http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-20030055441-A

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filingDate 2001-12-26-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_54d08caea8ed2220e5782c749b179cae
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publicationDate 2003-07-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20030055441-A
titleOfInvention Process of High Flow Thermoplastic Resin Having Good Moldability
abstract In the high flow thermoplastic resin of the present invention, the total flow rate of the styrene monomer to the first and second reactors in the first reactor is F, the total flow rate to the first reactor is F 1 , and 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, 6.2 ≤ F 1 / F 2 ≤ 7.2, 2.4 Continuous bulk polymerization under the condition of? V 1 / V 1 '? 3.0; When the contents of the reactor of the second reactor in the second reactor is V 2 , and the contents of the reaction solution in the second reactor are V 2 ′, 2.4 ≤ V 2 / V 2 '≤ 4.8, F = F 1 + F 2 Continuous bulk polymerization by continuously adding 2.0 to 2.5% by weight of a hydrocarbon compound on a final pellet basis under the condition of; The unreacted monomer is separated from the polymer produced from the second reactor and then cut into pellets. The average molecular weight is 18 to 250,000, the fluidity is 9.5 to 12.0, and the yellowness is 1.0 or less.
priorityDate 2001-12-26-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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