Method for producing o-chlorobenzonitrile
A technology of o-chlorobenzonitrile and o-chlorotoluene, applied in the preparation of hydrocarbon ammoxidation, organic chemistry, etc., can solve the problems of reactor load reduction, reactor amplification effect, and difficulty in removing heat from the reaction, so as to increase the reaction load, The effect of improving selectivity and overcoming the amplification effect
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Embodiment 1
[0052] Catalyst preparation:
[0053] 224g V 2 o 5 Add it into a solution at a temperature of 80-90° C. consisting of 490 milliliters of water and 468 grams of oxalic acid, stir well, and react to obtain a vanadium oxalate solution.
[0054] The weight percent concentration is 40% SiO 2 1250 grams of silica sol are slowly added in the above-mentioned solution under stirring, then add respectively by 864 grams of Cr (NO 3 ) 3 9H 2 O. 12.4 g KNO 3 , 71.6 g Co(NO 3 )·6H 2 A solution of O and 500 ml of water, 76.4 g of H 3 BO 3 , a solution composed of 85.1 grams of 85% phosphoric acid and 500 milliliters of water and 43.5 grams (NH 4 ) 6 Mo 7 o 24 4H 2 O and the solution that 100 milliliters of waters form, stir, heat and evaporate to solid content 40% (weight), obtain viscous slurry.
[0055] The above slurry was spray-dried in a spray dryer to shape, and the formed catalyst precursor was pre-calcined at 300°C for 2 hours, and then fired at 650°C for 4.5 hours to ...
Embodiment 2~10
[0066] The catalyst preparation method is the same as in Example 1, and the proportioning or composition of the catalyst is changed to obtain the catalyst composition in Table 1, and the catalyst evaluation method in Example 1 is used for evaluation. Its result list 1.
[0067]
Embodiment 11
[0074] According to the catalyst preparation method and composition of Example 1, 3.0 tons of industrial catalysts are produced, once filled in the 1000 tons / year o-chlorobenzonitrile fluidized bed reactor, and carried out industrial production according to the process evaluation conditions of Example 1, the catalyst is processed by half a year. Industrial operation calibration shows that the catalyst has good activity and stability. The results are shown in Table 2 below:
[0075] project
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