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A kind of cobalt-based catalyst and its method for propylene epoxidation reaction

A technology of cobalt-based catalyst and epoxidation reaction, which is applied in the direction of catalyst activation/preparation, catalyst carrier, chemical instruments and methods, etc., which can solve the problems of severe equipment corrosion, large investment, and long process, and achieve good stability and noble metal The effect of low dosage and high reactivity

Active Publication Date: 2022-01-04
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The chlorohydrin method seriously pollutes the environment, and the equipment corrodes severely, so it will be gradually eliminated
The co-oxidation method overcomes the shortcomings of the chlorohydrin method, but the process is long and the investment is large. At the same time, due to the production of a large number of co-products, it is severely restricted by the co-product market.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] 5.0g ethyl orthosilicate, 2.0g magnesium hydroxide and 3.0g concentration of 35% concentrated hydrochloric acid, deionized water 60mL, stirred at 80 ℃ for 1h, cooled to room temperature, dropwise added 10g concentration of 10% (NH 4 ) 6 W 7 o 24 ·6H 2 O aqueous solution was stirred at room temperature for 15 minutes to obtain a uniform solid solution suspension, which was left to stand at 80°C for 8 hours, aged at room temperature for 48 hours, the gel was rotary evaporated to remove water, and dried in vacuum at 110°C to obtain a powdery solid. The solid was placed in a tube furnace and roasted under a nitrogen gas temperature program. Starting at 30°C, the temperature was raised to 300°C at a rate of 2.25°C / min, kept at 300°C for 4 hours, and then started at 300°C, and the temperature was raised at a rate of 2.5°C / min. To 600°C, keep at 600°C for 4h. After natural cooling, the SiO2-MgO-WO3 metal composite oxide carrier is obtained.

Embodiment 2

[0036] 6.0g ethyl orthosilicate, 2.0g magnesium hydroxide and 3.0g concentration of 35% concentrated hydrochloric acid, deionized water 60mL, stirred at 80 ℃ for 1h, cooled to room temperature, dropwise added 8g concentration of 10% (NH 4 ) 6 W 7 o 24 ·6H 2O aqueous solution was stirred at room temperature for 15 minutes to obtain a uniform solid solution suspension, which was left to stand at 80°C for 8 hours, aged at room temperature for 48 hours, the gel was rotary evaporated to remove water, and dried in vacuum at 110°C to obtain a powdery solid. The solid was placed in a tube furnace and roasted under a nitrogen gas temperature program. Starting at 30°C, the temperature was raised to 300°C at a rate of 2.25°C / min, kept at 300°C for 4 hours, and then started at 300°C, and the temperature was raised at a rate of 2.5°C / min. To 600°C, keep at 600°C for 4h. After natural cooling, the SiO2-MgO-WO3 metal composite oxide carrier is obtained.

Embodiment 3

[0038] 4.0g ethyl orthosilicate, 2.0g magnesium hydroxide and 3g concentration of 35% concentrated hydrochloric acid, deionized water 60mL, stirred at 80 ℃ for 1h, cooled to room temperature, dropwise added 8g concentration of 10% (NH 4 ) 6 Mo 7 o 24 ·6H 2 O aqueous solution was stirred at room temperature for 15 minutes to obtain a uniform solid solution suspension, which was left to stand at 80°C for 8 hours, aged at room temperature for 48 hours, the gel was rotary evaporated to remove water, and dried in vacuum at 110°C to obtain a powdery solid. The solid was placed in a tube furnace and roasted under a nitrogen gas temperature program. Starting at 30°C, the temperature was raised to 300°C at a rate of 2.25°C / min, kept at 300°C for 4 hours, and then started at 300°C, and the temperature was raised at a rate of 2.5°C / min. To 600°C, keep at 600°C for 4h. After natural cooling, a SiO2-MgO-MoO3 metal composite oxide carrier is obtained.

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Abstract

A cobalt-based catalyst for the epoxidation of propylene, which is a catalyst used to catalyze the epoxidation of propylene to generate propylene oxide under the condition of oxygen as the oxygen source, wherein the cobalt in the oxidized state and X is loaded on a carrier containing tungsten oxide and (or) molybdenum oxide in the range of 0.05-0.99 in terms of Co / (Co+X) atomic ratio, where X is selected from nickel, gold, palladium, platinum, ruthenium, silver, At least one element of the group consisting of lanthanum and copper.

Description

technical field [0001] The invention provides a method for applying a novel cobalt-based catalyst to catalyze the epoxidation reaction of propylene to generate propylene oxide under the condition of using oxygen as an oxygen source. Background technique [0002] Propylene oxide (PO) is an important basic organic chemical raw material. Mainly used in the production of polyurethane, unsaturated resins and surfactants. Propylene oxide is also an important raw material for fine chemical products. There are nearly a hundred kinds of its downstream derivative products, which are widely used in many industries such as automobile, construction, food, medicine and cosmetics. [0003] At present, the production methods of propylene oxide in the industry mainly include the chlorohydrin method and the co-oxidation method (Halcon method), and the production capacity of these two methods accounts for more than 95% of the PO production capacity in the world. The chlorohydrin method serio...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/28B01J23/30B01J23/89B01J32/00B01J37/03B01J37/08C07D301/10C07D303/04
CPCY02P20/52
Inventor 高爽赵公大吕迎
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI