Catalytic coating and double-layer microporous catalytic burner applying catalytic coating
A catalytic coating, double-layer technology, applied in the field of double-layer microporous catalytic burners, can solve the problem that the catalytic effect of the catalyst needs to be optimized, so as to improve the thermal stability and anti-sintering performance, improve the catalytic activity, and increase the combustion reaction. effect of time
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preparation example 1
[0065] A kind of adhesive, is made from the raw material of following mass number: SB powder 40g; Ce(NO 3 ) 3 ·6H 2 O8g; LaNO 3 ·H 2 O8g; HNO 3 20g; isobutyric acid 6g; deionized water 60g.
[0066] A preparation process of adhesive specifically comprises the following process steps:
[0067] According to the mass number, deionized water, LaNO 3 ·H 2 O and Ce(NO 3 ) 3 ·6H 2 Add O to SB powder to obtain mixture A, then stir mixture A, control the speed at 300r / min, add HNO to mixture A according to the mass ratio 3 and isobutyric acid, and then heated the mixture A at a constant temperature, controlled the system temperature to 75° C., and controlled the reaction time to 3 hours to obtain an adhesive.
preparation example 2-5
[0069] The differences between the mass numbers and process parameters of the raw materials in the adhesive of Preparation Example 2-5 and Preparation Example 1 are listed in Table 2, and the rest are the same as Preparation Example 1.
[0070] The mass number and process parameter of raw material in table 2 preparation example 2-5 adhesive
[0071]
[0072]
preparation example 6
[0074] An active ingredient made from the following molar quantities of raw material: Co(NO 3 ) 2 ·6H 2 O 0.2mol; Mg(NO 3 ) 2 0.8mol; (NH 2 ) 2 CO 5mol.
[0075] A kind of preparation technology of active component specifically comprises the following processing steps:
[0076] Co(NO 3 ) 2 ·6H 2 O, Mg(NO 3 ) 2 and (NH 2 ) 2 CO was mixed and stirred to obtain a mixture C, and then the mixture C was ground at room temperature, and the ground mixture C was subjected to a combustion reaction at a system temperature of 800°C, and the reaction time was controlled to be 30 minutes to obtain the product D. The active component can be obtained by naturally cooling the product D.
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