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 | , , , |
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Format | Patent |
Language | English |
Published |
26.12.2002
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Edition | 7 |
Subjects | |
Online Access | Get full text |
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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%. |
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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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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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