Catalyst preparation
View Patent ↗The invention relates to a process for the preparation of an epoxidation catalyst which process involves (a) drying a silica gel carrier having a weight average particle size of from 0.1 mm to 2 mm at a temperature of from more than 200° C. to 300° C., and (b) contacting the carrier obtained in step (a) with a gas stream containing titanium halide to obtain an impregnated carrier, and the use of such catalyst in the preparation of alkylene oxide.
1. A process for the preparation of an epoxidation catalyst which process comprises:
(a) drying a silica gel carrier, comprising silicon, having a weight average particle size of from 0.1 mm to 2 mm, at a temperature of from more than 200° C. to 300° C.; and,
(b) contacting the carrier obtained in step (a) with a gas stream comprising titanium halide to obtain an impregnated carrier, wherein said sillica gel carrier has a surface area of at most 1,000 m 2 /g.
2. The process of claim 1 , wherein the drying of step (a) is performed at a temperature which is higher than the temperature at which the impregnation of step (b) is performed.
3. The process of claim 1 , wherein the amount of titanium halide supplied in step (b) is such that the molar ratio of titanium halide added to silicon present in the carrier is from 0.050 to 0.063.
4. The process of claim 1 , wherein the gas stream consists of titanium halide.
5. The process of claim 1 , in which process the silica gel carrier has a surface area of at most 500 m 2 /g.
6. The process of claim 1 , wherein the silica gel carrier is dried for a period of time of from 1 hour to 8 hours.
7. The process of claim 1 , further comprising:
(c) calcining the impregnated carrier to obtain a calcined impregnated carrier; and,
(d) hydrolyzing the calcined impregnated carrier.
8. The process of claim 7 further comprising:
(e) contacting the carrier obtained in step (d) with a silylating agent.
9. The process of claim 8 , wherein the drying of step (a) is performed at a temperature which is higher than the temperature at which the impregnation of step (b) is performed.
10. The process of claim 8 , wherein the amount of titanium halide supplied in step (b) is such that the molar ratio of titanium halide added to silicon present in the carrier is from 0.050 to 0.063.
11. The process of claim 8 , wherein the gas stream consists of titanium halide.
12. The process of claim 8 , wherein the silica gel carrier has a surface area of at most 500 m 2 /g.
13. The process of claim 8 , wherein the silica gel carrier is dried for a period of time of from 1 hour to 8 hours.
14. The process of claim 8 , wherein the calcining of step (c) is performed at a temperature of at least 500° C.
15. The process of claim 8 , wherein the hydrolyzing of step (d) is performed at a temperature in the range of from 150° C. to 400° C.
16. The process of claim 8 , wherein the silylating agent comprises hexamethyldisilazane.
17. A process for the preparation of an alkylene oxide which process comprises:
contacting a hydroperoxide and an alkene with a heterogeneous epoxidation catalyst; and,
withdrawing a product stream comprising an alkylene oxide and an alcohol and/or water, wherein the catalyst was prepared according to a process comprising:
(a) drying a silica gel carrier, comprising silicon, having a weight average particle size of from 0.1 mm to 2 mm, at a temperature of from more than 200° C. to 300° C.; and,
(b) contacting the carrier obtained in step (a) with a gas stream comprising titanium halide to obtain an impregnated carrier, wherin said sillica gel carrier has a surface area of at most 1,000 m 2 /g.
18. The process of claim 8 , wherein the alkene comprises propene and the alkylene oxide comprises propylene oxide.
19. The process of claim 8 , wherein the hydroperoxide comprises ethylbenzene hydrogen peroxide and in which the alcohol comprises 1-phenyl ethanol.
20. The process of claim 10 , further comprising dehydrating 1-phenylethanol to obtain styrene.