US4014933A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of amines from alcohols
Assignee: BASF SE
•
Filing: 1973-08-27
•
Granted: 1977-03-29
•
Expires: 1993-08-27
Abstract
Abstract An improved method of preparing amines by reaction of alcohols with ammonia or primary or secondary amines at elevated temperature and superatmospheric pressure in the presence of hydrogen and a hydrogenation catalyst containing cobalt, nickel and copper, the improvement comprising using a catalyst which contains (calculated on the metal content of the catalyst) from 70 to 95% by weight of a mixture of cobalt and nickel and from 5 to 30% by weight of copper, the ratio by weight of cobalt to nickel being from 4:1 to 1:4. The amines prepared in this way are suitable for the production of emulsifying agents, plant protection agents and vulcanization accelerators.
Inventors
- 👤 Guenther Boettger
- 👤 Hubert Corr
- 👤 Herwig Hoffmann
- 👤 Herbert Toussaint
- 👤 Siegfried Winderl
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 19:17
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J27/195; B01J27/198; B01J23/00; B01J23/70; B01J23/72; B01J23/74; B01J23/755; B01J23/76; B01J23/89; B01J23/8933; B01J27/185; B01J27/1853; B01J27/188; B01J23/90
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
239 words
In a process for the production of an amine by reacting an alkanol having one to eighteen carbon atoms; or a cycloalkanol having five to twelve carbon atoms; or an alkanolamine selected from the group consisting of ethanolamine, propanolamine, isopropanolamine, and hexanolamine; or a polyalcohol selected from the group consisting of diethanolamine, diisopropanolamine, ethylene glycol, propylene glycol, butanediol, pentanediol, hexanediol, 4,4'-bishydroxycyclohexyl-propane-(2,2); or a glycol ether selected from the group consisting of methyl glycol, ethyl glycol and butyl glycol; or and a polyalkylene glycol ether selected from the group consisting of polyethylene glycol ether, polypropylene glycol ether, and polybutylene glycol ether, with ammonia or a primary or a secondary amine, the ammonia or amine being present in an excess of from 5 to 50 moles over the stoichiometric amount of alcohol in the presence of hydrogen and a cobalt, nickel and copper-containing aluminum oxide or silicon dioxide supported catalyst at a temperature of from 100° to 200° C and at a pressure of from 10 to 250 atmospheres, the improvement which consists essentially of using a supported catalyst containing, based on the metal content of the catalyst, from 70 to 95% by weight of a mixture of cobalt and nickel and from 5 to 30% by weight of copper, the ratio by weight of cobalt to nickel being from 4:1 to 1:4, the metal content of the catalyst being from 5 to 80% by weight, based on the whole catalyst.
Claim 2
Dependent Claim
239 words
In a process for the production of an amine by reacting an alkanol having one to eighteen carbon atoms; or a cycloalkanol having five to twelve carbon atoms; or an alkanolamine selected from the group consisting of ethanolamine, propanolamine, isopropanolamine, and hexanolamine; or a polyalcohol selected from the group consisting of diethanolamine, diisopropanolamine, ethylene glycol, propylene glycol, butanediol, pentanediol, hexanediol, 4,4'-bishydroxycyclohexyl-propane-(2,2); or a glycol ether selected from the group consisting of methyl glycol, ethyl glycol and butyl glycol; or and a polyalkylene glycol ether selected from the group consisting of polyethylene glycol ether, polypropylene glycol ether, and polybutylene glycol ether, with ammonia or a primary or a secondary amine, the ammonia or amine being present in an excess of from 5 to 50 moles over the stoichiometric amount of alcohol in the presence of hydrogen and a cobalt, nickel and copper-containing aluminum oxide or silicon dioxide supported catalyst at a temperature of from 100° to 200° C and at a pressure of from 10 to 250 atmospheres, the improvement which consists essentially of using a supported catalyst containing, based on the metal content of the catalyst, from 70 to 95% by weight of a mixture of cobalt and nickel and from 5 to 30% by weight of copper, the ratio by weight of cobalt to nickel being from 4:1 to 1:4, the metal content of the catalyst being from 5 to 80% by weight, based on the whole catalyst.
Claim 3
Dependent Claim
27 words
A process as set forth in claim 1, wherein the metal content of the catalyst is from 10 to 30% by weight, based on the whole catalyst.
Claim 4
Dependent Claim
23 words
A process as set forth in claim 1, wherein from 5 to 100 liters of hydrogen is used for each mole of alcohol.
Claim 5
Dependent Claim
55 words
A process as set forth in claim 1 wherein the catalyst additionally contains, besides cobalt and nickel, one or two of the metals manganese, chromium, zinc, vanadium and silver, and also sodium, potassium, calcium or barium in a ratio by weight of from 1:200 to 1:10 with reference to the mixture of cobalt and nickel.
Claim 6
Dependent Claim
21 words
A process as set forth in claim 1 wherein a catalyst is used which also contains phosphoric acid or boric acid.
Claim 7
Dependent Claim
54 words
A process as set forth in claim 1 wherein the ratio by weight of cobalt to nickel is from 2:1 to 1:2, and in which the metal content of the catalyst is from 80 to 90% by weight of a mixture of cobalt and nickel and from 10 to 20% by weight of copper.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-28 | 1980-09-27 | 1981-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-28 | 1984-09-27 | 1985-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-28 | 1988-09-27 | 1989-03-29 | $7700.00 | Window Closed / Lapsed |