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filingDate 1979-12-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_67c68a88a245ca215f94be30514f2f91
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publicationDate 1980-06-25-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber EP-0012413-A1
titleOfInvention Process for the preparation of thermoplastic synthetic resins
abstract A) einem oder mehreren organischen Polyisocyanaten, B) gegebenenfalls einem oder mehreren im wesentlichen linearen Polyolen mit Molekulargewichten zwischen 400 und 10000 und C) einem oder mehreren Hydroxylgruppen und/oder Aminogruppen aufweisenden Kettenverlängerungsmitteln mit einem Molekulargewicht unter 400, nwobei das Verhältnis der NCO-Gruppen von Komponente A) zu den zerewitinoffaktiven Gruppen der Komponenten B) und C) zwischen 0,9 und 1,2 liegt, in Gegenwart eines vorgefertigten thermoplastischen Polymeren, vorzugsweise ABS-Polymer, Polycarbonat oder Polyurethan, in Extrudern, dadurch gekennzeichnet, daß man 4 bis 65 Gew.-%, bezogen auf Verfahrensprodukt, des vorgefertigten thermoplastischen Polymeren über eine erste Einspeisstelle in den Extruder einbringt, danach über eine zweite und gegebenenfalls weitere Einspeisstellen 35 bis 96 Gew.-%, bezogen.auf Verfahrensprodukt, der Komponenten A) bis C) dem auf geschmolzenen thermoplastischen Polymeren zudosiert und, nachdem die Umsetzung der Komponenten A) bis C) im wesentlichen abgeschlossen ist, das Verfahrensprodukt aus dem Extruder austrägt.Process for the production of thermoplastic chemical materials of high rigidity and good impact strength in the cold by implementation of A) one or more organic polyisocyanates, B) optionally one or more substantially linear polyols with molecular weights between 400 and 10,000 and C) one or more chain extenders having hydroxyl groups and / or amino groups and having a molecular weight below 400, wherein the ratio of the NCO groups of component A) to the zerewitinoffactive groups of components B) and C) is between 0.9 and 1.2, in the presence of a prefabricated thermoplastic polymer, preferably ABS polymer, polycarbonate or polyurethane, in extruders , characterized in that 4 to 65% by weight, based on the product of the process, of the prefabricated thermoplastic polymer is introduced into the extruder via a first feed point, then 35 to 96% by weight, based on a second and optionally further feed points Process product which components A) to C) metered onto the melted thermoplastic polymer and, after the reaction of components A) to C) has essentially been completed, discharges the process product from the extruder.n n n The process products are used, for example, for the production of films, gears, cable sheathing and seals.
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