Method for preparing antimony-containing catalyst used for ammoxidation of alkane
An oxidation reaction and catalyst technology, which is applied in the preparation of hydrocarbon ammoxidation, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve the problems of poor catalyst stability, volatile active components, complex preparation process, etc., to achieve Good catalyst stability, good test results and good repeatability
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Embodiment 1
[0045] 17.0 grams of ammonium heptamolybdate and 2.4 grams of antimony trioxide were dissolved in 40.0 grams of hot water to make solution (I); 3.37 grams of ammonium metavanadate were dissolved in 70.0 grams of hot water to make solution (II) ; Dissolve 2.99 grams of niobium oxalate in 9.0 grams of hot water to make a solution (III); dissolve 3.0 grams of oxalic acid in 5 grams of water to make a solution (IV). Solution (I) is joined in the solution (II) under stirring, then add solution (III) and solution (IV) successively, finally add 50 grams of silica sols that weight concentration is 40%, make the slurry of catalyst, will The slurry was stirred and evaporated at 90°C until a viscous slurry was obtained, then dried, ground, calcined in an air atmosphere at 300°C for 1 hour, and then calcined in a nitrogen atmosphere at 600°C with a flow rate of 60 ml / min for 2 hours. Propane ammoxidation catalyst 50% Mo 1 V 0.3 Nb 0.17 Sb 0.1 o x +50% SiO2 2 After tableting, 20-40 m...
Embodiment 2~5 and comparative example 2~4
[0049] Catalysts with different compositions in the following table were prepared by the same method as in Example 1, and the ammoxidation of propane to acrylonitrile was carried out with the prepared catalyst under the following reaction conditions. The specific changes and results are shown in Table 1.
[0050] The reaction conditions of above-mentioned embodiment and comparative example are:
[0051] Fixed bed reactor with an inner diameter of 8 mm
[0052] Reaction temperature 400°C
[0053] Reaction pressure Atmospheric pressure
[0054] Catalyst loading 2.0 grams
[0055] Catalyst contact time 1.2 g·s / ml
[0056] Raw material ratio (mole) propane / ammonia / air=1 / 1.2 / 10
[0057] Table 1
[0058]
[0059] The stability evaluation result of embodiment 1 and comparative example 1 is shown in table 2
[0060] Table 2
[0061]
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