Tellurium containing alkane ammoxidation reaction catalyst
An oxidation reaction and catalyst technology, which is applied in the field of catalysts for propane ammoxidation to acrylonitrile and isobutane ammoxidation to methacrylonitrile, can solve the problems of poor catalyst stability, complicated preparation process, and low yield. Achieve the effect of good catalyst stability, good repeatability and easy access to raw materials
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[0042] [Example 1]
[0043]Dissolve 15.0 g of ammonium heptamolybdate and 4.46 g of telluric acid in 69.2 g of hot water to prepare solution (I); dissolve 3.06 g of ammonium metavanadate in 60.0 g of hot water to prepare solution (II); 5.78 grams of niobium oxalate was dissolved in 16.0 grams of hot water to make solution (III); 2.32 grams of oxalic acid was dissolved in 5 grams of water to make solution (IV); 1ml of 98% concentrated sulfuric acid was dissolved in 9 grams of water to make solution ( V). Mix solution (I), solution (II), and solution (III) under stirring, and then add solution (IV), solution (V) and 50 grams of silica sol with a weight concentration of 40% to prepare a catalyst slurry. Then put the slurry into the crystallization kettle and crystallize at 175°C for 48 hours. After the completion, take it out and stir and evaporate at 90°C to obtain a viscous slurry, then dry, grind, and calcinate in a nitrogen atmosphere at 600°C for 2 hours. Propane ammoxidation ca...
Example
[0046] [Examples 2 to 6 and Comparative Examples 2 to 3]
[0047] The catalysts with different compositions in the following table were prepared by basically the same method as in Example 1, and the prepared catalyst was used to carry out the reaction of propane ammoxidation to acrylonitrile under the following reaction conditions. The specific changes and results are shown in Table 1.
[0048] The reaction conditions of the above examples and comparative examples are:
[0049] Fixed bed reactor with an inner diameter of 8 mm
[0050] Reaction temperature 405℃
[0051] Reaction pressure atmospheric pressure
[0052] Catalyst loading volume 2.0g
[0053] Catalyst contact time 1.2 g·sec / ml
[0054] Raw material ratio (mole) propane / ammonia / air=1 / 1.2 / 10
[0055] Table 1
[0056]
Example Embodiment
[0057] The stability evaluation results of Example 6 and Comparative Example 1 are shown in Table 2.
[0058] Table 2
[0059]
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