Catalyst for methane catalytic combustion and preparation method thereof
A methane catalytic combustion and catalyst technology, which is applied in the direction of combustion methods, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of complex catalyst preparation process, improve activity and high temperature thermal stability, prolong service life, The effect of inhibiting sintering
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Embodiment 1
[0074] The Pd-CeO provided by this embodiment 2 / Al 2 o 3 The preparation method of methane catalytic combustion catalyst is as follows:
[0075] (1) Preparation of Pd nanoparticles
[0076] Dissolve 20mg of potassium chloropalladate in 2mL of deionized water and stir to dissolve. Then 10 mL of acetone was added and mixed well, the solution changed from dark brown to orange red. Then about 8 mg of 11-mercaptoalkanoic acid was added to the above solution and stirred at room temperature until dissolved. Next, add 1 mL containing 20 mg NaBH to the clear solution 4 The solution. Immediately a black substance was deposited on the bottom of the container. Remove the supernatant, wash the black sediment at the bottom of the container with 10mL of methanol and 10mL of acetone, and then add 10mL of deionized water to fully disperse.
[0077] (2) Aqueous phase dispersion of Pd-CeO 2 Preparation of two-component nanostructures
[0078] 0.175mmol Ce(NO 3 ) 3 ·6H 2 O and 0.44m...
Embodiment 2
[0084] In the present embodiment, except adding Ce(NO 3 ) 3 ·6H 2 The amounts of O and L-arginine were 0.35mmol and 0.9mmol respectively (that is, the molar ratio of Ce to L-arginine was 1:2.5), and the rest were the same as the preparation method in Example 1.
[0085] For the catalyst prepared in this example, the loading of Pd is 0.57wt%, and the molar ratio of Pd to Ce is 1:5.5. The content and activity data of each component are listed in Table 1.
Embodiment 3
[0087] The only difference from Example 2 is that in step (2), the dispersion prepared in step (1) is added dropwise into solution A, and the temperature is controlled at 10° C. during the whole process of dropping and stirring. The content and activity data of each component of the obtained catalyst are listed in Table 1.
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