http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-6838543-B2
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ec361cf7a6412a07a4e7cfccc45581ef |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G64-205 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G64-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G64-30 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G64-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G64-30 |
| filingDate | 2001-11-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2005-01-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_130a01ddacd3fbaaf58347ade121c883 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3eecd69e3a3685a9229fa2174f9bd8e4 |
| publicationDate | 2005-01-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | US-6838543-B2 |
| titleOfInvention | Method for producing polycarbonates |
| abstract | Polycarbonates are produced by reacting a monomeric carbonate component with at least one diphenol or dialcohol in the presence of a transesterification catalyst, wherein the molten component is mixed with the transesterification catalyst by stirring and a transesterification product is produced, which is polycondensated. For polycondensation, the transesterification product is passed through a preliminary reactor, at least one intermediate reactor and one final reactor, the reactors being connected in series and having a substantially horizontal driven shaft with stirrers attached thereto. It is ensured that in the preliminary reactor and in the final reactor a dwell time of the melt of 5 minutes to 2 hours is maintained, that the temperatures in the preliminary reactor are maintained in the range from 220 to 300° C. and in the final reactor in the range from 240 to 350° C., and that the pressure in the preliminary reactor is maintained in the range from 100 to 800 mbar and in the final reactor in the range from 0.1 to 50 mbar. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-7279544-B2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2009114523-A1 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/US-2005131197-A1 |
| priorityDate | 2000-12-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 33.