GB1109540A - Production of epsilon-caprolactam - Google Patents
Production of epsilon-caprolactamInfo
- Publication number
- GB1109540A GB1109540A GB58452/66A GB5845266A GB1109540A GB 1109540 A GB1109540 A GB 1109540A GB 58452/66 A GB58452/66 A GB 58452/66A GB 5845266 A GB5845266 A GB 5845266A GB 1109540 A GB1109540 A GB 1109540A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- copper
- metal
- caprolactam
- caprolactone
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Catalysts (AREA)
Abstract
Copper chromite, also referred to as copper chromium oxide, which may contain an optional third metal is prepared (a) by mixing aqueous solutions of ammonia, a cupric salt, a dichromate and optionally an additional metal salt and then thermally decomposing the resulting precipitate or (b) by reducing a mixture of the appropriate metal oxides with hydrogen. The molar ratio of copper to chromium in the compound is from 1 : 0.1 to 1 : 1.5 and of copper to the third metal is from 1 : 0.01 to 1 : 0.2. The compound may be shaped, e.g. into particles of 10 mesh size and is used as a catalyst in the conversion of e -caprolactone into e -caprolactam. A large number of optional metals is specified.ALSO:e -Caprolactam is prepared by reacting e -caprolactone with ammonia in the presence of hydrogen and a copper chromite catalyst, in the vapour phase. The addition of water to the reaction mixture, within the range 0 to 200 moles per mole of e -caprolactone, increases the life of the catalyst and the selectivity of e -caprolactam formation. Suitably the reaction is carried out at a temperature of 170 DEG to 300 DEG at a pressure of 0.5 to 3 atmospheres and with a partial pressure of hydrogen of 0.01 to 3 atmospheres. The molar ratio of copper to chromium in the catalyst is from 1:0.1 to 1:1.5 and the catalyst can include as an additional metal: calcium, strontium, magnesium, barium, zinc, cadmium, aluminium, gallium, titanium, germanium, tin, lead, vanadium antimony, bismuth, molybdenum, manganese, rhenium, iron, cobalt, nickel, ruthenium, rhodium, palladium, osmium, iridium and platinum.ALSO:A catalyst for the conversion of e -caprolactone to e -caprolactam comprises copper chromite which may contain a third metal and may be used alone or on a carrier e.g. kieselguhr, silica gel, alumina or pumice. The preparation and shaping of these catalysts are described. The molar ratio of copper to chromium in the catalyst is from 1:0.1 to 1:1.5 and the third metal may be: calcium, strontium, magnesium, barium, zinc, cadmium, aluminium, gallium, titanium, germanium, tin, lead, vanadium, antimony, bismuth, molybdenum, manganese, rhenium, iron, cobalt, nickel, ruthenium, rhodium, palladium, osmium, iridium and platinum.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB58452/66A GB1109540A (en) | 1966-12-30 | 1966-12-30 | Production of epsilon-caprolactam |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB58452/66A GB1109540A (en) | 1966-12-30 | 1966-12-30 | Production of epsilon-caprolactam |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1109540A true GB1109540A (en) | 1968-04-10 |
Family
ID=10481654
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB58452/66A Expired GB1109540A (en) | 1966-12-30 | 1966-12-30 | Production of epsilon-caprolactam |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1109540A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1993016042A1 (en) * | 1992-02-07 | 1993-08-19 | Akzo N.V. | Process for producing pyrrolidone and n-alkyl pyrrolidones |
CN112337470A (en) * | 2019-08-07 | 2021-02-09 | 中国石油化工股份有限公司 | Catalyst for preparing organic amine through fatty carboxylic ester amination reaction and preparation method and application thereof |
-
1966
- 1966-12-30 GB GB58452/66A patent/GB1109540A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1993016042A1 (en) * | 1992-02-07 | 1993-08-19 | Akzo N.V. | Process for producing pyrrolidone and n-alkyl pyrrolidones |
US5478950A (en) * | 1992-02-07 | 1995-12-26 | Akzo Nobel N.V. | Process for producing pyrrolidone and N-alkyl pyrrolidones |
CN112337470A (en) * | 2019-08-07 | 2021-02-09 | 中国石油化工股份有限公司 | Catalyst for preparing organic amine through fatty carboxylic ester amination reaction and preparation method and application thereof |
CN112337470B (en) * | 2019-08-07 | 2023-08-15 | 中国石油化工股份有限公司 | Catalyst for preparing organic amine by amination reaction of fatty carboxylic ester, preparation method and application thereof |
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