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http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-20
filingDate 1998-09-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dff45a32561835a77f9fb7b8b18deac9
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4962c26f5352643cc77583d6746650f5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3c394f3cae996d3d663ec009ee547664
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_586ec4b633df1c44f03136bca89f773d
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publicationDate 2000-04-11-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber JP-2000103803-A
titleOfInvention Method for producing vinyl chloride polymer
abstract PROBLEM TO BE SOLVED: To provide a vinyl chloride polymer having a high bulk specific gravity, a sharp particle size distribution, a sharp pore size distribution in particles, and suitable for high-speed extrusion molding with high productivity, and Stable production. SOLUTION: A polymerization vessel having an internal volume of 100 m 3 or more provided with a stirrer, an outer jacket and a reflux condenser is used. Under polymerization conditions in which the amount of heat removed by the reflux condenser during polymerization is 30% or more of the total amount of heat removed and the polymerization time is within 6 hours, the vinyl chloride-based monomer is added in the presence of an oil-soluble polymerization initiator. In suspension polymerization in an aqueous medium, a predetermined dispersion stabilizer is used, a predetermined amount of acid or oxygen is present in the polymerization system, and the initial droplet diameter is controlled to 40 to 80 μm.
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