US2010099550A1PendingUtilityA1

Homogeneous Process for the Hydrogenation of Carboxylic Acids and Derivatives Thereof

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Assignee: DAVY PROCESS TECHN LTDPriority: May 2, 2002Filed: Aug 24, 2009Published: Apr 22, 2010
Est. expiryMay 2, 2022(expired)· nominal 20-yr term from priority
B01J 2531/842B01J 2531/96C07C 29/149B01J 2531/825B01J 31/4023Y02P20/52B01J 2531/0258B01J 31/4053B01J 2231/641B01J 31/24B01J 31/2409B01J 2531/822C07C 27/04Y02P20/584B01J 2531/824B01J 2531/821B01J 31/4046B01J 31/40
57
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Claims

Abstract

A homogenous process for the hydrogenation of the carboxylic acids and/or derivatives thereof in the presence of a catalyst comprising ruthenium, rhodium, iron, osmium or palladium, and an organic phosphine is described in which the hydrogenation is carried out in the presence of at least about 1% by weight water. A process for regenerating a catalyst comprising ruthenium, rhodium, iron, osmium or palladium and an organic phosphine is also described in which the regeneration is carried out in the presence of hydrogen and water.

Claims

exact text as granted — not AI-modified
1 . A homogeneous process for the hydrogenation of carboxylic acids and/or derivatives thereof in the presence of a catalyst comprising:
 (a) ruthenium, rhodium, iron, osmium or palladium; and   (b) an organic phosphine;   wherein the hydrogenation is carried out in the presence of more than 1% by weight water.   
   
   
       2 . A homogeneous process according to  claim 1  wherein the carboxylic acids and/or derivatives thereof are present as solvent. 
   
   
       3 . A homogeneous process according to  claim 1  wherein a solvent is present and the water is present as an additive therein. 
   
   
       4 . A homogeneous process according to  claim 3  wherein the water is present in an amount of more than 1% to the solubility limit of the water in the solvent. 
   
   
       5 . A homogeneous process according to  claim 3  wherein the water is present in an amount greater than the solubility limit of the water in the solvent and the excess water forms an aqueous phase. 
   
   
       6 . A homogeneous process according to  claim 1  wherein water is generated in situ. 
   
   
       7 . A homogeneous process according to  claim 2  wherein the product of the reaction forms the solvent. 
   
   
       8 . A homogeneous process according to  claim 1  wherein the water is a solvent for the reaction. 
   
   
       9 . A homogeneous process according to  claim 1  wherein the catalyst is a ruthenium/phosphine catalyst system 
   
   
       10 . A homogeneous process according to  claim 9  wherein the phosphine component of the catalyst system is a tridentate phosphine. 
   
   
       11 . A homogeneous process according to  claim 9  wherein the phosphine component of the catalyst system is tris-1,1,1-(diphenyl-phosphinomethyl)ethane. 
   
   
       12 . A homogeneous process according to  claim 1  wherein the reaction is carried out in the absence of a promotor for the catalyst. 
   
   
       13 . A homogeneous process according to  claim 1  wherein the reaction is carried out in the absence of halide. 
   
   
       14 . A homogeneous process according to  claim 1  wherein the reaction temperature is in the range of from about 150° C. to about 350° C. 
   
   
       15 . A homogeneous process according to  claim 1  wherein the reaction pressure is in the range of from about 250 psig to about 2000 psig. 
   
   
       16 . A homogeneous process according to  claim 10  wherein the pressure is from about 800 psig to about 1200 psig. 
   
   
       17 . A homogeneous process according to  claim 1  wherein the catalyst is regenerated in the presence of the water and hydrogen. 
   
   
       18 . A process for regenerating a catalyst comprising:
 (a) ruthenium, rhodium, iron, osmium or palladium; and   (b) an organic phosphine;   
     wherein the regeneration is carried out in the presence of hydrogen and water. 
   
   
       19 . A process according to  claim 18  wherein the regeneration is carried out at a temperature of from about 150° C. to about 350° C.

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