GB743736A - Phenol production - Google Patents
Phenol productionInfo
- Publication number
- GB743736A GB743736A GB1633253A GB1633253A GB743736A GB 743736 A GB743736 A GB 743736A GB 1633253 A GB1633253 A GB 1633253A GB 1633253 A GB1633253 A GB 1633253A GB 743736 A GB743736 A GB 743736A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mixture
- benzene
- toluene
- extracted
- sulphuric acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C39/00—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring
- C07C39/02—Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring monocyclic with no unsaturation outside the aromatic ring
- C07C39/08—Dihydroxy benzenes; Alkylated derivatives thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Resorcinol is obtained by decomposing m-diisopropylbenzene dihydroperoxide in a reaction solvent in the homogeneous phase and under substantially anhydrous conditions with a sulphuric acid catalyst, the solvent being a mixture of acetone with benzene, toluene, diisopropyl ether or a substantially water-insoluble ketone (such as methyl isobutyl ketone, cyclohexanone, 2-hexanone) or a mixture of two or more of these compounds. The amount of sulphuric acid may be 0.01 to 2 per cent by weight based on the volume of the decomposition reaction mixture and the temperature of reaction may be 20-130 DEG C. The dihydroperoxide may be used as a crude oxidation reaction mixture containing original hydrocarbon, or it may be extracted with aqueous alkali, the extract neutralized with carbon dioxide, and then extracted with benzene, toluene or methyl isobutyl ketone. Continuous and batch processes are described in the examples.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1633253A GB743736A (en) | 1953-06-13 | 1953-06-13 | Phenol production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1633253A GB743736A (en) | 1953-06-13 | 1953-06-13 | Phenol production |
Publications (1)
Publication Number | Publication Date |
---|---|
GB743736A true GB743736A (en) | 1956-01-25 |
Family
ID=10075381
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1633253A Expired GB743736A (en) | 1953-06-13 | 1953-06-13 | Phenol production |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB743736A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3190923A (en) * | 1959-07-13 | 1965-06-22 | Distillers Co Yeast Ltd | Process for the recovery of dihydroperoxide content from aqueous alkali extraction solution of dialkylated aromatic hydrocarbon oxidation reaction mixtures |
US3376352A (en) * | 1963-02-21 | 1968-04-02 | Montedison Spa | Process for producing hydroquinone from p-dialkyl-benzene-bis-hydroperoxides |
US4059637A (en) * | 1974-09-03 | 1977-11-22 | Sumitomo Chemical Company, Limited | Method for extraction of dihydroperoxide |
US4120902A (en) * | 1977-03-07 | 1978-10-17 | Phillips Petroleum Company | Oxidation product recovery |
EP0028931A1 (en) * | 1979-11-12 | 1981-05-20 | Mitsui Petrochemical Industries, Ltd. | Process for producing resorcinol |
EP1066233A1 (en) * | 1998-02-24 | 2001-01-10 | Indspec Chemical Corporation | Improved process for the production of a dihydroxybenzene and dicarbinol from diisopropylbenzene |
CN102471257A (en) * | 2009-08-19 | 2012-05-23 | 住友化学株式会社 | Method for handling aqueous solution containing water-soluble substance, method for manufacturing alkylbenzene hydroperoxides, and method for manufacturing hydroxybenzenes |
-
1953
- 1953-06-13 GB GB1633253A patent/GB743736A/en not_active Expired
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3190923A (en) * | 1959-07-13 | 1965-06-22 | Distillers Co Yeast Ltd | Process for the recovery of dihydroperoxide content from aqueous alkali extraction solution of dialkylated aromatic hydrocarbon oxidation reaction mixtures |
US3376352A (en) * | 1963-02-21 | 1968-04-02 | Montedison Spa | Process for producing hydroquinone from p-dialkyl-benzene-bis-hydroperoxides |
US4059637A (en) * | 1974-09-03 | 1977-11-22 | Sumitomo Chemical Company, Limited | Method for extraction of dihydroperoxide |
US4120902A (en) * | 1977-03-07 | 1978-10-17 | Phillips Petroleum Company | Oxidation product recovery |
EP0028931A1 (en) * | 1979-11-12 | 1981-05-20 | Mitsui Petrochemical Industries, Ltd. | Process for producing resorcinol |
US4339615A (en) * | 1979-11-12 | 1982-07-13 | Mitsui Petrochemical Industries Ltd. | Process for producing resorcinol |
EP1066233A1 (en) * | 1998-02-24 | 2001-01-10 | Indspec Chemical Corporation | Improved process for the production of a dihydroxybenzene and dicarbinol from diisopropylbenzene |
EP1066233A4 (en) * | 1998-02-24 | 2001-04-25 | Indspec Chemical Corp | Improved process for the production of a dihydroxybenzene and dicarbinol from diisopropylbenzene |
US6350921B1 (en) | 1998-02-24 | 2002-02-26 | Indspec Chemical Corporation | Process for the production of a dihydroxybenzene and dicarbinol from diisopropylbenzene |
CN102471257A (en) * | 2009-08-19 | 2012-05-23 | 住友化学株式会社 | Method for handling aqueous solution containing water-soluble substance, method for manufacturing alkylbenzene hydroperoxides, and method for manufacturing hydroxybenzenes |
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