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Catalyst for catalytic methane oxidation and preparation method thereof

A methane catalysis and catalyst technology, which is applied in the field of methane catalytic oxidation catalyst and its preparation, can solve the problems of difficult and stable use, inapplicability and the like

Active Publication Date: 2015-02-25
韩霜
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The composite oxides used in the above two catalysts are prepared by roasting at a temperature of 500°C to 700°C for 4 hours. It is difficult to use stably at a temperature higher than 700°C, and the methane combustion reaction is a strong exothermic reaction. The temperature of complete combustion is generally higher than 700°C, therefore, the above two catalysts are not suitable for catalytic oxidation of methane

Method used

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Examples

Experimental program
Comparison scheme
Effect test

specific Embodiment approach 1

[0124] The general reaction formula of a tin-based solid solution is Sn 0.5 Cr 0.5 o 2 The catalyst for the catalytic oxidation of methane for the post-treatment of natural gas vehicle exhaust is a core-shell structure of modified alumina wrapped by tin-based solid solution hydrolysis, and the carrier is a micron powder of core-shell structure wrapped by tin-based solid solution hydrolysis.

[0125] Its components and their mass percentages are as follows:

[0126] Tin-based solid solution Sn 0.5 Cr 0.5 o 2 20%;

[0127] Rare earth modified alumina and 80%;

[0128] Its preparation method has the following steps successively:

[0129] 1) Preparation of modified alumina

[0130] Adopt peptization method to prepare, have the following sub-steps successively:

[0131]1.1) According to the ratio of 30 / 100ml, and the mass percentage of the precursor of alumina-pseudoboehmite PB and the nitrate of rare earth metal is 1:7%, add deionized water and rare earth met...

specific Embodiment approach 2

[0148] The general reaction formula of a tin-based solid solution is Sn 0.5 Ce 0.5 o 2 The catalyst for the catalytic oxidation of methane for the post-treatment of natural gas vehicle exhaust is a core-shell structure of modified alumina wrapped by tin-based solid solution hydrolysis, and the carrier is a micron powder of core-shell structure wrapped by tin-based solid solution hydrolysis.

[0149] Its components and their mass percentages are as follows:

[0150] Tin-based solid solution Sn 0.5 Ce 0.5 o 2 20%;

[0151] Alkaline earth metal modified alumina 80%;

[0152] The step 1) of the preparation method for preparing modified alumina is the same as the first embodiment.

[0153] The step 2) in its preparation method prepares methane catalytic oxidation catalyst basically with specific embodiment one, difference is:

[0154] Weigh the precursor of 15.8g tin oxide tetrahydrate tin tetrachloride SnCl 4 4H 2 The precursor of O and 9g ceria 3 ) 4 ·6H ...

specific Embodiment approach 3

[0158] The general reaction formula of a tin-based solid solution is Sn 0.5 Zr 0.5 o 2 The catalyst for the catalytic oxidation of methane for the post-treatment of natural gas vehicle exhaust is a core-shell structure of modified alumina wrapped by tin-based solid solution hydrolysis, and the carrier is a micron powder of core-shell structure wrapped by tin-based solid solution hydrolysis.

[0159] Its components and their mass percentages are as follows:

[0160] Tin-based solid solution Sn 0.5 Zr 0.5 o 2 20%;

[0161] Rare earth modified alumina 80%;

[0162] The step 1) of the preparation method for preparing modified alumina is the same as the first embodiment.

[0163] The step 2) in its preparation method prepares methane catalytic oxidation catalyst basically with specific embodiment one, difference is:

[0164] Weigh the precursor of 10.7g tin oxide tetrahydrate tin tetrachloride SnCl 4 4H 2 O and 19.6 g of zirconium oxide precursor zirconium ni...

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Abstract

The invention discloses a catalyst for catalytic methane oxidation and a preparation method thereof. The catalyst has a tin-based solid solution hydrolysate coated core-shell structure, the supporter is micro powder of the tin-based solid solution hydrolysate coated core-shell structure, and the core-shell structure is a modified aluminum oxide core-shell structure; the tin-based solid solution is the one doped with rare earth or transition metal, the reaction general formula of the tin-based solid solution is SnxM1-xO2, and in the formula, M is one of the rare earth and the transition metal; x is a coefficient; and the catalyst comprises 10-70 mass percent of tin-based solid solution and the balance of rare earth modified aluminum oxide or alkaline-earth metal modified aluminum oxide. By adopting the tin-based solid solution hydrolysate coated core-shell structure, the consumption of tin rich solid solution is reduced to 10-30%, and the catalyst has excellent thermal stability and low-temperature activity; the raw materials are readily available non-noble metals, so the cost is low; and the catalyst is simple in preparation, has light pollution, facilitates large-scale industrialized production, and is suitable for catalytic oxidation treatment of natural gas automobile exhaust of which the methane concentration is less than 4%.

Description

technical field [0001] The invention relates to a methane oxidation catalyst, in particular to a catalyst for catalytic oxidation of methane and a preparation method thereof. Background technique [0002] Existing noble metal-based methane catalytic oxidation catalysts have a strong ability to activate chemical bonds O-O and C-H, making originally very stable molecules form highly reactive free radicals, thereby triggering chain reactions. Compared with catalytic oxidation catalysts, it has higher catalytic activity. However, in actual use, due to the problems of poor stability and easy sintering of noble metals, some catalysts are improved by improving the carrier of noble metals or palladium Pd and other platinum group metals platinum Pt , osmium Os, iridium Ir, ruthenium Ru, rhodium Rh at least one common method for making double noble or multi-noble metal catalysts has not yet achieved significant results in improving its thermal stability, and the price is expensive, so...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/14B01J23/34B01J23/26B01J23/835B01D53/94B01D53/72
Inventor 韩昭廖缤戢廷孟德宽
Owner 韩霜
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