Process for producing propylene oxide using a pretreated epoxidation catalyst
View Patent ↗A process for preparing propylene oxide by epoxidizing propylene with an oxidant in the presence of a pretreated catalyst; wherein the catalyst comprises an activated titanium silicalite with MFI structure (TS-1) catalyst; and wherein the catalyst has been activated by pretreatment with methanol to form the pretreated catalyst. The pretreated TS-1 catalyst may be used in the epoxidizing propylene reaction with no additional methanol added; and the pretreated catalyst has equivalent activity to TS-1 catalyst used with large excesses of methanol.
1. A process for preparing propylene oxide comprising epoxidizing propylene with an oxidant in the presence of a pretreated titanium-containing zeolite catalyst with MFI structure where no methanol is added as a solvent to the process; wherein the pretreated catalyst comprises an activated titanium silicalite with MFI structure (TS-1) catalyst comprising a pretreated titanium-containing zeolite catalyst being pretreated with methanol at a mole ratio of methanol to TS-1 catalyst from 0.1:1 methanol:TS-1 catalyst to 100:1 methanol:TS-1 catalyst at a temperature of from about −20° C. to about 60° C. for about 1 minute to about 24 hours and air dried at a temperature of below 65° C. prior to employing the TS-1 catalyst in the propylene epoxidation reaction.
2. The process of claim 1 , wherein at least a portion of the methanol is chemically bound to the TS-1 catalyst; and wherein the fraction of titanium that is chemically bonded with methanol in titanium silicalite-1 comprises from about 50% to about 200%.
3. The process of claim 1 , wherein said pretreated catalyst is in the form of a solid activated catalyst separate from excess methanol and wherein said pretreated catalyst maintains its reactivity in an oxidation reaction.
4. The process of claim 1 , wherein the oxidant comprises a peroxide compound.
5. The process of claim 1 , wherein the oxidant comprises hydrogen peroxide.
6. The process of claim 1 , wherein the pretreating with methanol is carried out at a temperature of from about 0° C. to about 60° C.
7. The process of claim 1 , including the step of separating the excess methanol from the pretreated catalyst.
8. The process of claim 7 , wherein the separating step comprises filtering, centrifuging or evaporating.