GB996322A - Simultaneous recovery of pure ammonium sulphate and pure lactams from rearrangement mixtures of alicyclic ketoximes - Google Patents
Simultaneous recovery of pure ammonium sulphate and pure lactams from rearrangement mixtures of alicyclic ketoximesInfo
- Publication number
- GB996322A GB996322A GB1568962A GB1568962A GB996322A GB 996322 A GB996322 A GB 996322A GB 1568962 A GB1568962 A GB 1568962A GB 1568962 A GB1568962 A GB 1568962A GB 996322 A GB996322 A GB 996322A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ammonium sulphate
- lactam
- mother liquor
- weight
- amount
- 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
- C07D201/16—Separation or purification
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01C—AMMONIA; CYANOGEN; COMPOUNDS THEREOF
- C01C1/00—Ammonia; Compounds thereof
- C01C1/24—Sulfates of ammonium
- C01C1/242—Preparation from ammonia and sulfuric acid or sulfur trioxide
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Other In-Based Heterocyclic Compounds (AREA)
- Pyrrole Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for continuously recovering pure ammonium sulphate in the preparation of lactams (see Division C2) by Beckmann rearrangement of a cycloalkanone oxime having 6 to 10 ring carbon atoms with 98 to 100% wt. sulphuric acid or oleum containing up to 35% wt. of free sulphur trioxide, which reaction mixture contains 30 to 50% wt. lactam, followed by neutralizing said reaction mixture by contact with ammonia in the presence of 5 to 50 times the amount (with reference to the weight of reaction mixture) of 25 to 45% wt. ammonium sulphate solution, comprises separating the resulting lactam and ammonium sulphate phases, evaporating the ammonium sulphate phase until ammonium sulphate has been precipitated in an amount corresponding to the sulphuric acid in the rearrangement mixture, diluting the mother liquor with such an amount of water as is necessary to restore the ammonium sulphate solution to its original concentration, and returning the diluted mother liquor to the neutralization zone. Concentration of the ammonium sulphate fraction may be effected by evaporation under reduced pressure. Preferably 5 to 50 times the weight of mother liquor (with reference to the weight of rearrangement mixture) is returned to the neutralization zone.ALSO:A process for the recovery of pure lactams and pure ammonium sulphate from reaction mixtures obtained by Beckmann re-arrangement of a cycloalkanone oxime having 6 to 10 ring carbon atoms with 98 to 100% wt. sulphuric acid or oleum containing up to 35% wt. of free sulphur trioxide, which reaction mixture contains 30 to 50% wt. of lactam, comprises neutralizing said reaction mixtures by contact with ammonia in the presence of 5 to 50 times the amount (with reference to the weight of the reaction mixture) of 25 to 45% wt. ammonium sulphate solution, separating the resulting lactam and ammonium sulphate phases, evaporating the ammonium sulphate phase until ammonium sulphate has been precipitated in an amount corresponding to the sulphuric acid in the re-arrangement mixture, diluting the mother liquor with such an amount of water as is necessary to restore the ammonium sulphate solution to its original concentration, returning the diluted mother liquor to the neutralization zone, extracting the lactam phase with at least three times its weight of benzene, toluene or xylene, and distilling to obtain the lactam. Preferably 5 to 50 times the amount of mother liquor (with reference to the weight of re-arrangement mixture) is returned to the neutralization zone. Concentration of the ammonium sulphate solution may be effected by evaporation under reduced pressure. The lactam may be extracted by a countercurrent extraction in a one-stage or multi-stage process. In specific examples caprolactam and caprylolactam are produced from cyclohexanone oxine and cyclooctanone oxine respectively.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB62294A DE1194863B (en) | 1961-04-27 | 1961-04-27 | Process for the simultaneous production of pure ammonium sulfate and pure lactams from mixtures obtained by Beckmann rearrangement of cycloaliphatic ketoximes with sulfuric acid or oleum |
Publications (1)
Publication Number | Publication Date |
---|---|
GB996322A true GB996322A (en) | 1965-06-23 |
Family
ID=6973517
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1568962A Expired GB996322A (en) | 1961-04-27 | 1962-04-25 | Simultaneous recovery of pure ammonium sulphate and pure lactams from rearrangement mixtures of alicyclic ketoximes |
Country Status (4)
Country | Link |
---|---|
CH (1) | CH415640A (en) |
DE (1) | DE1194863B (en) |
GB (1) | GB996322A (en) |
NL (2) | NL141509B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0264126A2 (en) * | 1986-10-17 | 1988-04-20 | BASF Aktiengesellschaft | Process for the neutralisation of reaction mixtures obtained by the Beckmann rearangement of cyclohexanone oximes |
CN103896840A (en) * | 2012-12-28 | 2014-07-02 | 帝斯曼知识产权资产管理有限公司 | Method and equipment for continuously producing epsilon-caprolactam |
CN103896838A (en) * | 2012-12-28 | 2014-07-02 | 帝斯曼知识产权资产管理有限公司 | Method and equipment for continuously producing epsilon-hexanolactam |
WO2015010885A1 (en) * | 2013-07-26 | 2015-01-29 | Dsm Ip Assets B.V. | Continuous process for recovery of caprolactam and crystalline ammonium sulfate |
CN111408157A (en) * | 2020-04-14 | 2020-07-14 | 中石化南京工程有限公司 | Ammonium sulfate crystallization method and device thereof |
CN115093354A (en) * | 2022-06-29 | 2022-09-23 | 中国天辰工程有限公司 | Method for synthesizing caprolactam through Beckmann rearrangement reaction |
CN115367795A (en) * | 2022-09-01 | 2022-11-22 | 山东东佳集团股份有限公司 | Novel process for preparing ammonium sulfate by recycling catalyst titanium dioxide water washing liquid in acid making tail gas system |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4138472A (en) * | 1976-11-10 | 1979-02-06 | Basf Aktiengesellschaft | Process for obtaining coarsely crystalline pure ammonium sulfate |
DE2651195C3 (en) * | 1976-11-10 | 1985-01-31 | Basf Ag, 6700 Ludwigshafen | Process for the production of coarsely crystalline pure ammonium sulphate |
DE2926279A1 (en) * | 1979-06-29 | 1981-01-08 | Basf Ag | METHOD FOR CLEANING CAPROLACTAM |
DE4314281C1 (en) * | 1993-04-30 | 1995-01-19 | Leuna Werke Gmbh | Process for crystallising contaminated aqueous ammonium sulphate solutions |
DE4407222A1 (en) * | 1994-03-04 | 1995-09-07 | Basf Ag | Process for the recovery of caprolactam from oligo and / or polymers of caprolactam |
EP1092681A1 (en) * | 1999-10-13 | 2001-04-18 | Va Tech Wabag AG | Process for the neutralization of waste acids under simultaneous recovery of salt crystals |
CZ308473B6 (en) | 2018-11-27 | 2020-09-09 | Vysoká škola chemicko-technologická v Praze | Method for isolation of ɛ-caprolactam from the upper lactam phase |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE858701C (en) * | 1942-10-17 | 1952-12-08 | Basf Ag | Process for the cleavage of the lactam esters obtained in the rearrangement of oximes of cyclic ketones with sulfuric acid |
-
0
- NL NL277685D patent/NL277685A/xx unknown
-
1961
- 1961-04-27 DE DEB62294A patent/DE1194863B/en active Pending
-
1962
- 1962-04-25 GB GB1568962A patent/GB996322A/en not_active Expired
- 1962-04-25 CH CH498262A patent/CH415640A/en unknown
- 1962-04-26 NL NL277685A patent/NL141509B/en not_active IP Right Cessation
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0264126A3 (en) * | 1986-10-17 | 1988-06-22 | Basf Aktiengesellschaft | Process for the neutralisation of reaction mixtures obtained by the beckmann rearangement of cyclohexanone oximes |
US4806638A (en) * | 1986-10-17 | 1989-02-21 | Basf Aktiengesellschaft | Neutralization of reaction mixtures obtained by Beckman rearrangement of cyclohexanone oxime |
EP0264126A2 (en) * | 1986-10-17 | 1988-04-20 | BASF Aktiengesellschaft | Process for the neutralisation of reaction mixtures obtained by the Beckmann rearangement of cyclohexanone oximes |
CN103896838B (en) * | 2012-12-28 | 2018-03-23 | Cap Iii 有限公司 | The method and apparatus of continuous production ε caprolactams |
CN103896840A (en) * | 2012-12-28 | 2014-07-02 | 帝斯曼知识产权资产管理有限公司 | Method and equipment for continuously producing epsilon-caprolactam |
CN103896838A (en) * | 2012-12-28 | 2014-07-02 | 帝斯曼知识产权资产管理有限公司 | Method and equipment for continuously producing epsilon-hexanolactam |
CN103896840B (en) * | 2012-12-28 | 2018-06-05 | Cap Iii 有限公司 | The method and apparatus of continuous production epsilon-caprolactams |
CN105408313A (en) * | 2013-07-26 | 2016-03-16 | Capiii有限公司 | Continuous process for recovery of caprolactam and crystalline ammonium sulfate |
WO2015010885A1 (en) * | 2013-07-26 | 2015-01-29 | Dsm Ip Assets B.V. | Continuous process for recovery of caprolactam and crystalline ammonium sulfate |
CN105408313B (en) * | 2013-07-26 | 2018-11-09 | Cap Iii 有限公司 | A kind of continuation method of commercial scale recycling caprolactam and crystalline sulfuric acid ammonium |
CN111408157A (en) * | 2020-04-14 | 2020-07-14 | 中石化南京工程有限公司 | Ammonium sulfate crystallization method and device thereof |
CN115093354A (en) * | 2022-06-29 | 2022-09-23 | 中国天辰工程有限公司 | Method for synthesizing caprolactam through Beckmann rearrangement reaction |
CN115093354B (en) * | 2022-06-29 | 2024-01-16 | 中国天辰工程有限公司 | Method for synthesizing caprolactam through Beckmann rearrangement reaction |
CN115367795A (en) * | 2022-09-01 | 2022-11-22 | 山东东佳集团股份有限公司 | Novel process for preparing ammonium sulfate by recycling catalyst titanium dioxide water washing liquid in acid making tail gas system |
CN115367795B (en) * | 2022-09-01 | 2024-02-20 | 山东东佳集团股份有限公司 | Novel process for preparing ammonium sulfate by recycling catalyst titanium dioxide washing liquid in acid-making tail gas system |
Also Published As
Publication number | Publication date |
---|---|
NL277685A (en) | |
NL141509B (en) | 1974-03-15 |
CH415640A (en) | 1966-06-30 |
DE1194863B (en) | 1965-06-16 |
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