A kind of in-situ dissolution type catalyst and its preparation method and application
A catalyst and in-situ technology, applied in the direction of chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of large limitations of leaching metal elements and harsh leaching conditions , slow dissolution rate, etc., to achieve the effect of no change in catalyst morphology, improved catalytic activity, and improved stability
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Embodiment 1
[0050] (1) Add 0.001 mol of Cu(NO) to 20 mL of deionized water successively 3 ) 2 ·3H 2 O, 0.002mol Ni(NO 3 ) 2 ·6H 2 O and 0.1 g of multi-walled carbon nanotubes (MWCNTs), stir well. The mixed solution was transferred to a sonicator to suspend for 30 min, and then stirred at a constant speed for 24 h at room temperature to form a uniform suspension;
[0051] (2) Transfer the suspension to the autoclave, react at 80°C for 12 hours, take out and continue stirring at 80°C to completely evaporate the solvent.
[0052] (3) the solid remaining in the step (2) is placed in a quartz boat and placed in a tube furnace for calcination, and the air flow rate is 60 mLmin -1 , heated to 200°C at a heating rate of 3°C / min, and kept for 1h.
[0053] (4) Wash the powder of the calcined material in step (3) alternately with deionized water and ethanol three times, transfer it to a vacuum drying oven, and dry it at 50°C overnight to obtain Cu-doped NiOOH@MWCNT (denoted as Cu 1 Ni 2 @MW...
Embodiment 2
[0056] According to the process of Example 1, the molar ratio of copper salt and nickel salt in step (1) was changed to 1:1.5 to obtain a copper-based catalyst with nickel-based hydroxide as a solid solution. The specific surface area of the catalyst is 56.32m 2 / g.
Embodiment 3
[0058] According to the process of Example 1, the calcination temperature in step (3) was changed to be heated to 300° C. at the same heating rate, and kept for 1 h. The specific surface area of the catalyst is 50.5m 2 / g.
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