Selective liquid phase oxidation of toluene to benzaldehyde

Abstract

The present invention provides an improved process for the liquid phase oxidation of toluene to benzaldehyde with high selectivity and good activity in an organic acid medium using a catalyst system consisting of transition metal/metals and bromide as a promoter in the presence of lean oxygen.

1 . A process for the preparation of benzaldehyde comprising: 
 (i) subjecting toluene to liquid phase oxidation in a reaction mixture comprising: 
 (a) an organic solvent;  
 (b) a catalyst system comprising at least one transition metal and a bromide promoter; and  
 (c) diluted oxygen, wherein the concentration of oxygen is in the range from 1 to 10% of the reaction mixture,  
   (ii) cooling the reaction mixture to room temperature and    (iii) separating the benzaldehyde.    
     
     
         2 . The process as claimed in  claim 1  wherein the benzaldehyde is separated by distillation.  
     
     
         3 . The process as claimed in  claim 1  wherein the transitional metal is selected from the group consisting of manganese, chromium, iron, vanadium, cobalt, molybdenum, and a combination thereof.  
     
     
         4 . The process as claimed in  claim 3  wherein the transition metal catalyst comprises a combination of manganese and iron.  
     
     
         5 . The process as claimed in  claim 4  wherein the mole ratio of manganese to iron is in the range from 0.1 to 10.  
     
     
         6 . The process as claimed in  claim 5  wherein the mole ratio of manganese to iron is in the range from 0.2 to 5.0.  
     
     
         7 . The process as claimed in  claim 1  wherein the transitional metal is a salt selected from the group consisting of acetates, bromides, carbonates, fluoride, iodides, chlorides, nitrates, sulfates and vanadates.  
     
     
         8 . The process as claimed in  claim 7  wherein the transitional metal is a salt selected from the group consisting of acetates, chlorides and vanadates.  
     
     
         9 . The process as claimed in  claim 1  wherein the bromide promoter is selected from the group consisting of sodium bromide, hydrogen bromide and zinc bromide.  
     
     
         10 . The process as claimed in  claim 1  wherein the bromide promoter comprises sodium bromide.  
     
     
         11 . The process as claimed in  claim 3  wherein the concentration of manganese with respect to toluene is in the range of 0.1-7 mol %.  
     
     
         12 . The process as claimed in  claim 3  wherein the concentration of manganese with respect to toluene is in the range of 0.3-5.0 mol %.  
     
     
         13 . The process as claimed in  claim 3  wherein the concentration of iron with respect to toluene is in the range of 0.1-5 mol %.  
     
     
         14 . The process as claimed in  claim 3  wherein the concentration of iron with respect to toluene is in the range of 0.3-4.0 mol %.  
     
     
         15 . The process as claimed in  claim 3  wherein the concentration of bromine with respect to toluene is in the range of 0.05-5.0 mol. %.  
     
     
         16 . The process as claimed in  claim 3  wherein the concentration of bromine with respect to toluene is in the range of 0.1-3.0 mol %.  
     
     
         17 . The process as claimed in  claim 1  wherein the organic solvent is selected from the group consisting of an aliphatic acid and an aromatic organic acid, or a combination thereof.  
     
     
         18 . The process as claimed in  claim 1  wherein the organic solvent is selected from the group consisting of acetic acid, benzoic acid and propionic acid.  
     
     
         19 . The process as claimed in  claim 1  wherein the organic solvent comprises acetic acid.  
     
     
         20 . (canceled)  
     
     
         21 . The process as claimed in  claim 1  wherein the concentration of oxygen is in the range of 2-7% in nitrogen.  
     
     
         22 . The process as claimed in  claim 1  wherein the reaction is carried out at a temperature in the range of 70°-180° C. and pressure in the range of 1-80 bar.  
     
     
         23 . The process as claimed in  claim 1  wherein the reaction is carried out at a temperature in the range of 90°-160° C. and pressure in the range of 20-70 bar.  
     
     
         24 . The process as claimed in  claim 1  wherein the selectivity to benzaldehyde obtained is in the range of 60-75% and benzoic acid and benzyl alcohol are obtained as side products.  
     
     
         25 . The process as claimed in  claim 3  wherein the transition metal catalyst comprises a combination of manganese and vanadium.  
     
     
         26 . The process as claimed in  claim 25  wherein the mole ratio of manganese to vanadium is in the range from 0.1 to 10.  
     
     
         27 . The process as claimed in  claim 26  wherein the mole ratio of manganese to vanadium is in the range from 0.2 to 5.0.  
     
     
         28 . The process as claimed in  claim 3  wherein the concentration of vanadium with respect to toluene is in the range of 0.1-5 mol %.  
     
     
         29 . The process as claimed in  claim 3  wherein the concentration vanadium with respect to toluene is in the range of 0.3-4.0 mol %.