Direct epoxidation process
View Patent ↗A process is disclosed for reacting an olefin, hydrogen, and oxygen in a reactor in the presence of a catalyst comprising a transition metal zeolite and a noble metal to produce a reaction mixture comprising an epoxide and acidic byproducts. A portion of the reaction mixture is contacted with an adsorbent so that a treated mixture having a reduced amount of byproducts is produced. The treated mixture is recycled back to the reactor. Including an adsorption step should improve the catalyst productivity and epoxide selectivity.
1. An epoxidation process comprising:
(a) reacting an olefin, hydrogen, and oxygen in the presence of an epoxidation catalyst comprising a transition metal zeolite and a noble metal to produce a reaction mixture comprising an epoxide and acidic byproducts;
(b) contacting a portion of the reaction mixture with an adsorbent to produce a treated mixture having a reduced amount of acidic byproducts; and
(c) recycling the treated mixture to step (a).
2. The process of claim 1 wherein the noble metal is supported on the transition metal zeolite.
3. The process of claim 2 wherein the noble metal is selected from the group consisting of palladium, platinum, gold, rhenium, silver, and mixtures thereof.
4. The process of claim 2 wherein the transition metal zeolite is a titanium zeolite.
5. The process of claim 1 wherein the noble metal is supported on a carrier.
6. The process of claim 5 wherein the carrier is selected from the group consisting of carbons, titanias, zirconias, niobias, silicas, aluminas, silica-aluminas, titania-silicas, zirconia-silicas, niobia-silicas, ion-exchange resins, and mixtures thereof.
7. The process of claim 5 wherein the transition metal zeolite is a titanium zeolite.
8. The process of claim 5 wherein the noble metal is selected from the group consisting of palladium, platinum, gold, rhenium, silver, and mixtures thereof.
9. The process of claim 1 wherein the epoxidation reaction is performed in the presence of a solvent.
10. The process of claim 9 wherein the solvent is selected from the group consisting of alcohols, ethers, esters, ketones, carbon dioxide, water, and mixtures thereof.
11. The process of claim 1 wherein the adsorbent is selected from the group consisting of basic ion-exchange resins, aluminas, calcium oxide, magnesium oxide, activated carbons, and mixtures thereof.
12. The process of claim 1 wherein the adsorbent is a basic ion-exchange resin.
13. The process of claim 1 wherein the adsorbent is in a fixed-bed.
14. The process of claim 1 wherein the adsorbent is in a slurry.
15. The process of claim 1 wherein step (b) is performed in continuous flow mode.
16. The process of claim 1 wherein step (b) is performed in batch mode.
17. The process of claim 1 wherein the adsorbent is regenerated on-line.
18. The process of claim 1 wherein the adsorbent is in multiple adsorption vessels.
19. The process of claim 1 wherein the olefin is propylene.
20. The process of claim 19 wherein the adsorbent is a basic ion-exchange resin.