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公开(公告)号:US3583140A
公开(公告)日:1971-06-08
申请号:US3583140D
申请日:1969-08-12
Applicant: BASF AG
Inventor: LORENZ FRIEDRICH , LABER WALTER
CPC classification number: D02G1/04
Abstract: Apparatus for manufacturing bulky yarns employing flowing gaseous or liquid media by the false twist technique. It consists of a tubular yarn guide chamber and a lateral conduit for the fluid medium disposed perpendicularly to the axis of the guide chamber and opening into same tangentially to the internal wall thereof, the guide chamber being cylindrical and at the yarn inlet end having a drastically reduced cross-sectional area compared to the cross section of the remainder of the chamber. The fluid inlet is located immediately downstream of the yarn inlet end (in the direction of movement of the yarn) in the enlarged portion of the chamber. The latter narrows at a point downstream of the fluid inlet (in the direction of movement of the yarn) and subsequently opens into a tubular duct the internal wall of which contains groovelike recesses over at least part of its length.
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公开(公告)号:CA889646A
公开(公告)日:1972-01-04
申请号:CA889646D
Applicant: BASF AG
Inventor: LORENZ FRIEDRICH , LABER WALTER
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公开(公告)号:DE2038403A1
公开(公告)日:1972-02-10
申请号:DE2038403
申请日:1970-08-01
Applicant: BASF AG
Inventor: LORENZ FRIEDRICH DIPL-ING DR , LABER WALTER
IPC: D02G1/16
Abstract: Synthetic linear polymeric yarn crimping device in which the yarns are texturised 3-dimensionally without formation of knots or loops is formed by a cylindrical pressure chamber having a coaxial yarn inlet and a convergent/divergent crimped yarn discharge nozzle whose throat has a cross-sectional area which is smaller than the cross-sectional area of the gaseous media supply duct terminating radially in the chamber.
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公开(公告)号:CA942446A
公开(公告)日:1974-02-19
申请号:CA118903
申请日:1971-07-22
Applicant: BASF AG
Inventor: LABER WALTER , GOTTSCHALK ALFRED , SCHWAAB JOSEF , JECKEL GUENTER , MOSTHAF HELMUT
Abstract: 1348286 Incorporating grafted rubbers into thermoplastics material BADISCHE ANILIN- & SODA-FABRIK AG 29 July 1971 [30 July 1970] 35617/71 Heading C3G A process for incorporating rubber into a thermoplastics material comprises precipitating a rubber latex, freeing the rubber mechanically of 10-98% of its initial water content so that the resulting rubber contains 2-50% by weight water, mixing the said rubber with the thermoplastics material at a temperature which is above the softening point of the thermoplastics materials, and removing the remainder of water during or after the incorporation. The thermoplastics material may be a homopolymer or copolymer of styrene, vinyl chloride or methyl methacrylate. Numerous rubbers are specified but it is preferred to use graft copolymers in which monomers forming rigid polymers are polymerized in aqueous emulsion on to a rubber base. The finished plastics material advantageously contains 5-60%, preferably 10-50%, by weight of the rubber worked into 95-40%, preferably 90-50%, by weight of thermoplastics material. The initial water removal may be carried out by filtration, pressing or centrifugation. Incorporation of the rubber into the thermoplastics material may be carried out in conventional mixing equipment, advantageously extruders or kneaders. The thermoplastics may be introduced into the mixing equipment as a melt. Alternatively it is possible to start from a dispersion of the thermoplastics material, to precipitate and partly dehydrate the same, and then to work it into the moist rubber. When an extruder is used it is advantageous to meter in the moist rubber first since this may be carried out under mild conditions without using superatmospheric conditions. After the thermoplastics material and rubber have passed through together the two components are mixed homogeneously together, at a temperature above the softening point of the thermoplastics material. The remaining water is removed by counterpressure or evaporation. In the example a styrene/acrylonitrile (70:30) copolymer is incorporated into a rubber latex produced by emulsion graft polymerization of 50 parts by weight of a mixture of styrene and acrylonitrile (70 : 30) in the presence of 100 parts by weight of a butadiene/butyl acrylate (40 : 60) copolymer.
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