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
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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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