http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-102033267-B1
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F6-001 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D1-0082 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-582 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D1-0064 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D1-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F6-10 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-01 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-001 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08J11-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F210-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08L23-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F210-14 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F6-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F6-003 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F10-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F6-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08J11-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08L23-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F6-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-01 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-00 |
| filingDate | 2016-12-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2019-10-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2019-10-16-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | KR-102033267-B1 |
| titleOfInvention | Inline Blending Process |
| abstract | (a) one reactor (2, 8) fluidly connected to one low pressure separator (3, 9) downstream, and further connecting the low pressure separator (3, 9) back to the corresponding reactor (2, 8) Providing at least two reactor-low pressure separator units (1, 7) each comprising a recycle line (5, 11) in a parallel arrangement; (b) polymerizing olefin monomers having at least two carbon atoms in each reactor (2, 8) by solution polymerization; (c) forming a non-reducing reactor effluent stream comprising a homogeneous fluid phase polymer-monomer-solvent mixture in each reactor (2, 8); (d) passing the non-reducing reactor effluent stream from each reactor (2, 8) to the corresponding low pressure separator (3, 9); Wherein the temperature and pressure of the low pressure separators 3, 9 are adjusted so that the liquid phase and the gas phase are obtained to produce the polymer rich liquid phase and the polymer lean gas phase, (e) separating the polymer lean gas phase from the polymer rich liquid phase in each low pressure separator (3, 9) to form a separated polymer lean vapor stream and a separated polymer rich liquid stream; (f) combining the polymer rich liquid stream from step (e) in a further low pressure separator and / or mixer 13 to produce a combined polymer rich liquid stream 16; (g) reintroducing the polymer lean vapor stream from step (e) via recycle line (5, 11) to the corresponding reactor (2, 8); An in-line blending process for a polymer is disclosed that includes. |
| priorityDate | 2015-12-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 54.