Preparation method for propylene epoxidation catalyst and use thereof

Patent metadata

Field	Value
Publication number	US-2022305479-A1
Application number	US-202017291250-A
Country	US
Kind code	A1
Filing date	Jan 14, 2020
Priority date	Jan 14, 2020
Publication date	Sep 29, 2022
Grant date	—

Abstract

Provided are a preparation method for a propylene epoxidation catalyst, and a use thereof. During the preparation, an alkoxide solution of a prepared active component and a silica gel support are mixed, then a rotary evaporation treatment is performed on the mixture to remove a low-carbon alcohol to obtain a catalyst precursor, and then the obtained catalyst precursor is subjected to calcination and silylation treatments to obtain the propylene epoxidation catalyst. The catalyst is prepared in a simple process, can be applied to the chemical process of preparing propylene oxide by propylene epoxidation, has high average selectivity to propylene oxide, and has industrial application prospect.

First claim

What is claimed is:

1 - 15 . (canceled)

16 . A preparation method of a propylene epoxidation catalyst, comprising the following steps:
(1) titanate and ammonium molybdate are dissolved in a low-carbon alcohol, and mixed with a silica gel support to perform a rotary evaporation treatment to remove the low-carbon alcohol to obtain a catalyst precursor; (2) a calcination treatment is performed on the catalyst precursor obtained in step ( 1 ) at elevated temperature to obtain an oxide catalyst; and (3) a silylation treatment is performed on the oxide catalyst obtained in step ( 2 ) using a silylating reagent to obtain the propylene epoxidation catalyst.

17 . The preparation method according to claim 16 , wherein in step ( 2 ), the catalyst precursor is calcined at elevated temperature under an ammonia atmosphere.

18 . The preparation method according to claim 16 , wherein in step ( 1 ), the amount of Ti in the titanate is 2 to 5 wt % of the mass of the silica gel support in step ( 1 ), and the concentration of the titanate in the low-carbon alcohol is 1 to 10 wt %.

19 . The preparation method according to claim 16 , wherein the titanate in step ( 1 ) is one or more selected from the group consisiting of tetramethyl titanate, tetraethyl titanate, tetrapropyl titanate, tetraisopropyl titanate, tetrabutyl titanate, and tetraisobutyl titanate.

20 . The preparation method according to claim 18 , wherein in step ( 1 ), the amount ratio of titanate to ammonium molybdate is such that the molar ratio of Mo to Ti is 0.05:1 to 0.2:1.

21 . The preparation method according to claim 16 , wherein the silica gel support in step ( 1 ) has an equivalent spherical diameter of 0.5 to 3 mm and a specific surface area of 800 to 900 m 2 /g.

22 . The preparation method according to claim 16 , wherein the silica gel support in step ( 1 ) has an average pore size of 2 to 3 nm.

23 . The preparation method according to claim 17 , wherein in step ( 2 ), calcination process conditions are: a calcination atmosphere is ammonia gas, and a two-stage temperature programming is adopted, in which in a first stage, a calcination temperature is 140° C. to 160° C., a calcination duration is 1 to 3 h, and a space velocity of the ammonia gas is 2 to 5 h −1 , and in a second stage, a calcination temperature is 450° C. to 600° C., a calcination duration is 3 to 5 h, and a space velocity of the ammonia gas is 0.4 to 2 h −1 .

24 . The preparation method according to claim 17 , wherein in step ( 2 ), the content of N in the oxide catalyst obtained after the calcination treatment is greater than 0.2 wt %.

25 . The preparation method according to claim 16 , wherein the silylating reagent in step ( 3 ) is hexamethyldisilazane, and the temperature of the silylation treatment is 200° C. to 300° C.

26 . The preparation method according to claim 16 , wherein the amount of the silylating reagent in step ( 3 ) is 5 to 15 wt % of the mass of the silica gel support, and the duration of the silylation treatment is 60 to 180 min.

27 . The preparation method according to claim 21 , wherein during the rotary evaporation treatment in step ( 1 ), a rotary evaporation speed is 10 to 100 rpm, a rotary evaporation temperature is 50° C. to 70° C., and a pressure is 50 to 100 KPa.

28 . A preparation method of propylene oxide, wherein the method uses the propylene epoxidation catalyst prepared by the preparation method according to claim 16 in catalyzing a propylene epoxidation reaction.

29 . The preparation method according to claim 28 , wherein the propylene epoxidation reaction is a reaction in which propylene is reacted with cumene hydroperoxide as an oxidizing agent to prepare propylene oxide.

30 . The preparation method according to claim 29 , wherein the molar ratio of the propylene to the cumene hydroperoxide is 5:1 to 7:1, and a weight hourly space velocity is 2 to 3.5 h −1 .

Assignees

• Wanhua Chemical Group Co Ltd

Inventors

• Wang Lei
• Wang Tongji
• Ye Fei
• Sun Kang
• Chu Naibo
• Jiao Qiankun
• Li Yuan

Classifications

• B01J37/0018 Primary

  Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat) · CPC title

• B01J21/08

  Silica · CPC title

• B01J21/063

  Titanium; Oxides or hydroxides thereof · CPC title

• B01J2523/47

  Titanium · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title