Direct epoxidation process using a mixed catalyst system
View Patent ↗Catalyst mixtures useful for the direct epoxidation of olefins are disclosed. The catalyst mixture comprises a titanium or vanadium zeolite and a supported catalyst comprising a noble metal, bismuth, and a carrier. The invention includes a process for producing an epoxide comprising reacting an olefin, hydrogen and oxygen in the presence of the catalyst mixture. The process results in significantly reduced alkane byproduct formed by the hydrogenation of olefin.
1. A process for producing an epoxide comprising reacting an olefin, hydrogen and oxygen in the presence of a titanium or vanadium zeolite and a supported catalyst comprising palladium, bismuth and a carrier.
2. The process of claim 1 wherein the titanium or vanadium zeolite is a titanium silicalite.
3. The process of claim 1 wherein the titanium zeolite is TS-1.
4. The process of claim 1 wherein the supported catalyst contains 0.01 to 10 weight percent palladium and 0.001 to 5 weight percent bismuth.
5. The process of claim 1 wherein the carrier is selected from the group consisting of carbon, titania, zirconia, niobia, silica, alumina, silica-alumina, tantalum oxide, molybdenum oxide, tungsten oxide, titania-silica, zirconia-silica, niobia-silica, and mixtures thereof.
6. The process of claim 1 wherein the olefin is a C 2 -C 6 olefin.
7. The process of claim 1 wherein the reaction is performed in the presence of a solvent selected from the group consisting of alcohols, ethers, esters, ketones, nitrites, water, liquid CO 2 , and mixtures thereof.
8. The process of claim 7 wherein the reaction is performed in the presence of a buffer.
9. A process for producing propylene oxide comprising reacting propylene, hydrogen and oxygen in a solvent in the presence of a titanium zeolite and a supported catalyst comprising palladium, bismuth and a carrier, wherein the supported catalyst contains 0.01 to 10 weight percent palladium and 0.001 to 5 weight percent bismuth.
10. The process of claim 9 wherein the titanium zeolite is a titanium silicalite.
11. The process of claim 9 wherein the carrier is selected from the group consisting of carbon, titania, zirconia, niobia, silica, alumina, silica-alumina, tantalum oxide, molybdenum oxide, tungsten oxide, titania-silica, zirconia-silica, niobia-silica, and mixtures thereof.
12. The process of claim 9 wherein the solvent is selected from the group consisting of alcohols, ethers, esters, ketones, nitrites, water, liquid CO 2 , and mixtures thereof.
13. The process of claim 12 wherein the reaction is performed in the presence of a buffer.
14. A catalyst mixture comprising a titanium or vanadium zeolite and a supported catalyst comprising palladium, bismuth, and a carrier.
15. The catalyst mixture of claim 14 wherein the titanium or vanadium zeolite is a titanium silicalite.
16. The catalyst mixture of claim 14 wherein the carrier is selected from the group consisting of carbon, titania, zirconia, niobia, silica, alumina, silica-alumina, tantalum oxide, molybdenum oxide, tungsten oxide, titania-silica, zirconia-silica, niobia-silica, and mixtures thereof.