METHOD FOR PRODUCING PHENOL

PROBLEM TO BE SOLVED: To provide a method for producing phenol and α-methylstyrene in high yield while suppressing the formation of a cumylphenol, a methylstyrene dimer and a high-boiling point compound in the method for producing the phenol by a cumene-method. SOLUTION: This method for producing th...

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Main Authors TAKAI TOSHIHIRO, KATO YOJI, KOKUBU YOSHIMITSU, DOI KENJI
Format Patent
LanguageEnglish
Published 26.12.2002
Edition7
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Abstract PROBLEM TO BE SOLVED: To provide a method for producing phenol and α-methylstyrene in high yield while suppressing the formation of a cumylphenol, a methylstyrene dimer and a high-boiling point compound in the method for producing the phenol by a cumene-method. SOLUTION: This method for producing the phenol is characterized in that an oxidation product of the cumene is washed by bringing the oxidation product into contact with at least 5 wt.% or more of water based on the amount of the oxidation product of the cumene fed to a reactor, subjecting the washed product to an oil-water separation, removing the water from the separated oil phase so that the content may be <=1 wt.%, feeding the water-removed product to a reactor, and reacting the fed product at 55-90 deg.C reaction temperature while keeping acetone concentration in the reaction mixture so as to be 20-70 wt.% until the conversion of cumene hydroperoxide becomes 95-99.9%.
AbstractList PROBLEM TO BE SOLVED: To provide a method for producing phenol and α-methylstyrene in high yield while suppressing the formation of a cumylphenol, a methylstyrene dimer and a high-boiling point compound in the method for producing the phenol by a cumene-method. SOLUTION: This method for producing the phenol is characterized in that an oxidation product of the cumene is washed by bringing the oxidation product into contact with at least 5 wt.% or more of water based on the amount of the oxidation product of the cumene fed to a reactor, subjecting the washed product to an oil-water separation, removing the water from the separated oil phase so that the content may be <=1 wt.%, feeding the water-removed product to a reactor, and reacting the fed product at 55-90 deg.C reaction temperature while keeping acetone concentration in the reaction mixture so as to be 20-70 wt.% until the conversion of cumene hydroperoxide becomes 95-99.9%.
Author TAKAI TOSHIHIRO
KATO YOJI
KOKUBU YOSHIMITSU
DOI KENJI
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Snippet PROBLEM TO BE SOLVED: To provide a method for producing phenol and α-methylstyrene in high yield while suppressing the formation of a cumylphenol, a...
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SourceType Open Access Repository
SubjectTerms ACYCLIC OR CARBOCYCLIC COMPOUNDS
APPARATUS THEREFOR
CHEMISTRY
CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS
GENERAL METHODS OF ORGANIC CHEMISTRY
GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS
METALLURGY
ORGANIC CHEMISTRY
TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
Title METHOD FOR PRODUCING PHENOL
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