GB555981A - A process of obtaining ª‡-and ª‰-methylnaphthalene and fractions enriched in either of these compounds - Google Patents
A process of obtaining ª‡-and ª‰-methylnaphthalene and fractions enriched in either of these compoundsInfo
- Publication number
- GB555981A GB555981A GB222342A GB222342A GB555981A GB 555981 A GB555981 A GB 555981A GB 222342 A GB222342 A GB 222342A GB 222342 A GB222342 A GB 222342A GB 555981 A GB555981 A GB 555981A
- Authority
- GB
- United Kingdom
- Prior art keywords
- isomer
- methyl naphthalene
- mixture
- methylnaphthalene
- product
- 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
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/17—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound with acids or sulfur oxides
- C07C7/171—Sulfuric acid or oleum
Abstract
555,981. Alpha and beta methylnaphthalene. COULSON, E. A. Feb. 19, 1942, No. 2223. [Class 2 (iii)] Alpha-methylnaphthalene is separated from a mixture of α- and #-methyl naphthalene or a mixture containing the two isomers such as tar oil by a process which comprises sulphonating the mixture to produce the monosulphonic acids of oc- and #-methylnaphthalene and selectively hydrolysing the mixture to desulphonate the greater part of the α-isomer, which is finally recovered. The selective hydrolysis is preferably carried out by heat, and the product recovered by steam distillation. After the separation of the α-isomer, further hydrolysis results in the isolation of the #-isomer. This may be still further purified by sulphonation followed by fractional crystallization from dilute sulphuric .acid. The preferred temperature for the hydrolysis of the α-isomer is at or below 124‹C., and for the #-isomer from 124‹- 150‹C. In examples, (1) A neutral tar fraction boiling between 232‹-240‹C. is treated with 98 per cent. sulphuric acid in the presence of silver sulphate at a temperature below 30‹C. The reaction mixture is poured on crushed ice and the aqueous layer separated from the unsulphonated oil. The aqueous layer is heated to boiling and steam passed through. The α- methyl naphthalene is thus distilled off. The residue is heated to 145‹-150‹C. and again steam-distilled to give a product predominating in #-methyl naphthalene. (2) The fraction rich in #-methyl naphthalene obtained in example (1) is again sulphonated as in example (1) and the product fractionally crystallized and finally desulphonated to give pure #-methyl naphthalene.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB222342A GB555981A (en) | 1942-02-19 | 1942-02-19 | A process of obtaining ª‡-and ª‰-methylnaphthalene and fractions enriched in either of these compounds |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB222342A GB555981A (en) | 1942-02-19 | 1942-02-19 | A process of obtaining ª‡-and ª‰-methylnaphthalene and fractions enriched in either of these compounds |
Publications (1)
Publication Number | Publication Date |
---|---|
GB555981A true GB555981A (en) | 1943-09-15 |
Family
ID=9735754
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB222342A Expired GB555981A (en) | 1942-02-19 | 1942-02-19 | A process of obtaining ª‡-and ª‰-methylnaphthalene and fractions enriched in either of these compounds |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB555981A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2583554A (en) * | 1950-02-09 | 1952-01-29 | Feldman Julian | Method for the separation of alpha-methyl naphthalene from beta-methyl naphthalene by azeotropic distillation |
US3270074A (en) * | 1963-02-05 | 1966-08-30 | Ashland Oil Inc | Process for the production of pure methylnaphthalene |
CN104628607A (en) * | 2015-02-16 | 2015-05-20 | 曲靖众一合成化工有限公司 | Continuous alpha-naphthalene sulfonic acid pressure hydrolysis method and device |
-
1942
- 1942-02-19 GB GB222342A patent/GB555981A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2583554A (en) * | 1950-02-09 | 1952-01-29 | Feldman Julian | Method for the separation of alpha-methyl naphthalene from beta-methyl naphthalene by azeotropic distillation |
US3270074A (en) * | 1963-02-05 | 1966-08-30 | Ashland Oil Inc | Process for the production of pure methylnaphthalene |
CN104628607A (en) * | 2015-02-16 | 2015-05-20 | 曲靖众一合成化工有限公司 | Continuous alpha-naphthalene sulfonic acid pressure hydrolysis method and device |
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