GB762879A - Process for purifying lactams - Google Patents
Process for purifying lactamsInfo
- Publication number
- GB762879A GB762879A GB31303/53A GB3130353A GB762879A GB 762879 A GB762879 A GB 762879A GB 31303/53 A GB31303/53 A GB 31303/53A GB 3130353 A GB3130353 A GB 3130353A GB 762879 A GB762879 A GB 762879A
- Authority
- GB
- United Kingdom
- Prior art keywords
- lactam
- dowex
- solution
- aqueous solution
- per cent
- 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
- C07D—HETEROCYCLIC COMPOUNDS
- C07D201/00—Preparation, separation, purification or stabilisation of unsubstituted lactams
- C07D201/02—Preparation of lactams
- C07D201/08—Preparation of lactams from carboxylic acids or derivatives thereof, e.g. hydroxy carboxylic acids, lactones or nitriles
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D201/00—Preparation, separation, purification or stabilisation of unsubstituted lactams
- C07D201/16—Separation or purification
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Polyamides (AREA)
Abstract
A lactam is purified by passing the impure lactam in aqueous solution over both anion and cation exchangers. The anion and cation exchangers may be used in any order and they may also be used in the form of a mixed bed. Any non-ionogenic impurities which may be present may be removed by using a surfaceactive adsorption agent, e.g. activated carbon or a bleaching earth, in the form of a filter bed before or after passing the lactam solution through the ion exchangers. Suitable cation exchangers are those containing strongly acid groups such as sulphonated polymerization and polycondensation products, e.g. sulphonated polystyrene. Weaker cation exchange agents may also be used. Suitable anion exchange agents are quaternary ammonium bases of high molecular weight. The concentration of the aqueous lactam solution should preferably not exceed 30 per cent and the lactam may be recovered from the treated aqueous solution by evaporation preferably under reduced pressure. The non-ionogenic impurities present in the impure lactam may also be removed by previously subjecting a solution of the lactam in an inert organic solvent medium to an oxidizing treatment so as to oxidize the impurities selectively, e.g. by the process disclosed in Specification 757,406. In examples: (1) a 50 per cent aqueous solution of impure caprolactam is passed successively through a column filled with Dowex-50 and a column filled with Dowex-2 and the purified solution is then neutralized by passing through a pH correction filter and then evaporated to recover the purified lactam; (2) as in (1) except that the aqueous solution of the lactam is of 20 per cent concentration and the pH correction filter is stated to be Dowex-50; (3) a 20 per cent aqueous solution of impure caprolactam is passed successively through columns filled with Dowex-2, Dowex-50 and previously washed activated carbon and the purified solution then evaporated; (4) crude caprolactam is purified by passing a 20 per cent aqueous solution thereof through a column filled with a mixture of equal parts by volume of Dowex-2 and Dowex-50; (5) a 20 per cent solution in benzene of the lactam obtained by the Beckmann transformation of cyclohexanone oxime is boiled with a saturated aqueous solution of KMnO4 and after distilling off the water as an azeotrope with benzene the solution is filtered and extracted with water to give a 20 per cent aqueous solution of the lactam which is then passed successively through columns filled with activated carbon, Dowex-50, Dowex-2, and Dowex-50.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL762879X | 1952-11-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB762879A true GB762879A (en) | 1956-12-05 |
Family
ID=19827527
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB31303/53A Expired GB762879A (en) | 1952-11-15 | 1953-11-11 | Process for purifying lactams |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB762879A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2960499A (en) * | 1957-10-26 | 1960-11-15 | Stamicarbon | Preparing a lactam containing lactam oligomers |
WO2007099029A2 (en) * | 2006-02-24 | 2007-09-07 | Basf Aktiengesellschaft | Method for the purification of caprolactam made from lysin |
CN101781280A (en) * | 2010-03-11 | 2010-07-21 | 江苏爱利思达清泉化学有限公司 | Method for preparing color-stable epsilon-caprolactone |
WO2019228651A1 (en) | 2018-06-01 | 2019-12-05 | Uhde Inventa-Fischer Gmbh | Method for recycling extract water in the production of polyamide 6 |
-
1953
- 1953-11-11 GB GB31303/53A patent/GB762879A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2960499A (en) * | 1957-10-26 | 1960-11-15 | Stamicarbon | Preparing a lactam containing lactam oligomers |
WO2007099029A2 (en) * | 2006-02-24 | 2007-09-07 | Basf Aktiengesellschaft | Method for the purification of caprolactam made from lysin |
WO2007099029A3 (en) * | 2006-02-24 | 2007-10-25 | Basf Ag | Method for the purification of caprolactam made from lysin |
CN101781280A (en) * | 2010-03-11 | 2010-07-21 | 江苏爱利思达清泉化学有限公司 | Method for preparing color-stable epsilon-caprolactone |
WO2019228651A1 (en) | 2018-06-01 | 2019-12-05 | Uhde Inventa-Fischer Gmbh | Method for recycling extract water in the production of polyamide 6 |
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