http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-1038996-A

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G63-78
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-82
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G63-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G63-78
filingDate 1975-10-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1978-09-19-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_08c1eaee8408bcbb29ea3d7abc26484f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_483119941d95142ac094cef823909e14
publicationDate 1978-09-19-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CA-1038996-A
titleOfInvention Continuous manufacture of linear polyesters
abstract ABSTRACT OF THE DISCLOSURE An improved process for the continuous manufacture of linear high molecular weight polyesters by direct esterification of terephthalic acid with excess glycols in a medium comprising terephthalic acid glycol esters or their oligomers, under superatmospheric pressure at temperatures above 200°C, followed by polycondensation in the presence Or catalysts at from 260 to 290°C. The improvement is that the mixture fed to the esterification contains terephthalic acid and glycols in the molar ratio of 1:1.15 to 1:1.5 and that during the esterification from 20 to 30% by weight Or the excess of glycols over the molar ratio terephthalic acid:glycols = 1:1 are continuously distilled from the reaction mixture.
priorityDate 1974-10-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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