Catalyst for ammoxidation preparation of 2,4-dichlorobenzonitrile
A technology for the conversion rate of dichlorobenzonitrile and dichlorotoluene is applied in the preparation of hydrocarbon ammoxidation, physical/chemical process catalysts, organic chemistry, etc., and can solve the problems of poor wear resistance of catalysts, high production costs, and fluidization of the reaction. Poor quality and other problems, to achieve the effect of reducing the formation of bubbles, improving the quality of fluidization, and reducing production costs
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Embodiment 1
[0036] Catalyst preparation:
[0037] 201 g V 2 O 5 Add 440 ml of water and 420 g of oxalic acid to a solution at a temperature of 80-90° C., fully stir, and react to obtain a vanadium oxalate solution.
[0038] 40% (weight) SiO 2 1250 grams of silica sol was slowly added to the above solution under stirring, and then 798 grams of Cr(NO 3 ) 3 ·9H 2 A solution of O and 300 ml of water and 39.2 g (NH 4 ) 6 Mo 7 O 24 ·4H 2 A solution composed of O and 50 ml of water, 0.11 mol of phosphoric acid solution, and finally 9.4 g of NaNO 3 And 20 ml of water, then add 113.7 g of 30% (weight) TiCl 3 The hydrochloric acid solution is stirred and mixed, heated and evaporated to a solid content of 42% by weight to obtain a viscous slurry.
[0039] The above slurry is sprayed into shape, the gas inlet temperature of the atomizer is 250°C, the outlet temperature is 130°C, the formed catalyst is dried at 160°C for 12 hours, and calcined at 550°C for 8 hours to obtain the catalyst composition: V 1.0 Cr ...
Embodiment 2~5
[0046] The catalyst was prepared and evaluated according to the same operating conditions and process as in Example 1, except that the catalyst composition was changed and its performance examples are as follows.
[0047]
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Abstract
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