Methane catalytic oxidation catalyst for natural gas vehicle and preparation method of methane catalytic oxidation catalyst

An oxidation catalyst, methane catalysis technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve problems such as poor thermal stability, low activity, and high price , to achieve the effects of low ignition temperature and complete combustion temperature, high content of active components, and simple preparation method

Active Publication Date: 2015-04-29
韩霜
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Platinum Pt, palladium Pd, rhodium Rh and other supported noble metal catalysts have good low-temperature catalytic activity for methane combustion, but these catalysts have problems such as high price, poor thermal stability and easy sintering, which limit their application in natural gas vehicles. The application of exhaust gas post-treatment, and perovskite composite metal oxide catalysts and supported transition metal oxide catalysts are also difficult to be used industrially due to factors such as small specific surface area, poor mechanical strength and low activity. Perovskite composite metal oxide catalysts In the strong exothermic reaction of oxide catalysts, there are still problems such as easy sintering at high temperature and easy loss of B-site short-period elements.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

specific Embodiment approach 1

[0053] A general reaction formula is Sn 0.50 Zr 0.40 Ce 0.10 o 2 The methane catalytic oxidation catalyst for natural gas vehicle exhaust aftertreatment, and its preparation method has the following steps in sequence:

[0054] 1) Preparation of mixed salt

[0055] The precursor of the tin dioxide that takes 12.6g is tin tetrachloride tetrahydrate SnCl 4 4H 2 The precursor of the zirconium dioxide of O, 12.4g zirconium nitrate pentahydrate Zr (NO 3 ) 4 ·5H 2 O, and 3.1 g of the stabilizer cerium oxide precursor cerium nitrate hexahydrate Ce(NO 3 ) 2 ·6H 2 O, placed in a mortar, mixed evenly to form mixed salt;

[0056] 2) Add 40 g of urea whose weight is 1.42 times its weight to the above mixed salt, and grind for 0.5 h to obtain a paste;

[0057] 3) Put the paste above in an oven and bake it at 200°C for 12 hours to prepare a semi-finished catalyst;

[0058] 4) Place the above-mentioned semi-finished catalyst in a box-type resistance furnace, also known as a muffl...

specific Embodiment approach 2

[0062] A general reaction formula is Sn 0.50 Zr 0.40 Y 0.10 o 2 The methane catalytic oxidation catalyst for natural gas vehicle exhaust aftertreatment, its preparation method is basically the same as the specific embodiment one, the difference is:

[0063] Precursor of tin dioxide, tin tetrachloride SnCl 4 4H 2 O is 13.2 g;

[0064] The precursor of zirconium dioxide, zirconium nitrate Zr(NO 3 ) 4 ·5H 2 O is 12.9g;

[0065] The precursor of the stabilizer is yttrium nitrate pentahydrate Y (NO 3 ) 3 ·5H 2 O is 2.9g;

[0066] Urea is 120g, which is 4.13 times the weight of the mixed salt.

[0067] The solid solution catalyst Sn that specific embodiment two makes 0.50 Zr 0.40 Y 0.10 o 2 , when the volume ratio of air to methane is 49 and the air velocity is 30000m 3 Under the condition that / h and catalyst consumption are 0.2g, the methane conversion rate (%) under different stabilizer temperatures is shown in Table 1 above.

specific Embodiment approach 3

[0068] A general reaction formula is Sn 0.50 Zr 0.40 co 0.10 o 2 The methane catalytic oxidation catalyst for natural gas vehicle exhaust aftertreatment, its preparation method is basically the same as the specific embodiment one, the difference is:

[0069] Precursor of tin dioxide, tin tetrachloride SnCl 4 4H 2 O is 13.5g;

[0070] The precursor of zirconium dioxide, zirconium nitrate Zr(NO 3 ) 4 ·5H 2 O is 13.2g;

[0071] Precursor of stabilizer cobalt dioxide cobalt nitrate hexahydrate Co(NO 3 ) 2 ·6H 2 O is 2.2g;

[0072] Urea is 60g, which is twice the weight of the mixed salt.

[0073] The specific embodiment three prepared solid solution catalyst Sn 0.50 Zr 0.40 co 0.10 o 2 , when the volume ratio of air to methane is 49 and the air velocity is 30000m 3 Under the condition that / h and catalyst consumption are 0.2g, the methane conversion rate (%) under different stabilizer temperatures is shown in Table 1 above.

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Abstract

The invention relates to a methane catalytic oxidation catalyst for natural gas vehicle exhaust aftertreatment and a preparation method of the methane catalytic oxidation catalyst. The methane catalytic oxidation catalyst is a stannum-zirconium composite oxide solid solution catalyst, wherein the stannum / zirconium atomic ratio is at least 1.1, the general equation is Sn(1-x)ZrxM0.10O2, M is at least one of rare earth and transition metal, and x is a coefficient; the methane catalytic oxidation catalyst is prepared from the following components in percentage by weight: 50-70% of a stannic oxide (SnO2) precursor, 15-40% of a zirconium dioxide (ZrO2) precursor and the balance being a stabilizer oxide precursor. The preparation method sequentially comprises the following steps: (1) preparing mixed salt; (2) adding a precipitant-urea; (3) carrying out homogeneous precipitation reaction; and (4) roasting to obtain a finished product. The methane catalytic oxidation catalyst has the high active component content and can completely oxidize methane at about 500 DEG C, and the catalytic oxidation ability of a stannum-zirconium composite oxide solid solution on the methane, propane and carbon monoxide can be remarkably improved; and besides, the preparation method is simple, can be operated easily and is low in cost.

Description

technical field [0001] The invention relates to a catalyst, in particular to a methane catalytic oxidation catalyst for aftertreatment of exhaust gas from a natural gas vehicle and a preparation method thereof. Background technique [0002] As a clean energy, natural gas is taking an increasing proportion in the energy structure. However, the combustion temperature of its main component methane is very high, so the combustion efficiency is low, and a small amount of nitrogen oxides NO will be produced during the combustion process. X and other incomplete combustion products, resulting in environmental pollution. The oxygen-enriched combustion of methane in the presence of a catalyst is more in line with environmental protection requirements. [0003] The catalysts for the catalytic oxidation of methane for vehicles mainly include platinum Pt, palladium Pd, rhodium Rh and other supported noble metal catalysts, perovskite composite metal oxide catalysts and supported transit...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/14B01J23/835B01J23/34B01D53/94B01D53/72B01D53/62
CPCY02A50/20
Inventor 韩昭边义军孟德宽
Owner 韩霜
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