GB873676A - Manufacture of resorcinol - Google Patents
Manufacture of resorcinolInfo
- Publication number
- GB873676A GB873676A GB25568/58A GB2556858A GB873676A GB 873676 A GB873676 A GB 873676A GB 25568/58 A GB25568/58 A GB 25568/58A GB 2556858 A GB2556858 A GB 2556858A GB 873676 A GB873676 A GB 873676A
- Authority
- GB
- United Kingdom
- Prior art keywords
- resorcinol
- meta
- cleavage
- removal
- free
- 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
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/68—Purification; separation; Use of additives, e.g. for stabilisation
- C07C37/70—Purification; separation; Use of additives, e.g. for stabilisation by physical treatment
- C07C37/74—Purification; separation; Use of additives, e.g. for stabilisation by physical treatment by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for the manufacture of resorcinol by the catalytic cleavage of a reaction mixture containing meta-diisopropyl benzene dihydroperoxide derived from the oxidation of meta-diisopropyl benzene, comprises heat-decomposing the material contained in the cleavage reaction product which is less volatile than resorcinol while passing steam through said material, simultaneously distilling off the additional quantities of resorcinol and meta-isopropenyl phenol so formed, separating any oil phase from the aqueous distillate and subjecting the latter to flash distillation to obtain an overhead fraction containing water and meta-isopropenyl phenol and a substantially anhydrous residue fraction containing resorcinol substantially free from metaisopropenyl phenol. The heat treatment may be carried out after removal or neutralisation of the catalyst employed in the cleavage reaction and after removal of acetone, unchanged hydrocarbons and free resorcinol or concurrently with the distillation of the cleavage reaction product without prior removal of any of the free resorcinol. Superheated steam is preferably employed in the process. The distillate from the thermal decomposition is preferably maintained at a pH of at least 4. The flash distillation conditions specified range from a pressure of about 50 mm. at a wall temperature of about 170 DEG C. up to atmospheric pressure at a wall temperature of about 210 DEG C. An example is furnished in which resorcinol is recovered from the crude aqueous solution obtained by the acid catalysed cleavage of meta-diisopropylbenzene dihydroperoxide. Specification 857,113 also is referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB25568/58A GB873676A (en) | 1958-08-08 | 1958-08-08 | Manufacture of resorcinol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB25568/58A GB873676A (en) | 1958-08-08 | 1958-08-08 | Manufacture of resorcinol |
Publications (1)
Publication Number | Publication Date |
---|---|
GB873676A true GB873676A (en) | 1961-07-26 |
Family
ID=10229799
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25568/58A Expired GB873676A (en) | 1958-08-08 | 1958-08-08 | Manufacture of resorcinol |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB873676A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4283567A (en) * | 1978-12-20 | 1981-08-11 | Mitsui Petrochemical Industries Ltd. | Method for recovering resorcinol |
US4339614A (en) * | 1980-03-14 | 1982-07-13 | Pcuk Produits Chimiques Ugine Kuhlmann | Superacid catalyzed preparation of resorcinol from meta-isopropylphenol |
US4420376A (en) * | 1982-08-23 | 1983-12-13 | The Goodyear Tire & Rubber Company | Separation of resorcinol from non-extractable impurities |
-
1958
- 1958-08-08 GB GB25568/58A patent/GB873676A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4283567A (en) * | 1978-12-20 | 1981-08-11 | Mitsui Petrochemical Industries Ltd. | Method for recovering resorcinol |
US4339614A (en) * | 1980-03-14 | 1982-07-13 | Pcuk Produits Chimiques Ugine Kuhlmann | Superacid catalyzed preparation of resorcinol from meta-isopropylphenol |
US4420376A (en) * | 1982-08-23 | 1983-12-13 | The Goodyear Tire & Rubber Company | Separation of resorcinol from non-extractable impurities |
EP0102314A2 (en) * | 1982-08-23 | 1984-03-07 | The Goodyear Tire & Rubber Company | Separation of resorcinol from non-extractable impurities |
EP0102314A3 (en) * | 1982-08-23 | 1985-10-30 | The Goodyear Tire & Rubber Company | Separation of resorcinol from non-extractable impurities |
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