http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104955853-B
Outgoing Links
Predicate | Object |
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classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08L2205-025 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C09D133-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F220-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F20-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-001 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-02 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-01 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F20-18 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-02 |
filingDate | 2013-11-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2016-12-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2016-12-14-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-104955853-B |
titleOfInvention | Produce method and the mechanograph of methacrylate polymer compositions |
abstract | For the method producing methacrylate polymer compositions, it includes the first polymerization procedure, wherein enter first via the supply confession of reactor be thoroughly mixed type reactor by comprising raw material composite A containing raw material monomer A, polymerization initiator A and chain-transferring agent A no less than 50 weight % methyl methacrylates, and raw material composite A is thoroughly mixed in type reactor experience continuous bulk polymerization first, and takes out gained intermediate composition via the first outlet being thoroughly mixed type reactor;With the second polymerization procedure, wherein enter second via the supply confession of reactor by comprising be thoroughly mixed type reactor containing raw material monomer B, polymerization initiator B and raw material composite B of chain-transferring agent B no less than 50 weight % methyl methacrylates and the intermediate composition taken out in the first polymerization procedure, and raw material composite B and intermediate composition are thoroughly mixed in type reactor second and are further subjected to continuous bulk polymerization, and take out gained methacrylate polymer compositions via the second outlet being thoroughly mixed type reactor;Wherein meet public formula (I), (II), (III), (IV) and (V). |
priorityDate | 2012-12-03-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 257.