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A kind of hydrogen selective oxidation catalyst and preparation method thereof

An oxidation catalyst and selective technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of high loss rate of hydrocarbons, large loading of precious metals, poor reaction stability, etc., to reduce Effects of production cost, narrow particle size distribution, and easy process control

Active Publication Date: 2018-04-20
NINGBO HAIYUE NEW MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The catalyst systems currently reported mainly use alumina and silica as catalyst supports, and noble metals as active components such as Pt-Sn / Al 2 o 3 、In 2 o 3 / SiO 2 Such catalysts have defects such as poor reaction stability, easy deactivation, and high loss rate of hydrocarbons.
[0004] The Chinese invention patent application "Catalytic Method for Hydrogen Selective Oxidation in Propane Dehydrogenation Process" with the application number CN201010146876.9 discloses a method using nano-alumina as a carrier and Pt, Sn, Li, etc. as active components. The catalyst prepared by the method, the catalyst has a higher oxygen conversion rate and a lower hydrocarbon loss rate, but its noble metal loading is larger, the production cost is higher, and the selectivity of hydrogen needs to be further improved
[0005] The Chinese invention patent application with the application number CN201010146878.8 "Catalytic Catalyst for Hydrogen Selective Oxidation in Propane Dehydrogenation Process and Its Preparation Method" discloses a catalyst carrier with nano-alumina as catalyst carrier, and Bi, Pb, Mo At least one metal or oxide is used as an active component to prepare a new type of catalyst by means of ultrasonic and hydrothermal combination, and it is applied to the selective catalytic oxidation of hydrogen. The results show that the catalyst has a higher oxygen conversion rate and a lower Low hydrocarbon loss, but low hydrogen conversion (<77%) needs further improvement

Method used

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  • A kind of hydrogen selective oxidation catalyst and preparation method thereof
  • A kind of hydrogen selective oxidation catalyst and preparation method thereof
  • A kind of hydrogen selective oxidation catalyst and preparation method thereof

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Experimental program
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Embodiment 1

[0027] The preparation method of the hydrogen selective oxidation catalyst of this embodiment includes the following steps:

[0028] (1) Add HCl, anhydrous ethanol and templating agent to water in sequence, heat to 50℃ and stir for 40min; under stirring at 2500r / min, slowly add TEOS and nickel acetylacetonate to the above system, after the addition is complete Continue to stir for 12h;

[0029] The above template is a mixture of P123 and 1-butyl-3-methylimidazole leucine salt, and the molar ratio of P123 to 1-butyl-3-methylimidazole leucine salt in the mixture is 2:1 ;

[0030] (2) Transfer the system obtained in step (1) to a hydrothermal reactor, where the components and their molar ratios in the hydrothermal reactor are n(Ni source): n(SiO 2 Source): n (templating agent): n (HCl): n (H 2 O): n (ethanol) = 0.1:1:0.01:6:10:135, sealed and moved into an oven at 100°C for 26h, the resulting system was filtered, and the resulting filter cake was washed and dried at 2°C The heating ra...

Embodiment 2

[0036] The preparation method of the hydrogen selective oxidation catalyst of this embodiment includes the following steps:

[0037] (1) Add HCl, anhydrous ethanol and templating agent to water in sequence, heat to 70℃ and stir for 30min; under stirring at 1000r / min, slowly add TEOS and nickel acetylacetonate to the above system, after the addition is complete Continue stirring for 36h;

[0038] The above template is a mixture of P123 and 1-butyl-3-methylimidazole leucine salt, and the molar ratio of P123 to 1-butyl-3-methylimidazole leucine salt in the mixture is 2:1 ;

[0039] (2) Transfer the system obtained in step (1) to a hydrothermal reactor, where the components and their molar ratios in the hydrothermal reactor are n(Ni source): n(SiO 2 Source): n (templating agent): n (HCl): n (H 2 O): n (ethanol) = 0.3:1:0.05:6:15:135, sealed and moved into an oven at 130°C for 24h, the resulting system was filtered, and the resulting filter cake was washed and dried at 5°C The heating r...

Embodiment 3

[0045] The preparation method of the hydrogen selective oxidation catalyst of this embodiment includes the following steps:

[0046] (1) Add HCl, anhydrous ethanol and templating agent to water in sequence, heat to 60℃ and stir for 35min; under stirring at 1500r / min, slowly add TEOS and nickel acetylacetonate to the above system, after the addition is complete Continue stirring for 20h;

[0047] The above template is a mixture of P123 and 1-butyl-3-methylimidazole leucine salt, and the molar ratio of P123 to 1-butyl-3-methylimidazole leucine salt in the mixture is 2:1 ;

[0048] (2) Transfer the system obtained in step (1) to a hydrothermal reactor, where the components and their molar ratios in the hydrothermal reactor are n(Ni source): n(SiO 2 Source): n (templating agent): n (HCl): n (H 2 O): n (ethanol) = 0.1:1:0.02:6:12:135, sealed and moved into an oven at 120°C for 25h, the resulting system was filtered, and the resulting filter cake was washed and dried at 3°C The heating r...

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Abstract

The invention relates to a hydrogen selective oxidation catalyst, which uses SBA-15 molecular sieve with mesoporous structure as a carrier, Pt and Sn as main active components, and Ni as auxiliary active components, and Pt in the catalyst The loading amount is 0.05-0.5wt% of the weight of the catalyst carrier, the loading amount of Ni is 0.5-3.0wt% of the weight of the catalyst carrier, and the loading amount of Sn is 1.5-5.0wt% of the weight of the catalyst carrier. The present invention also relates to the preparation method of the above-mentioned catalyst. The present invention directly introduces Ni into the carrier SBA-15, which is conducive to promoting the activation of H2 on the surface of the catalyst so as to accelerate the hydrogen selective oxidation reaction and improve the conversion rate of hydrogen and oxygen in the reaction. ; Cooperate with active components Pt and Sn, so that the overall catalyst has high reaction stability and low hydrocarbon loss rate, because SBA‑15 itself has a large specific surface area, the active components are dispersed on the catalyst carrier Uniformity improves the catalytic activity of the catalyst.

Description

Technical field [0001] The invention relates to a hydrogen selective oxidation catalyst and a preparation method thereof. Background technique [0002] Propane dehydrogenation to propylene technology is currently one of the main sources of propylene. This method uses propane as a raw material to obtain propylene under the action of a catalyst, and at the same time generates hydrogen as a by-product. Since propane dehydrogenation is a strongly endothermic, reversible, and increased molecular number reaction, the chemical reaction is affected by the equilibrium reaction. There are problems such as low single-pass conversion of propane and high energy consumption in the reaction process. Carbon deposits are likely to cause catalyst deactivation, which restricts the further application and promotion of propane dehydrogenation to propylene technology. If hydrogen, which is the by-product of propane dehydrogenation, undergoes selective catalytic conversion, not only can it provide hea...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/035
Inventor 陈尊仲钱进
Owner NINGBO HAIYUE NEW MATERIAL