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Hydrogen selective oxidation catalyst used in propane dehydrogenation process and preparation method thereof

An oxidation catalyst, propane dehydrogenation technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problems of low hydrogen conversion rate and oxygen conversion rate , to achieve the effect of good catalytic activity, good technical effect and high oxygen conversion rate

Active Publication Date: 2011-10-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is the problem of low hydrogen conversion rate and oxygen conversion rate in the previous literature, providing a new hydrogen selective oxidation catalyst used in the propane dehydrogenation process

Method used

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  • Hydrogen selective oxidation catalyst used in propane dehydrogenation process and preparation method thereof
  • Hydrogen selective oxidation catalyst used in propane dehydrogenation process and preparation method thereof
  • Hydrogen selective oxidation catalyst used in propane dehydrogenation process and preparation method thereof

Examples

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Effect test

Embodiment 1

[0025] According to the weight ratio of nano-alumina and metal oxide is 80:20, take 2 grams and the specific surface is 50 meters 2 / g, Al with a pore size of 29 nm 2 o 3 and 0.8477 g Bi(NO 3 ) 3 Put it into a 500ml beaker, add 50ml of 1 mol / L dilute nitric acid, dissolve it by ultrasonication for 30 minutes, put the sample into the reaction kettle, seal it and carry out hydrothermal reaction at 120°C for 12 hours, and wait for cooling after the reaction is completed After reaching room temperature, take out the sample, wash it with water, and suction filter until the filtrate is neutral. After drying in a blast drying oven at 100°C for 6 hours, move it into a muffle furnace and roast at 550°C for 4 hours to obtain the desired metal oxide. catalyst. The prepared catalyst was loaded into a fixed-bed reactor, and the activity evaluation was carried out at 550°C. The results were as follows: the selectivity of hydrogen in the process was 68%, the conversion rate of oxygen was...

Embodiment 2

[0027] According to the weight ratio of nano-alumina and metal oxide is 90:10, take 2 grams of specific surface to be 50 meters 2 / g, Al with a pore size of 29 nm 2 o 3 and 0.3768 g Bi(NO 3 ) 3 Put it into a 500ml beaker, add 50ml of 1 mol / L dilute nitric acid, dissolve it by ultrasonication for 30 minutes, put the sample into the reaction kettle, seal it and carry out hydrothermal reaction at 120°C for 12 hours, and wait for cooling after the reaction is completed After reaching room temperature, take out the sample, wash it with water, and suction filter until the filtrate is neutral. After drying in a blast drying oven at 100°C for 6 hours, move it into a muffle furnace and roast at 550°C for 4 hours to obtain the desired metal oxide. catalyst. The prepared catalyst was loaded into a fixed-bed reactor, and the activity evaluation was carried out at 550°C. The results were as follows: the selectivity of hydrogen in the process was 71%, the conversion rate of oxygen was 9...

Embodiment 3

[0029] According to the weight ratio of nano-alumina and metal oxide is 50:50, take 2 grams of specific surface as 50 meters 2 / g, Al with a pore size of 29 nm 2 o 3 and 3.3907 g Bi(NO 3 ) 3Put it into a 500ml beaker, add 50ml of 1 mol / L dilute nitric acid, dissolve it by ultrasonication for 30 minutes, put the sample into the reaction kettle, seal it and carry out hydrothermal reaction at 120°C for 12 hours, and wait for cooling after the reaction is completed After reaching room temperature, take out the sample, wash it with water, and suction filter until the filtrate is neutral. After drying in a blast drying oven at 100°C for 6 hours, move it into a muffle furnace and roast at 550°C for 4 hours to obtain the desired metal oxide. catalyst. The prepared catalyst was loaded into a fixed-bed reactor, and the activity evaluation was carried out at 550°C. The results were as follows: the selectivity of hydrogen in the process was 77%, the conversion rate of oxygen was 98.2%...

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Abstract

The invention relates to a hydrogen selective oxidation metallic oxide catalyst used in a propane dehydrogenation process and a preparation method thereof, which mainly solve the problems that in the prior art, the hydrogen selective oxidation catalyst has the defects of low hydrogen selective oxidization rate and low oxygen conversion rate. In the invention, a nanometer aluminium oxide catalyst is loaded by using at least one of metal or oxides of Bi, Pb and Mo and comprises 1 to 50 parts of metal or oxides thereof and 55 to 99 parts of nanometer aluminium oxide by weight parts; the problemsare better solved by the technical scheme of the preparation method of the catalyst; and the catalyst can be applied to the hydrogen selective oxidation industrial production.

Description

technical field [0001] The invention relates to a hydrogen selective oxidation catalyst used in the propane dehydrogenation process and a preparation method thereof. Background technique [0002] Propylene is an important organic chemical raw material in petrochemical industry. In addition to being used to synthesize polypropylene, it is also widely used to produce acrylonitrile, propylene oxide, cumene, nonylphenol and other products. In addition, propylene oligomers are used to improve gasoline The main component of octane. At present, the main sources of propylene are the by-products of petroleum steam cracking to ethylene and the by-products of catalytic cracking gasoline. Since the steam cracking method is limited by the propane / ethylene co-production ratio, and the catalytic cracking method is restricted by the further production of high-octane gasoline from light hydrocarbons, it is very important to develop new methods for the preparation of propylene. [0003] The...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/18B01J23/28B01J23/44B01J23/652C07C11/06C07C5/48
CPCY02P20/52
Inventor 吴省吴文海樊志贵缪长喜陈庆龄杨为民
Owner CHINA PETROLEUM & CHEM CORP