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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D303-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D301-19
filingDate 1985-06-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1990-02-20-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fd03274b4592b55e8d999184b2fd984c
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_77e7bf235fe6086036b792b890ae2504
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_97af1c9e2fc61140a1696b964aec095c
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publicationDate 1990-02-20-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CA-1266053-A
titleOfInvention Epoxidation process using molybdenum catalysts
abstract IMPROVED EPOXIDATION PROCESS USING MOLYBDENUM CATALYSTS (D#80, 313-F) ABSTRACT OF THE DISCLOSURE A method of preparing an epoxide compound by re-acting an olefinically unsaturated compound with an organic hydroperoxide in the presence of a molybdenum catalyst is described. Selectivity to the epoxide is at least 96%, con-version of the hydroperoxide is at least 96%, yield to the epoxide is at least 94% and recovery of the catalyst is at least 90%. These excellent results are accomplished by using a molybdenum catalyst, such as a molybdenum complex of 2-ethyl-1-hexanol, at a concentration of 100 to 1000 ppm based on total charge, preferably 200 to 600 ppm. The mole ratio of olefinically unsaturated compound to organic hydro-peroxide is preferably in the range of 0.9:1 to 3.0:1 and the reaction temperature is preferably in the range of 50 to 180°C. It was further surprisingly discovered that the method of this invention works much better with t-butyl hydroperoxide as the organic hydroperoxide than with other hydroperoxides, such as cumene hydroperoxide.
priorityDate 1984-12-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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