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filingDate 2015-11-06-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6886cafdf30c878266808ec52e9d2f3d
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publicationDate 2017-07-05-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20170077249-A
titleOfInvention Process for the production of cyclohexanone from phenol
abstract The present invention relates to an industrial scale continuous process for the production and recovery of cyclohexanone from phenol and hydrogen, comprising hydrogenating phenol in a phenol hydrogenation reactor; And separating the cyclohexanone from the hydrogenated product stream in a separation and purification section [II] comprising at least four distillation sections; At least a portion of the reaction heat generated in the phenol hydrogenation reaction section [I] is applied to the production of steam; The molar ratio of cyclohexanone to phenol charged to the phenol hydrogenation reactor is 0.02 to 0.10 and / or; The molar ratio of cyclohexanol to phenol charged to the phenol hydrogenation reactor is from 0.001 to 0.10.
priorityDate 2014-11-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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