US2007149814A1PendingUtilityA1
Method for the production of amines
Est. expiryOct 17, 2023(expired)· nominal 20-yr term from priority
Inventors:Frederik Van LaarEkkehard SchwabSteffen OehlenschlägerHartwig VossWolfgang MackenrothKonrad MorgenschweisUlrich PenzelBernd Weidner
B01J 37/03B01J 37/14B01J 21/18B01J 37/18B01J 23/892C07C 209/36C07C 211/51B01J 23/89
47
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Claims
Abstract
The present invention provides a process for hydrogenating aromatic nitro compounds to the corresponding amines in the presence of hydrogenation catalysts, which comprises using hydrogenation catalysts in which nickel and platinum are present on a support in the form of an alloy having an atomic ratio of nickel to platinum in the alloy of between 30:70 and 70:30.
Claims
exact text as granted — not AI-modified1 . A process for hydrogenating aromatic nitro compounds to the corresponding amines in the presence of hydrogenation catalysts, which comprises using hydrogenation catalysts in which nickel and platinum are present on a support in the form of an alloy having an atomic ratio of nickel to platinum in the alloy of between 30:70 and 70:30.
2 . The process according to claim 1 , wherein the aromatic nitro compound used is dinitrotoluene.
3 . The process according to claim 1 , wherein the atomic ratio of nickel to platinum in the alloy is between 40:60 and 60:40.
4 . The process according to claim 1 , wherein the atomic ratio of nickel to platinum in the alloy is between 45:55 and 55:45.
5 . The process according to claim 1 , wherein the catalyst is used in an amount of from 0.01 to 10% by weight, based on the reaction mixture.
6 . The process according to claim 1 , wherein the catalyst is used in an amount of from 0.1 to 5% by weight, based on the reaction mixture.
7 . The process according to claim 1 , wherein the catalyst is used in an amount of from 0.2 to 2% by weight, based on the reaction mixture.
8 . The process according to claim 1 , wherein the hydrogenation is carried out at a temperature in the range from 80 to 250° C.
9 . The process according to claim 1 , wherein the catalyst used is used at its loading limit.
10 . A catalyst which comprises nickel and platinum on a support in the form of an alloy having an atomic ratio of nickel to platinum in the alloy of between 40:60 and 60:40, wherein the support is selected from the group comprising activated carbon, carbon black and graphite.
11 . The use of catalysts according to claim 10 for hydrogenating dinitrotoluene.Cited by (0)
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