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Catalyst for combustion of ventilation air methane and preparation method thereof

A technology for burning catalysts and wind methane, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of catalyst catalytic activity limitation, complex process, complex preparation methods, etc., to meet thermal stability and Requirements for low-temperature activity, cost reduction, and the effect of simple preparation methods

Inactive Publication Date: 2010-12-15
HAO HUA CHENGDU TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] However, there are two key issues with the catalysts used in the catalytic methane combustion process: thermal stability and low-temperature activity
The metal-supported catalyst applied by Ji Shengfu and others has the advantages of low pressure drop and easy modularization, but the preparation method is relatively complicated
The catalyst process evaluation conditions disclosed by Ugling Jun and others are single, and the effect in the actual exhaust gas treatment process cannot be determined
However, the perovskite catalyst studied by Hu Ruisheng et al. has a small specific surface area, and the catalytic activity of the catalyst is limited to a certain extent. The low-temperature catalytic activity is not good, and it does not deviate from the traditional preparation process through the wet-dry gel process, and the process is still relatively complicated.

Method used

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  • Catalyst for combustion of ventilation air methane and preparation method thereof

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Comparison scheme
Effect test

Embodiment 1

[0039] The composition of present embodiment catalyst is:

[0040] 1% active component, 30% coagent and 69% carrier, the active component is ferric nitrate equivalent to 1% ferric oxide, and the coagent is cerium nitrate equivalent to 30% cerium oxide , the carrier is 69% alumina, named VAM1.

[0041] The catalyst is prepared by the following method:

[0042] (1), 5.1g ferric nitrate nonahydrate (equivalent to 1g ferric oxide), 76g cerium nitrate hexahydrate (equivalent to 30g cerium dioxide) were dissolved in 100g concentration of 5wt% citric acid aqueous solution, made into solution;

[0043] (2), immerse 69g of alumina in the aqueous solution prepared in step (1), and immerse at room temperature for 4 hours;

[0044] (3) Extrude the mixture in step (2), dry at 120°C for 1 hour, and calcinate at 500°C for 4 hours to obtain a strip catalyst.

Embodiment 2

[0046] The composition of present embodiment catalyst is:

[0047] 50% active component, 1% coagent and 49% carrier, the active component is ferrous sulfate equivalent to 50% of the content of ferric oxide in the catalyst, and the coagent is equivalent to the content of dilanthanum trioxide It is 1% lanthanum nitrate, the carrier is composed of 40% titanium oxide and 9% zirconium oxide, named VAM2.

[0048] The catalyst is prepared by the following method:

[0049] (1), 2.7 g of lanthanum nitrate hexahydrate (equivalent to 1 g of lanthanum trioxide) was dissolved in 50 g of citric acid aqueous solution with a concentration of 1 wt%, to form a solution;

[0050] (2) Dissolve 40g of titanium oxide and 9g of zirconium oxide in the aqueous solution prepared in step (1), immerse at room temperature for 3 hours, dry naturally, press into tablets, dry at 120°C for 2 hours, and bake at 500°C for 5 hours , that is, the catalyst precursor is obtained.

[0051] (3) Dissolve 174.2g of ...

Embodiment 3

[0053] The composition of present embodiment catalyst is:

[0054] 40% active component, 20% coagent and 40% carrier, the active component is 40% copper oxide, the coagent is composed of lanthanum nitrate equivalent to 20% lanthanum trioxide, and the carrier is 20% Composed of magnesium oxide and 20% calcium oxide, named VAM3.

[0055] The catalyst is prepared by the following method:

[0056] (1) Fully mix 40g of copper oxide, 20g of magnesium oxide and 20g of calcium oxide.

[0057] (2) The mixture is rolled into a ball, dried at 120°C for 2 hours, and calcined at 500°C for 2 hours to make a catalyst precursor;

[0058] (3) Dissolve 54g of lanthanum nitrate hexahydrate (equivalent to 20g of dilanthanum trioxide) in 150g of citric acid aqueous solution with a concentration of 10wt% to form a solution. The catalyst precursor in step (2) was immersed in the solution, soaked at room temperature for 6 hours, dried at 120°C for 2 hours, and calcined at 700°C for 4 hours to obta...

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Abstract

The invention discloses a catalyst for combustion of ventilation air methane and a preparation method thereof. The catalyst of the invention consists of an active ingredient, an active auxiliary agent and a porous carrier, wherein the active ingredient may be one or two of oxides of iron and copper or soluble salts of iron and copper; the active auxiliary agent is any one of cerium or lanthanum compounds; the porous carrier may be one or more of aluminum oxide, titanium oxide, zirconium oxide, magnesium oxide, calcium oxide, silica, aluminium silicate and magnesium silicate; and in form of oxide, the active ingredient accounts for 1 to 50 weight percent, the active auxiliary agent accounts for 1 to 30 weight percent and the carrier accounts for the balance. The catalyst of the invention has a catalytic effect on the combustion of the ventilation air methane and has the advantages that: the preparation method is simple; cost is low; methane ignition temperature and complete combustion temperature are low; and the like.

Description

technical field [0001] The invention relates to a catalyst and a preparation method thereof, in particular to a mine exhaust methane combustion catalyst and a preparation method thereof. Background technique [0002] Ventilation Air Methane (also known as mine ventilation, Ventilation Air Methane, referred to as VAM), refers to the gas carried by the wind after a large amount of ventilation in the coal mining process, and the air flow passes through the mining face and other places where the wind is used, and its methane concentration is lower than 0.75%. The amount of methane discharged into the atmosphere through exhaust air in my country is about 10-15 billion cubic meters per year, which is equivalent to 13-20 million tons of standard coal, and it is basically not used. Although the concentration of methane in exhaust gas is very low, the total amount is huge, accounting for about 81% of the total amount of methane emitted from coal mine gas in my country. Because meth...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C10L3/00B01D53/86B01D53/72
Inventor 廖炯陈耀壮曾健姚松柏赵英
Owner HAO HUA CHENGDU TECH
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