http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2007204680-A

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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G65-10
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filingDate 2006-02-03-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7c5c62e1062280312ad4efc3bab2a1f6
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publicationDate 2007-08-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber JP-2007204680-A
titleOfInvention Method for producing polyether polyol
abstract The present invention provides a process for producing a high molecular weight polyether polyol (PEP) having a narrow molecular weight distribution even when copolymerized with ethylene oxide (EO), hardly clouding at room temperature, and excellent fluidity. In a reactor, a mixture of an alkylene oxide (AO) having 3 or more carbon atoms and EO is supplied to a polyether polyol initiator in the presence of a double metal cyanide complex catalyst. In the production method of PEP in which an external block chain is formed in the initiator by performing a polymerization reaction, As an initiator, PEP having an average number of functional groups per molecule of 1 to 8, a hydroxyl value of 18 to 200 mgKOH / g, and A% of terminal hydroxyl groups being primary hydroxyl groups is used. The relationship between the ratio of EO (E mol%) in the total mixture of AO and EO with 3 or more carbon atoms fed into the reactor (E mol%) and the primary hydroxyl group ratio (A%) of the initiator is (EA) The ratio of EO is maintained to be <40, and a mixture of AO and EO is supplied to carry out the copolymerization reaction so that the ratio of the initiator to the total mass of the obtained PEP is 3 to 60% by mass. [Selection figure] None
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2011136367-A1
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http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2012111813-A
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