GB586439A - Improvements in or relating to the production of benzene hexachloride isomers - Google Patents
Improvements in or relating to the production of benzene hexachloride isomersInfo
- Publication number
- GB586439A GB586439A GB614544A GB614544A GB586439A GB 586439 A GB586439 A GB 586439A GB 614544 A GB614544 A GB 614544A GB 614544 A GB614544 A GB 614544A GB 586439 A GB586439 A GB 586439A
- Authority
- GB
- United Kingdom
- Prior art keywords
- isomer
- solvent
- per cent
- benzene
- solids
- 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
- C07C23/00—Compounds containing at least one halogen atom bound to a ring other than a six-membered aromatic ring
- C07C23/02—Monocyclic halogenated hydrocarbons
- C07C23/10—Monocyclic halogenated hydrocarbons with a six-membered ring
- C07C23/12—Hexachlorocyclohexanes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/38—Separation; Purification; Stabilisation; Use of additives
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
To obtain from crude benzene hexachloride a composition containing an enhanced proportion of g -isomer to a -isomer, the material (obtainable by chlorinating benzene at ordinary or elevated temperature, while irradiating actinically, discontinuing the chlorination while unchanged benzene is still present and flashing off unchanged benzene with hot water) is treated with an aliphatic solvent therefor, other than methanol or ethanol, or with a cyclo-aliphatic solvent therefor containing a 6-carbon ring, the solvent being in such amount as to dissolve the g -isomer leaving a substantial proportion of the g -isomer undissolved, and if desired the solvent is then removed from the solution. Advantageously the composition is recovered from the extract as a precipitate by adding thereto a liquid which has a low solvent power for the g -isomer and which is miscible with the solvent. The aliphatic solvent may be a normally liquid chlorinated aliphatic hydrocarbon, e.g. chloroform, carbon tetrachloride, cis-dichloroethylene, trans-dichloroethylene, trichloroethylene, perchloroethylene, ethylidene chloride, ethylene dichloride, isobutyl chloride; or an esters of an aliphatic carboxylic acid, e.g. methyl acetate, ethyl acetate, n-butyl acetate, methyl trichloroacetate, methyl dichloroacetate, methyl propionate; and in either case the mixture of isomers may be recovered from the extract by mixing the latter with a pentane or a petrol ether fraction. The cycloaliphatic solvent may be cyclohexane, cyclohexene, cyclohexanol, cyclohexanone or decahydronaphthalene. Other specified solvents are: hydrocarbons: diesel oil, odourless distillate, kerosene, n-pentane, petrol ether, "white oil"; miscellaneous: diethyl carbonate, glacial acetic acid, acetone, acetonitrile, n-butyl bromide, diacetone alcohol, dimethyl acetal, ethyl ether, paraldehyde, carbon disulphide. In examples: (1) crude benzene hexachloride containing 12 per cent g -isomer and 70 per cent a -isomer (obtained by chlorinating benzene at 50 DEG C. under actinic radiations until a 20 per cent solution of the hexachlorides in benzene is formed and flashing off the excess benzene) is stirred with cyclohexane to obtain a solution containing 18 parts of solids of which 66 per cent are the g -isomer and from which the solvent is removed by evaporation; (2)-(6), crude benzene hexachloride, obtained as in (1), is: (2) deodorised by the method of Specification 586,464 and the product stirred with decahydronaphthalene to obtain a solution containing 18 parts of solids of which 66 per cent are the g -isomer; (3) stirred with tri-chloroethylene to obtain a solution containing 15 parts of solids of which 33 per cent are the g -isomer and the solvent is removed by evaporation; (4) refluxed with chloroform to obtain a solution containing substantially all the g -isomer, and the solution is concentrated to obtain the solid product; (5) stirred with glacial acetic acid to obtain a solution containing 23 parts of solids of which 21 per cent are g -isomer and the solids are precipitated by diluting with a large volume of water; (6) stirred with methyl acetate to form a slurry containing solid a -isomer, which is filtered and the filtrate is evaporated to obtain a solid containing 42 per cent of g -isomer. Specifications 573,689 and 573,693 also are referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB614544A GB586439A (en) | 1944-04-03 | 1944-04-03 | Improvements in or relating to the production of benzene hexachloride isomers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB614544A GB586439A (en) | 1944-04-03 | 1944-04-03 | Improvements in or relating to the production of benzene hexachloride isomers |
Publications (1)
Publication Number | Publication Date |
---|---|
GB586439A true GB586439A (en) | 1947-03-19 |
Family
ID=9809228
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB614544A Expired GB586439A (en) | 1944-04-03 | 1944-04-03 | Improvements in or relating to the production of benzene hexachloride isomers |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB586439A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE930389C (en) * | 1951-05-27 | 1955-07-14 | F Raschig G M B H Dr | Process for the production of pure ª † -hexachlorocyclohexane from hexachlorocyclohexane isomer mixtures |
DE934230C (en) * | 1951-06-19 | 1955-11-17 | Armour & Co | Process for the separation of deoxycholic acid from a cholic acid-deoxycholic acid mixture |
DE937348C (en) * | 1950-11-14 | 1956-01-05 | Hans Dipl-Chem Bremer | Process for the purification of technical hexachlorocyclohexane |
DE942508C (en) * | 1952-03-29 | 1956-05-03 | Basf Ag | Process for the production of pure ª † -hezachlorocyclohexane |
DE942393C (en) * | 1952-01-24 | 1956-05-03 | F Raschig G M B H Dr | Process for the production of pure ª † -hexachlorocyclohexane from hexachlorocyclohexane isomer mixtures, which in addition to mainly ª ‡ -hexachlorocyclohexane contain more than about 40% ª † -hexachlorocyclohexane |
-
1944
- 1944-04-03 GB GB614544A patent/GB586439A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE937348C (en) * | 1950-11-14 | 1956-01-05 | Hans Dipl-Chem Bremer | Process for the purification of technical hexachlorocyclohexane |
DE930389C (en) * | 1951-05-27 | 1955-07-14 | F Raschig G M B H Dr | Process for the production of pure ª † -hexachlorocyclohexane from hexachlorocyclohexane isomer mixtures |
DE934230C (en) * | 1951-06-19 | 1955-11-17 | Armour & Co | Process for the separation of deoxycholic acid from a cholic acid-deoxycholic acid mixture |
DE942393C (en) * | 1952-01-24 | 1956-05-03 | F Raschig G M B H Dr | Process for the production of pure ª † -hexachlorocyclohexane from hexachlorocyclohexane isomer mixtures, which in addition to mainly ª ‡ -hexachlorocyclohexane contain more than about 40% ª † -hexachlorocyclohexane |
DE942508C (en) * | 1952-03-29 | 1956-05-03 | Basf Ag | Process for the production of pure ª † -hezachlorocyclohexane |
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