Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_d95a0e44f20e2fd97d30ea0cc6bfdb62 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_b21b7fa3458beede6fc661023edbfc81 http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_6c8d4dc7bd1a30d8fda907fceaeb4e69 |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J2369-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00006 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00083 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00085 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G64-307 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F27-708 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J5-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F27-706 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-1862 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F27-11251 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01F27-702 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G64-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08J5-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08J3-12 |
filingDate |
2012-03-30-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_00a85459106202dd371afddf6b7c0c21 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7b447ad2e666652fba1e372afee89051 |
publicationDate |
2012-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
WO-2012133856-A1 |
titleOfInvention |
Method for producing polycarbonate resin, polycarbonate resin pellets and stretched film |
abstract |
The present invention pertains to a method for producing a polycarbonate resin by continuously feeding a carbonic acid diester and a dihydroxy compound containing a dihydroxy compound having a fluorene structure, with a polymerization catalyst, to reaction vessels, and conducting polycondensation. This method for producing a polycarbonate resin is characterized in that: the reaction vessels consists of at least a plurality of vessels connected in a series; the temperature inside the reaction vessel one before the last polymerization reaction vessel is 200°C to 225°C; and the melt viscosity of the reaction solution at the outlet of the reaction vessel one before the last polymerization reaction vessel is 20 Pa⋅s to 1000 Pa⋅s. |
priorityDate |
2011-03-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |