Tourmalinite-containing composite methane catalyst
A catalyst, tourmaline technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, gas fuels, etc., to achieve the effects of reduced agglomeration, rational use of energy saving and emission reduction, and shortened reaction time
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Embodiment 1
[0048] (1) According to the molar ratio La:Ce:Co:Mn=9:1:5:5, weigh La(NO 3 ) 3 ·6H 2 O 16.30g, Ce(NO 3 ) 3 ·6H 2 O 1.80g, Co(NO 3 ) 2 ·6H 2 O 6.03g, mass concentration 50%Mn(NO 3 ) 2 Solution 7.34g (total metal molarity is 0.0817mol);
[0049] (2) Dissolve the nitrate weighed in the previous step in 60ml of deionized water, add 20.8g (0.098mol) of citric acid, and stir at room temperature for 1 hour to mix the ingredients evenly;
[0050] (3) Heat and stir in a water bath (80°C), the water evaporates continuously, gradually forming a sol, and continue stirring until the color of the colloid becomes darker, forming a wet gel;
[0051] (4) Let the wet gel treated in step (4) stand for 12 hours, dry and grind to obtain dry gel;
[0052] (5) The material was placed in a muffle furnace, roasted at 800° C. for 5 hours, cooled and then ground to obtain 10 grams of perovskite-type methane catalytic material. Exist in the form of composite oxide pairs La 0.9 Ce 0.1 co 0....
Embodiment 2
[0054] The difference between this embodiment and Example 1 is that 0.2 g of tourmaline (2.74 μm) (produced by Henan Xixia Company) was added after adding citric acid in step (2), and stirred at room temperature for 1 hour to obtain a mixed solution. Other steps and parameters are the same as in Example 1. Tianjin Xianquan Industry and Trade Development Co., Ltd. WFS3015 catalyst evaluation device.
[0055] attached by figure 1 Comparative example 1, 2 samples, the sample catalytic activity after adding tourmaline is higher, and methane light-off temperature reduces 15 ℃, and complete conversion temperature advances 25 ℃, thus can find out that adding tourmaline sample can effectively improve catalytic material catalysis Oxidation of methane activity.
Embodiment 3
[0057] The difference between this embodiment and Example 1 is that the Ce(NO 3 ) 3 ·6H 2 O is replaced by Sr(NO 3 ) 2 . Other steps and parameters are the same as in Example 1.
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