http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-0098485-A2

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filingDate 1983-06-24-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2cbdd5778443ba72ee14149078c2f3ca
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publicationDate 1984-01-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber EP-0098485-A2
titleOfInvention Continuous process for dry-spinning polyacrylonitrile fibres and filaments with a high shrinkage potential
abstract a) eine Spinnlösung versponnen wird, deren Viskosität bei 100°C 10-60 Kugelfallsekunden beträgt, b) die Verdampfung des Lösungsmittels im Spinnschacht so gesteuert wird, daß der Lösungsmittelgehalt der Fäden beim Verlassen des Spinnschachtes maximal 10 Gew.-%, bezogen auf Faserfeststoffgehalt, beträgt, c) die Fäden vor dem Verstrecken mit einer Präparation versehen werden, die ein Gleitmittel und ein Antistatikum enthält und den Fäden einen Feuchtegehalt von maximal 10 Gew.-%, bezogen auf Faserfeststoffgehalt, verleiht und d) die Fäden vor und während des Verstreckens mit keiner weiteren Extraktionsflüssigkeitfür das Spinnlösungsmittel in Kontakt treten. Ready to ship high shrinkable threads and fibers; from acrylonitrile copolymers can be produced continuously using the dry spinning method by a) a spinning solution is spun, the viscosity of which is 10-60 falling ball seconds at 100 ° C, b) the evaporation of the solvent in the spinning shaft is controlled so that the solvent content of the threads when leaving the spinning shaft is a maximum of 10% by weight, based on the fiber solids content, c) before stretching, the threads are provided with a preparation which contains a lubricant and an antistatic and which gives the threads a moisture content of at most 10% by weight, based on the fiber solids content, and d) the threads do not come into contact with any further extraction liquid for the spinning solvent before and during drawing.
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priorityDate 1982-07-06-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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