Fluid bed catalyst in use for oxidizing reaction of olefin ammonia
A technology of fluidized bed catalyst and oxidation reaction, which is applied in the direction of metal/metal oxide/metal hydroxide catalyst, preparation of hydrocarbon ammoxidation, physical/chemical process catalyst, etc. Reduce and reduce active sites and other problems, and achieve the effects of improved wear resistance, long service life and excellent catalytic performance
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Embodiment 1
[0037] 425.4 g (NH 4 ) 6 Mo 7 o 24 4H 2 O was added to 325 grams of warm water at 70°C, stirred to make it all dissolve, and then 11.6 grams of solid silicon dioxide was added with a particle size of 5 to 20 nanometers. After the slurry was uniform, 1401 grams of 40 wt% silicon dioxide was added. Silica sol, make material A.
[0038] 178.3 g Fe(NO 3 ) 3 9H 2 O was added to 170 g of 70°C hot water, stirred and dissolved, and then 129.0 g of Bi(NO 3 ) 3 ·5H 2 O, 62.4 g Ce(NO 3 ) 3 ·nH 2 O, 105.7 g Mg(NO 3 ) 3 ·6H 2 O, 312.8 g Ni(NO 3 ) 3 ·6H 2 O and 18.1 g Co(NO 3 ) 3 ·6H 2 O is stirred and dissolved to make material B.
[0039] Add 1.5 grams of KNO to 20 grams of water 3 , 1.7 g LiNO 3 and 2.4 g CsNO 3 After dissolution it was added to feed B to form feed C.
[0040] Material C was added dropwise to material A under rapid stirring, and the obtained material was aged at 70°C for 3 hours, then spray-dried into granules, and the obtained granules were roa...
Embodiment 2~10
[0042] Change the starting material of the active component and the amount thereof, change the content of the carrier silica in the total amount of the catalyst and the amount of solid silica in the carrier, and the rest are the same as in Example 1. The finished catalyst was evaluated using the above-mentioned investigation and evaluation conditions.
Embodiment 2
[0048] Example 2 Mo 11.2 Bi 0.45 Fe 2 Ni 5.2 Mg 2 La 0.3 Rb 0.06 K 0.09 W 0.46 V 0.3 P 0.04 o x
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