http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-100465880-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F12-08 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-02 |
| filingDate | 2001-12-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2005-01-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2005-01-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-100465880-B1 |
| titleOfInvention | Process of the Thermoplastic Resin with High Tensile Strength and High Fluidity |
| abstract | The high rigidity thermoplastic resin of the present invention is the total flow rate of the styrene monomer is introduced into the first and second reactors in the first reactor, F, the total flow rate is introduced into the first reactor, F 1 , the total flow rate to the second reactor F 2 , when the reactor volume of the first reactor is V 1 and the volume of the reaction solution in the first reactor is V 1 ′, F = F 1 + F 2, 5.6 ≤ F 1 / F 2 ≤ 6.6, 1.8 ≦ V 1 / V 1 ′ ≦ 2.1; When the contents of the reactor in the second reactor are V 2 and the contents of the reaction solution in the second reactor are V 2 ′, 2.2 ≤ V 2 / V 2 '≤ 3.3, F = F 1 + F 2 Continuous bulk polymerization was carried out by continuously adding 0.3 to 1.2% by weight of a hydrocarbon compound on the basis of a final pellet under the condition of; Then, the unreacted monomer is separated from the polymer produced from the second reactor and then cut into pellets. The average molecular weight is 230,000 to 300,000, and the yellowness is 1.0 or less. |
| priorityDate | 2001-12-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 39.