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    • 4. 发明专利
    • AT385455T
    • 2008-02-15
    • AT04718934
    • 2004-03-10
    • BASF AG
    • GUENTHERBERG NORBERTCZAUDERNA BERNHARDSAUER MICHAELBARDON RAINERAN YOHWAN
    • B29B9/12B29B9/06
    • Granule surface contours include less than 10% concave locations, the remainder being convex, as determined by incident-light interference contrast spectroscopy. Independent claims are included for the following: (1) a method of manufacturing polymer granules comprising forcing a polymer melt through a nozzle into a cutting chamber flooded with coolant and dividing the polymer; (2) a method of manufacturing moldings, film or fibers; and (3) a method of quality control employing incident light interference contrast spectroscopy to measure and control concave inclusions in their surfaces. The interval between emerging from the nozzle and cutting to granules is less than 20 ms. The granules are cooled in liquid coolant to a temperature of 60-130[deg]C at a rate of 2-30[deg]C/s. Granule/coolant ratio is 0.03:1 to 0.12:1. Coolant is introduced into the chamber at a pressure of 1.1 bar. The quality control method, without consideration of granule surface curvature, determines ring-shaped reflections arising from concave locations, and the surface area they enclose. These areas are expressed as a ratio of the total observed surface area.
    • 6. 发明专利
    • Grafting polymer rubbers, useful in thermoplastic molding materials, comprises a grafting base and a grafting layer grafted with the grafting base obtained from vinylaromatic monomers and/or polar copolymerizable monomers
    • DE102005022630A1
    • 2006-11-16
    • DE102005022630
    • 2005-05-11
    • BASF AG
    • MC KEE GRAHAM EDMUNDBREULMANN MICHAELDUIJZINGS WILGUENTHERBERG NORBERTFISCHER WOLFGANGKOPPELMANN LARSSAUER MICHAEL
    • C08F279/00C08L51/00
    • Grafting polymer rubbers, obtained from a grafting base (a1) containing a first fraction group (i) by emulsion polymerization of produced particles with a particle diameter of less than 200 nm, and a second fraction (ii) by emulsion polymerization of produced particles with a particle diameter of greater than 550 nm; one or more grafting layer (a2) grafted with (a1) obtained from at least vinylaromatic monomers (a21) and/or at least a polar (a22) with copolymerizable monomers. Grafting polymer rubbers, obtained from a grafting base (a1) containing a first fraction group (i) by emulsion polymerization of produced particles with a particle diameter of less than 200 nm, and a second fraction (ii) by emulsion polymerization of produced particles with a particle diameter of greater than 550 nm, where the sum of the first fraction and the second fraction amounts to at least 75 wt.%, related to the total quantity of the particles of (a1), and the remaining 25 wt.%, related to the total quantity of the particles of (a1), where the particles are produced by emulsion polymerization, exhibits a particle diameter in the intermediate area between the particles of the first fractions and the particles of the second fractions, where (a1) is obtained from at least one alkyl acrylate (a11) with 1-32C atoms in the alkyl, optionally at least polyfunctional, crosslinking monomers (a12), optionally at least further monomers (a13), preferably vinylalkylether with 1-8C atoms in the alkyl, butadiene, isoprene, styrene, acrylonitrile, methacrylnitrile, methylmethacrylate, acrylic acid, methacrylic acid, itaconic acid and maleic acid anhydride, optionally groups (a14), from regulator-, initiator- and/or emulsifying agent systems; where a part or entire part of (a1) additionally exhibit a core, developed from 30-100 wt.% of at least vinylaromatic monomers and 0-70 wt.% of one or more further copolymerizable monomers, in each case related to the total quantity the core of forming monomers; and one or more grafting layers (a2) grafted with (a1), developed from at least vinylaromatic monomers (a21) and/or at least a polar (a22) with copolymerizable monomers, preferably from acrylonitrile, methacrylnitrile, esters of (meth)acrylic acid with 1-4C atoms in the acryl group, maleic acid anhydride and its imides, (meth)acrylamide and vinylalkylethers with 1-8C atoms in the alkyl; optionally groups (a23) from regulator-, initiator- and/or emulsifying agent systems. Independent claims are included for: (1) thermoplastic molding material comprising 5-90 wt.%, preferably 12-60 wt.% of particle forming grafting polymer, 10-95 wt.%, preferably 40-88 wt.% of at least one amorphous polymer, developed from at least vinylaromatic monomers and optionally at least ethylenic unsaturated monomers, or developed from methylmethacrylate and at least vinylaromatic monomers and/or optionally at least a further ethylenic unsaturated monomers, 0-75 wt.% of further polymers (b), preferably polycarbonates, polyamides, polyesters, polyetherketone, polyoxyalkylene, polyarylenesulfide, polyvinyl chloride or thermoplastic polyetherurethane, and 0-60 wt.% of fibers or particle forming fillers; and (2) molded articles, foils, fibers or foams obtained by using the thermoplastic molding materials.
    • 8. 发明专利
    • AT370830T
    • 2007-09-15
    • AT02021020
    • 2002-09-20
    • BASF AG
    • GUENTHERBERG NORBERTCZAUDERNA BERNHARDSAUER MICHAELBARDON RAINERAN YOHWAN
    • B29C48/395B29C48/76
    • The extruder has one or more degassing openings which are fitted with either a woven metal wire mesh, a finely perforated plate or a slit screen. Water is extracted either partially or completely in the fluid state. At least one dewatering opening is located upstream in front of a first metering unit and another downstream from the latter. Meshes are held in a frame pressed against the openings and in particular are folded onto an opening or attached to the latter by a bayonet connection. A preferred extruder has twin screws and: a) one or more metering sections in which thermoplastic material containing water or another vaporizable fluid is fed into the barrel and one or more dewatering openings; b) a compression section for dewatering a thermoplastic and including a restrictor and a dewatering opening; c) a feed section in which further thermoplastic melt is added; d) a mixing, kneading and/or plasticizing section; e) a degassing section in which residual water is extracted as steam via a dewatering opening; f) a metering section. All dewatering openings are fitted with a woven mesh, fine perforated plate or slit screen. Initial thermoplastic components contain not more than90wt% and are mixed with additional components while degassing and dewatering. Independent claims are included for: a) a process for manufacturing thermoplastics in which thermoplastic materials are fed into the claimed equipment, degassed and then metered; b) use of a metal wire mesh, fine perforated plate and/or slit screen for covering a degassing and/or dewatering opening in the claimed extruder.