Process for vapor phase hydrogenation
A process for selective formation of ethanol from acetic acid includes contacting a feed stream containing acetic acid and hydrogen at an elevated temperature with catalyst comprising platinum and tin on a high surface area silica promoted with calcium metasilicate. Selectivities to ethanol of over 85% are achieved at 280° C. with catalyst life in the hundreds of hours.
1. A process for hydrogenating alkanoic acids comprising passing a gaseous stream comprising hydrogen and an alkanoic acid in the vapor phase over a hydrogenation catalyst comprising:
a main metal selected from the group consisting of platinum, palladium, rhenium and mixtures thereof on a support selected from the group consisting of iron oxide, alumina, titania, zirconia, magnesium oxide, carbon, graphite and mixtures thereof; and
a metallic promoter selected the group consisting of tin, rhenium and mixtures thereof, the support being promoted with a redox promoter selected from the group consisting of: WO 3 ; MoO 3 ; Fe 2 O 3 and Cr 2 O 3 .
2. The process of claim 1 , wherein the main metal is rhenium.
3. The process of claim 1 , wherein at least 80% of the acetic acid converted is converted to ethanol and wherein less than 4% of the acetic acid is converted to compounds other than compounds selected from the group consisting of ethanol, ethyl acetate, acetaldehyde, ethylene, diethyl ether and mixtures thereof.
4. The process of claim 1 , wherein the main metal may be present from 0.1 to 10% by weight.
5. The process of claim 1 , wherein the process is conducted at a temperature from 225° C. and 300° C. and wherein the molar ratio of hydrogen to acetic acid is at least 4:1.
6. The process of claim 1 , wherein the process is conducted in a reactor selected from the group consisting of a fixed bed reactor, a fluid bed reactor and an ebullient bed reactor.