheldon M Process for producing a shaped article, such as fiber composed of a hydrophobic polymer and a hydrophilic polymer

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1988009836A1 (en) * 1985-12-10 1988-12-15 Christopher Francis Coles Improvements in or related to fibres
DE3604001A1 (en) * 1986-02-08 1987-08-13 Reifenhaeuser Masch Process and apparatus for producing a multimaterial monofilament strand from thermoplastic material
DE4120165C2 (en) * 1990-07-05 1995-01-26 Friedrichs Konrad Kg Extrusion tool for producing a hard metal or ceramic rod
DE4120166C2 (en) * 1991-06-19 1994-10-06 Friedrichs Konrad Kg Extrusion tool for producing a hard metal or ceramic rod with twisted inner holes
US6122877A (en) * 1997-05-30 2000-09-26 Andersen Corporation Fiber-polymeric composite siding unit and method of manufacture
GB0608462D0 (en) * 2006-04-28 2006-06-07 Auxetix Ltd Detection system
CN108179487A (en) * 2018-02-07 2018-06-19 常熟市翔鹰特纤有限公司 A kind of synthetic fibers rotary spinning system and spinning process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4814131A (en) * 1987-07-02 1989-03-21 Atlas Sheldon M Process for producing a shaped article, such as fiber composed of a hydrophobic polymer and a hydrophilic polymer

Also Published As

Publication number Publication date
US3651195A (en) 1972-03-21
FR1568499A (en) 1969-05-23
DE1760518A1 (en) 1971-12-23
DK117312B (en) 1970-04-13

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees