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US3255248A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalytic hydrogenation of organic nitrogenous carbon compounds to amines

Assignee: BASF SE
•
Filing: 1962-12-18
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Granted: 1966-06-07
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Expires: 1982-12-18
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Abstract

Abstract A process for the hydrogenation of aromatic amino compounds and acyclic and carbocyclic compounds containing nitrogenous groups reducible to amino groups, wherein a hydrogenation of an aromatic ring to give a cycloaliphatic ring and a reduction of a nitrogenous group to give an amino group is achieved, comprises carrying out the hydrogenation in the absence of sulphur at a temperature between 40 DEG C. and 250 DEG C. under a pressure between 20 and 600 atmospheres in the liquid phase in the presence of at least one metal hydrogenation catalyst, the catalytic activity of which is impaired by sulphur, the catalyst having been sintered prior to the hydrogenation. The catalyst may contain, for example, silver, manganese, copper, iron, cobalt or nickel and may be prepared by sintering the oxide at 800 DEG C.-1,400 DEG C. and heating the sintered oxide with hydrogen at 250 DEG C.-600 DEG C. The catalyst may be supported on a carrier and promotors may be added. Aromatic amines may be hydrogenated at 200 DEG C.-250 DEG C. to give cycloaliphatic amines and other nitrogenous compounds containing, for example, nitro, nitroso, isonitroso and cyano groups may be hydrogenated at 60 DEG C.-150 DEG C. to give amino compounds. Other substituents such as aldehyde groups which are reduced and carboxylic, halogen, amino and alkoxy groups which are not reduced may also be present in the reactants. A list of suitable reactants is given. In the examples, ethylene diamine, cyclohexylamine, tolylene diamine, dimethyl hydrazine and isopropylamine are prepared.ALSO:Oxides of silver, manganese, copper, iron, cobalt or nickel are converted to the metal by sintering the oxide by heating for example, to a temperature within 20-60 DEG C. of the melting point and reducing the sintered oxide with a stream of hydrogen. Mixtures of metal oxides may be reduced after sintering to give alloys and in examples alloys of cobalt and aluminium and cobalt, nickel and aluminium are prepared.

Inventors

  • 👤 Suessenguth Hermann
  • 👤 Corr Hubert
  • 👤 Simon Walter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 01:33
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/16; B01J37/18; B01J23/00; B01J23/16; B01J23/32; B01J23/34; B01J23/38; B01J23/48; B01J23/50; B01J23/70; B01J37/08; B01J37/12; B01J37/14; C; C07; C07C; C07C209/00; C07C209/30; C07C209/32; C07C209/36; C07C209/38; C07C209/44; C07C209/48; C07C209/68; C07C209/70; C07C209/72; C07C211/00; C07C211/01; C07C211/02; C07C211/03; C07C211/06; C07C211/09; C07C211/10; C07C211/33; C07C211/34; C07C211/35; C07C211/43; C07C211/44; C07C211/49; C07C211/50; C07C211/51; C07C241/00; C07C241/02; C07C243/00; C07C243/10; C07C243/12; C07C243/14; C07C2601/00; C07C2601/12; C07C2601/14

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 162 words
A PROCESS FOR THE HYDROGENATION OF A NITROGENOUSLY SUBSTITUTED HDYROCARBON SELECGED FROM THE CLASS CONSISTING OF (A) A HYDROCARBON OF 1 TO 12 CARBON ATOMS SUBSTITUTED SOLELY BY A NITROGENOUS RADICAL SELECTED FROM THE GROUP CONSISTING OF NIRTO, N-NITROSO, ISONITROSO, CYANO AND ARYL NUCLEARLY SUBSTITUTED AMINO, AND (B) A HYDROCARON OF 1 TO 12 CARBON ATOMS SUBSTITUTED SOLELY BY SAID NITROGENOUS RADICAL AND BY AN ADDITIONAL SUBSTITUENT SELECTED FROM THE GROUP CONSISTING OF HYDROXY, ALKOXY OF 1 TO 4 CARBON ATOMS AND ALKYL SUBSTITUTED AMINO, WHICH PROCESS COMPRISES: PREPARING A SINTERED CATALYST BY HEATING A MATERIAL SELECTED FROM TEH CLASS CONSISTING OF COBALT, NICKEL AND THE OXIDES OF THESE METALS TO A TEMPERATURE OF AT LEAST 1000*C. TO A TEMPERATURE ABOUT 20*C. BELOW THE MELTING POINT OF THE HEATED MATERIAL; AND HYDROGENATING SAID NITROGENOUSLY SUBSTITUTED HDYROCARBON IN LIQUID PHASE AT A TEMPERATURE BETWEEN 40*C. AND 250*C., AT A PRESSURE BETWEEN 20 AND 500 ATMOSPHERES AND IN THE PRESENCE OF SAID SINTERED CATALYST.
Claim 2
Dependent Claim 162 words
A PROCESS FOR THE HYDROGENATION OF A NITROGENOUSLY SUBSTITUTED HDYROCARBON SELECGED FROM THE CLASS CONSISTING OF (A) A HYDROCARBON OF 1 TO 12 CARBON ATOMS SUBSTITUTED SOLELY BY A NITROGENOUS RADICAL SELECTED FROM THE GROUP CONSISTING OF NIRTO, N-NITROSO, ISONITROSO, CYANO AND ARYL NUCLEARLY SUBSTITUTED AMINO, AND (B) A HYDROCARON OF 1 TO 12 CARBON ATOMS SUBSTITUTED SOLELY BY SAID NITROGENOUS RADICAL AND BY AN ADDITIONAL SUBSTITUENT SELECTED FROM THE GROUP CONSISTING OF HYDROXY, ALKOXY OF 1 TO 4 CARBON ATOMS AND ALKYL SUBSTITUTED AMINO, WHICH PROCESS COMPRISES: PREPARING A SINTERED CATALYST BY HEATING A MATERIAL SELECTED FROM TEH CLASS CONSISTING OF COBALT, NICKEL AND THE OXIDES OF THESE METALS TO A TEMPERATURE OF AT LEAST 1000*C. TO A TEMPERATURE ABOUT 20*C. BELOW THE MELTING POINT OF THE HEATED MATERIAL; AND HYDROGENATING SAID NITROGENOUSLY SUBSTITUTED HDYROCARBON IN LIQUID PHASE AT A TEMPERATURE BETWEEN 40*C. AND 250*C., AT A PRESSURE BETWEEN 20 AND 500 ATMOSPHERES AND IN THE PRESENCE OF SAID SINTERED CATALYST.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1969-06-06 1969-12-06 1970-06-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1973-06-06 1973-12-06 1974-06-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1977-06-06 1977-12-06 1978-06-07 $7700.00 Window Closed / Lapsed

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