http://rdf.ncbi.nlm.nih.gov/pubchem/patent/PL-188825-B1

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61L27-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G63-91
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61L27-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G63-48
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/A61F2-08
filingDate 1998-11-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b26e990aa6edd97c0e6459a1c0beb5af
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0b3ff8d89834c38e0c02b95e63d57fb5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_da1aa4298a2619ef51cb2ffc7ae85806
publicationDate 2005-04-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber PL-188825-B1
titleOfInvention Elastomer for temporary finger flexor tendon prosthesis and a method of production of elastomer
abstract 1. An elastomer for a temporary finger flexor tendon prosthesis, characterized by foldingnis made of a thermoplastic phthalic elastomer of formula I, in which it is alternately locatednthere are rigid oligo (butylene terephthalate) segments with a molecular weight of 220 to 2500nand flexible segments in the form of a dimerized fatty acid having 36 C atomsnin the molecule, the weight ratio of the rigid segments to the flexible segments in the chainnpolymer is 80:20 to 26:74.n5. Method of producing an elastomer for a temporary prosthesis of flexor tendons in the fingers,ncharacterized in that the thermoplastic phthalic elastomer is obtained by transesterificationn1,4-butancoliol dimethyl terephthalate to mono- or oligomers of butylene terephthalate weighingnmolecular weight 310 to 550 and subsequent polycondensation with the dimerized fatty acid containingn36 carbon atoms per molecule, the molar ratio in the transesterification reactionndimethyl terephthalate: 1,4-butanediol is as 1: 1.5 to 1: 2, and during polycondensation the rationmolar molar amount of dimethyl terephthalate used for transesterification to dimerizednfatty acid is 1: 1 to 1: 11.3, the transesterification and polycondensation reaction is carried out bynin the presence of the catalyst in an amount of 0.05 to 0.5 g per 1000 g of reaction mixturenand excipients in an amount of 0 to 5 g per 1000 g of reaction mixture, transesterification temperaturenis from 145 to 220 ° C and the polycondensation temperature is from 225 to 275 ° C andnduring the polycondensation, reduced pressure is applied to (1 torr, 133.322 Pa over a period of 20 ton90 minutes, and then the obtained product is subjected to extraction and after removing the extracting substancensterilization.
priorityDate 1998-11-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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