Catalyst for the oxidative esterification of aldehydes to carboxylic esters

Abstract

The present invention relates to a novel process for oxidative esterification, generally for reaction of aldehydes with alcohols in the presence of oxygenous gases directly to give the corresponding ester in the presence of a heterogeneous catalyst, by means of which, for example, (meth)acrolein can be converted to methyl (meth)acrylate. The new catalyst has titanium dioxide as the main component of the support material. The catalysts are especially notable for high mechanical and chemical stability and for good catalytic performance even over very long periods. The process is an improvement in the catalyst service life, activity and selectivity over prior art catalysts which lose activity and/or selectivity relatively quickly in continuous operation in media having even a small water content.

1 . A process for preparing a carboxylic ester from an aldehyde, the process comprising:
 continuously conducting an oxidative esterification of the aldehyde to the carboxylic ester via heterogeneous catalysis in a liquid phase in the presence of a catalyst particle,   wherein   the particle consists of 0.1% to 3% by weight of gold, 25% to 99.8% by weight of TiO 2 , 0% to 50% by weight of silicon oxide, 0% to 25% by weight of Al 2 O 3 , 0% to 25% by weight of at least one oxide of an alkali metal, an alkaline earth metal, a rare earth metal, and zirconium, 0% to 20% by weight of at least one oxide selected from the group consisting of an iron oxide, a zinc oxide, a nickel oxide, and a cobalt oxide, and 0% to 5% by weight of at least one other component;   gold, optionally together with the iron oxide, zinc oxide, nickel oxide, and/or cobalt oxide, is bound to the catalyst particle in the form of particles having an average diameter between 2 and 10 nm; and   the catalyst particle has an average geometric equivalent diameter between 5 μm and 10 mm.   
     
     
         2 . The process according to  claim 1 , wherein the catalyst particle consists of 0.3% to 2.5% by weight of gold, 50% to 99.5% by weight of TiO 2 , 0% to 20% by weight of the silicon oxide, 0% to 10% by weight of the at least one oxide selected from the group consisting of an iron oxide, a zinc oxide, a nickel oxide, and a cobalt oxide, and 0% to 5% by weight of the at least one other component. 
     
     
         3 . The process according to  claim 1 , wherein the catalyst particle consists of 0.3% to 2.5% by weight of gold, 96% to 99.5% by weight of TiO 2  and not more than 3.7% by weight of other components. 
     
     
         4 . The process according to  claim 1 , wherein the particles having an average diameter between 2 and 10 nm, which contain gold and optionally the iron oxide, zinc oxide, nickel oxide, and/or cobalt oxide, are present in an outer region of the catalyst particle. 
     
     
         5 . The process according to  claim 1 , wherein the particles having an average diameter between 2 and 10 nm, which contain gold and optionally the iron oxide, zinc oxide, nickel oxide, and/or cobalt oxide, are distributed homogeneously across the catalyst particle. 
     
     
         6 . The process according to  claim 1 , wherein the catalyst particles are porous and have a specific surface area between 20 and 300 m 2 /g and an average pore diameter of 2 to 30 nm. 
     
     
         7 . The process according to  claim 6 , wherein the specific surface area of the catalyst particles is between 30 and 200 m 2 /g, and the average pore diameter is 5 to 25 nm. 
     
     
         8 . The process according to  claim 1 , wherein the oxidative esterification is conducted in the presence of oxygen and an alcohol. 
     
     
         9 . The process according to  claim 8 , wherein the aldehyde is methacrolein and the carboxylic ester is an alkyl methacrylate. 
     
     
         10 . The process according to  claim 9 , wherein
 the alcohol is methanol;   methacrolein continuously reacts with methanol in the presence of an oxygenous gas at a reaction temperature between 40-120° C., an absolute pressure between 1 and 20 bar, and with a slurry density of the catalyst, which is being stirred and swirled in a steady-state product mixture comprising MMA, methacrolein, methanol and water, between 1% and 20% by weight; and   methacrolein is not fully converted in at least one reactor in each case, but after a partial conversion between 20% and 95% is separated continuously from the catalyst via filtration and fed to the workup.   
     
     
         11 . The process according to  claim 10 , wherein air is supplied continuously to the reactor as the oxygenous gas and an oxygen content of gas phase that forms the reaction mixture is between 2% and 8% by volume. 
     
     
         12 . The process according to  claim 10 , wherein the reaction is conducted at a reaction temperature between 50° C. and 100° C. at an absolute pressure between 2 and 15 bar. 
     
     
         13 . The process according to  claim 10 , wherein the slurry density of the catalyst is between 2% and 15% by weight. 
     
     
         14 . The process according to  claim 10 , wherein methacrolein is not fully converted in one reactor in each case or multiple reactors connected in series, but after a partial conversion between 40% and 80% is separated continuously from the catalyst via filtration and fed to the workup.