Method of regeneration of titanium-containing molecular sieve catalyst
View Patent ↗Disclosed herein is a method of regenerating a titanium-containing molecular sieve catalyst. Particularly, this invention provides a method of regenerating a titanium-containing molecular sieve catalyst used in epoxidation of olefin through simple treatment using a mixture solvent comprising aqueous hydrogen peroxide and alcohol. According to the method of this invention, when the catalyst having decreased activity is regenerated, the activity of the regenerated catalyst is equal to that of new catalyst and can be maintained stable for a long period of time.
1. A method of regenerating a titanium-containing molecular sieve catalyst, comprising:
i) pretreating the titanium-containing molecular sieve catalyst, which has been used in epoxidation of an olefin compound and thus inactivated, with water or alcohol, thus washing residual reaction materials and impurities; and
ii) passing through the pretreated catalyst a mixture solution comprising hydrogen peroxide, water, and alcohol, thus regenerating the catalyst under the condition of a temperature of 60˜200° C. and a pressure of 5˜50 atm, wherein the hydrogen peroxide in the mixture solution has a concentration of 0.1˜40 wt% and the water and alcohol in the mixture solution have a volume ratio of 1:10˜10:1.
2. The method according to claim 1 , further comprising washing the regenerated catalyst with water or alcohol and then drying it, after regenerating the catalyst in ii).
3. The method according to claim 1 , wherein the alcohol is selected from the group consisting of C1˜C10 alcohols.
4. The method according to claim 3 , wherein the alcohol is methanol, ethanol, propanol, or butanol.
5. The method according to claim 1 , wherein the titanium-containing molecular sieve catalyst is a titanium-containing molecular sieve catalyst including silicalite.
6. The method according to claim 5 , wherein the titanium-containing molecular sieve catalyst including silicalite is represented by Formula I below and has an MFI or MEL crystal structure:
x TiO 2 (1 −x )SiO 2 Formula I
wherein x is 0.001˜0.05.
7. The method according to claim 1 , wherein regenerating the catalyst in ii) is conducted at a flow rate of 0.1˜10 cc/min for 1-48 hours.
8. The method according to claim 1 , wherein regenerating the catalyst in ii) is conducted by passing the mixture solution through a catalyst bed under conditions of a temperature of 120˜150° C. and a pressure of 530 atm.
9. The method according to claim 1 , wherein, in a case where the epoxidation is conducted in, a continuous manner, pretreating the catalyst is conducted by introducing water or alcohol into a continuous reactor at a flow rate of 0.1˜10 cc/min under conditions of a temperature of 0˜60° C. and a pressure ranging from atmospheric pressure to 100 atm, and regenerating the catalyst is conducted by passing the mixture solution through a catalyst bed in the continuous reactor at a flow rate of 0.1˜10 cc/min in a temperature range of 25˜200° C.