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Reduction method, catalyst and application of catalyst for preparing propylene oxide by propylene epoxidation

A technology of propylene oxide and catalyst, which is applied in the application field of the catalyst in the direct epoxidation of propylene to prepare propylene oxide system, which can solve the problems of low propylene oxide generation rate, low activity, gap, etc., and achieve an increase in the generation rate , good active effect

Active Publication Date: 2021-05-11
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

However, although the gold catalyst has been extensively studied, its activity in the epoxidation of propylene is still relatively low, and the generation rate of propylene oxide is still relatively low, far from the industrialization target (Angew.Chem.Int.Ed, 2004, 43, 1546-1548) there is still a big gap

Method used

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  • Reduction method, catalyst and application of catalyst for preparing propylene oxide by propylene epoxidation
  • Reduction method, catalyst and application of catalyst for preparing propylene oxide by propylene epoxidation
  • Reduction method, catalyst and application of catalyst for preparing propylene oxide by propylene epoxidation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0064] This example illustrates the test results of the Au / TS-1 catalyst reduced with a mixed gas of hydrogen and ethylene at 200°C in the epoxidation of propylene.

[0065] Get 0.15g of fresh catalyst, pack in the reaction tube, pass into the volume is 5% H 2 and C 2 h 4 The mixed gas, the diluent gas is nitrogen, and the total gas flow rate is 20mL / min. The reaction furnace was raised from room temperature to 200 °C at a rate of 1 °C / min, kept at constant temperature for 1 h, and finally cooled down to room temperature naturally. The mixed gas of propylene, oxygen, hydrogen, and nitrogen with a volume ratio of 5 / 5 / 5 / 85 is passed into the reaction furnace at a flow rate of 20mL / min, and the reaction furnace is raised from room temperature to 200°C at a rate of 1°C / min. Epoxidation reaction with catalyst.

[0066] The result after reacting 10h is as follows: the conversion ratio of propylene is 7.0%, the selectivity of propylene oxide is 87%, and the generation rate of pro...

Embodiment 2

[0068] This example illustrates the test results of the Au / TS-1 catalyst reduced with a mixed gas of hydrogen and ethylene at 300°C in the epoxidation of propylene.

[0069] Get 0.15g of fresh catalyst, pack in the reaction tube, pass into the volume is 5% H 2 and C 2 h 4 The mixed gas, the diluent gas is nitrogen, and the total gas flow rate is 20mL / min. The reaction furnace was raised from room temperature to 300 °C at a rate of 1 °C / min, kept at a constant temperature for 1 h, and finally cooled down to room temperature naturally. The mixed gas of propylene, oxygen, hydrogen, and nitrogen with a volume ratio of 5 / 5 / 5 / 85 is passed into the reaction furnace at a flow rate of 20mL / min, and the reaction furnace is raised from room temperature to 200°C at a rate of 1°C / min. Epoxidation reaction with catalyst.

[0070] Figure 4 The test results of the catalyst reduced by the mixture of hydrogen and ethylene at 300°C in the epoxidation of propylene are shown. The result aft...

Embodiment 3

[0072] This example illustrates the test results of the Au / TS-1 catalyst reduced with the mixed gas of hydrogen and propylene in the epoxidation of propylene at 200°C.

[0073] Get 0.15g of fresh catalyst, pack in the reaction tube, pass into the volume is 5% H 2 and C 3 h 6 The mixed gas, the diluent gas is nitrogen, and the total gas flow rate is 20ml / min. The reaction furnace was raised from room temperature to 200 °C at 1 °C / min, kept at constant temperature for 1 h, and finally cooled down to room temperature naturally. The mixed gas of propylene, oxygen, hydrogen, and nitrogen with a volume ratio of 5 / 5 / 5 / 85 is passed into the reaction furnace at a flow rate of 20mL / min, and the reaction furnace is raised from room temperature to 200°C at a rate of 1°C / min. Epoxidation reaction with catalyst.

[0074] The result after reacting 10h is as follows: the conversion rate of propylene is 8.1%, the selectivity of propylene oxide is 85.6%, and the generation rate of propylene...

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Abstract

The present invention relates to a kind of reduction method of catalyst used for preparing propylene oxide by epoxidation of propylene, which adopts mixed gas containing olefin to replace traditional gas reducing agent (H 2 , O 2 or CO) to reduce the unreduced fresh catalyst, the mixed gas is H 2 Or a mixture of CO and olefins, and the fresh unreduced catalyst is a titanium-silicon molecular sieve material loaded with nano-gold. The present invention also relates to the catalyst obtained by the above reduction method and its application. The method of propylene epoxidation is as follows: propylene, oxygen and hydrogen are used as raw materials, and a gas-solid phase epoxidation reaction is carried out in the range of 150-210°C under normal pressure by contacting with a certain amount of catalyst. The catalyst reduced by this method shows very good activity in the propylene epoxidation reaction, and the generation rate of propylene oxide is also greatly improved, which has a great impetus for the industrial application of gold catalysts.

Description

technical field [0001] The invention relates to a reduction method of a catalyst for preparing propylene oxide by propylene epoxidation and the catalyst, and also relates to the application of the catalyst in a system for preparing propylene oxide by direct epoxidation of propylene. Background technique [0002] Propylene oxide is an important organic chemical raw material and the third largest propylene derivative after polypropylene and acrylonitrile. Chemical raw materials prepared from propylene oxide are widely used in medicine, cosmetics, construction and other industries. At present, the industrial production of propylene oxide mainly includes the chlorohydrin method and the co-oxidation method, and these two methods account for the vast majority of the total production capacity of propylene oxide in the world. The chlorohydrin method is highly corrosive to equipment due to the chlorine contained in the raw material. At the same time, a large amount of waste water, w...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/89C07D301/10C07D303/04
CPCB01J29/89B01J37/16B01J37/18C07D301/10C07D303/04Y02P20/52
Inventor 黄家辉任跃功
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI