Preparation method for propylene epoxidation catalyst, and application thereof

Patent metadata

Field	Value
Publication number	US-11291985-B2
Application number	US-201816646828-A
Country	US
Kind code	B2
Filing date	Jun 14, 2018
Priority date	Oct 27, 2017
Publication date	Apr 5, 2022
Grant date	Apr 5, 2022

Abstract

A preparation method for a propylene epoxidation catalyst: pre-hydrolyzing a silicon source, adding a titanium source and reacting to form a sol, atomizing the sol and then spraying it into liquid ammonia for molding, implementing pore broadening, and performing drying, calcination, and silanization treatment to obtain a Ti—SiO2 composite oxide catalyst. The present catalyst can be used in the chemical process of preparing propylene oxide by epoxidation of propylene, the average propylene oxide selectivity being up to 97.5%, having prospects for industrial application.

First claim

The invention claimed is:

1. A preparation method for a propylene epoxidation catalyst, comprising the following steps:
(1) pre-hydrolysis of silicon source: dissolving a silicon ester in a lower alcohol, adding a hydrolysis catalyst and water to react to obtain liquid A;
(2) sol formation: dissolving a titanium ester in a lower alcohol and adding the obtained system to liquid A; adding water or adding a mixed aqueous solution of NH 4 ReO 4 and a zinc salt to react to obtain a sol;
(3) atomizing the sol obtained in step (2) and spraying the atomized sol into liquid ammonia to obtain a catalyst precursor;
(4) carrying out a pore broadening treatment to the catalyst precursor obtained in step (3);
(5) drying and calcining the pore broadened catalyst precursor in step (4);
(6) carrying out a silanization treatment to the product obtained in step (5).

2. The method according to claim 1 , wherein the silicon ester in step (1) is selected from the group consisting of tetraethyl orthosilicate, tetramethyl orthosilicate, tetrapropyl orthosilicate and tetrabutyl orthosilicate and combinations thereof.

3. The method according to claim 1 , wherein the hydrolysis catalyst in step (1) is one of acetic acid and formic acid or a mixture thereof.

4. The method according to claim 3 , wherein, in step (1), the hydrolysis catalyst is added in an amount that is 0.8-1.5 wt % of the silicon ester; water is added in an amount that is the amount of water theoretically required to hydrolyze 30-80 wt % of the silicon ester;
the reaction temperature in step (1) is 40-70° C., and the reaction time is 1-3 h.

5. The method according to claim 1 , wherein the titanium ester used in step (2) is selected from the group consisting of tetramethyl titanate, tetraethyl titanate, tetrapropyl titanate, tetraisopropyl titanate, tetrabutyl titanate and tetraisobutyl titanate and combinations thereof.

6. The method according to claim 5 , wherein, based on the weight of SiO 2 corresponding to SiO 2 from the complete hydrolysis of the raw silicon ester in step (1), the amount of Ti in the titanium ester used in step (2) is 2-5% of the weight of SiO 2 ;
in step (2), the concentration of the titanium ester in the lower alcohol is 30-50 wt %;
the reaction time in step (2) is 1˜4 h.

7. The method according claim 1 , wherein in step (2), the molar ratio of Re in the used NH 4 ReO 4 to Ti in the used titanium ester is 0.01-0.05:1, and the molar ratio of Zn in the used zinc salt to Ti in the used titanium ester is 0.05-0.15:1.

8. The method according to claim 7 , wherein in step (2), if water is added for the reaction to form a sol, water is added in an amount that is the amount of water required for theoretical complete hydrolysis of the unhydrolyzed silicone ester in step (1) and the titanium ester in step (2);
in step (2), if the mixed aqueous solution of NH 4 ReO 4 and a zinc salt is added for the reaction to form a sol, the amount of water contained in the mixed aqueous solution of NH 4 ReO 4 and a zinc salt is the amount of water required for theoretical complete hydrolysis of the unhydrolyzed silicone ester in step (1) and the titanium ester in step (2).

9. The method according to claim 7 , wherein a pore broadening agent used in step (4) for performing the pore broadening treatment is liquid ammonia.

10. The method according to claim 9 , wherein the process conditions for the pore broadening treatment in step (4) include: the pore broadening temperature is 60-140° C., and the pore broadening time is 3-15 h.

11. The method according to claim 1 , wherein in step (2), if water is added for the reaction to form a sol, water is added in an amount that is the amount of water required for theoretical complete hydrolysis of the unhydrolyzed silicone ester in step (1) and the titanium ester in step (2);
in step (2), if the mixed aqueous solution of NH 4 ReO 4 and a zinc salt is added for the reaction to form a sol, the amount of water contained in the mixed aqueous solution of NH 4 ReO 4 and a zinc salt is the amount of water required for theoretical complete hydrolysis of the unhydrolyzed silicone ester in step (1) and the titanium ester in step (2).

12. The method according to claim 11 , wherein a pore broadening agent used in step (4) for performing the pore broadening treatment is liquid ammonia.

13. The method according to claim 12 , wherein the process conditions for the pore broadening treatment in step (4) include: the pore broadening temperature is 60-140° C., and the pore broadening time is 3-15 h.

14. The method according to claim 1 , wherein an atomizer is used in the step (3) to atomize the sol, and the sol sprayed by the atomizer has an average particle diameter that is from 100 to 850 μm.

15. The method according to claim 14 , wherein the sol sprayed by the atomizer has an average particle diameter that is from 400 to 580 μm.

16. The method according to claim 1 , wherein a pore broadening agent used in step (4) for performing the pore broadening treatment is liquid ammonia.

17. The method according to claim 16 , wherein the process conditions for the pore broadening treatment in step (4) include: the pore broadening temperature is 60-140° C., and the pore broadening time is 3-15 h.

18. The method according to claim 1 , wherein in the step (5), the drying temperature is 80-120° C.; the calcination temperature is 450-600° C.

19. The method according to claim 1 , wherein a silanization agent used in the silanization treatment in step (6) is hexamethyldisilazane; based on the weight of SiO 2 corresponding to the SiO 2 from complete hydrolysis of the raw silicon ester in step (1), the amount of the hexamethyldisilazane used is 5-15 wt %.

20. The method according to claim 19 , wherein the temperature of hexamethyldisilazane used for the silanization treatment is 126-150° C., the temperature of the silanization treatment is 200-300° C., and the time of the silanization treatment is 60-180 min.

21. The method according to claim 1 , wherein the lower alcohol in step (1) and step (2) is selected from C1-C3 alcohols.

22. A method for preparing propylene oxide, comprising contacting under epoxidation conditions a feedstock with the catalyst prepared by the method according to claim 1 to produce a product comprising said propylene oxide.

Assignees

• Wanhua Chemical Group Co Ltd

Inventors

• Wang Lei
• Wang Tongji
• Ye Fei
• Yang Lichao
• Yi Guangquan
• Cui Jiaoying
• Chu Naibo
• Li Yuan
• Hua Weiqi

Classifications

• B01J2229/32

  Reaction with silicon compounds, e.g. TEOS, siliconfluoride · CPC title

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title

• B01J23/002

  Mixed oxides other than spinels, e.g. perovskite · CPC title

• B01J37/0054 Primary

  Drying of aerosols · CPC title

• B01J23/36

  Rhenium · CPC title