Method for directly synthesizing aniline from benzene and ammonia by one step
A benzene one-step, direct technology, applied in chemical instruments and methods, preparation of amino-substituted hydrogen atoms, molecular sieve catalysts, etc., can solve the problems of complex catalyst preparation process, unsatisfactory yield and other problems, and achieve short catalytic reaction time, low price, high yield effect
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[0018] Example 1 Weigh 0.1143g NiSO respectively 4 , 0.1007g CuSO 4 ·5H 2 O, 0.0795g CeN 5 O 9 ·6H 2 O, 0.1004g VOSO 4 ·NH 2 O, 0.5127g TiCl 3 ·NH 2 O (35%) was heated and stirred in 2 mL of deionized water until all was dissolved, and set aside. Weigh 5 parts of 1g TS-1 powder and place them in 5 test tubes respectively, and vacuumize at 25℃ for 0.5 hours, the vacuum degree is 0.9×10 2 KPa, while maintaining the vacuum, respectively pour the prepared 5 parts of the metal salt solution into the carrier in the 5 test tubes while it is hot, and let stand for 24 hours; move the test tube into the drying box, Dry it at a temperature of ℃ to completely dry, transfer the dried catalyst into a crucible, and calcinate at 500℃ for 4 hours. The catalysts are labeled as Ni / TS-1, Cu / TS-1, Ce / TS-1, V / TS-1, Ti / TS-1, and the metal loading percentages of the above 5 catalysts are all 2.5%. Store them dry for later use .
Example Embodiment
[0019] Example 2 Weigh 0.2286g, 0.3429g, 0.4572g NiSO respectively 4 According to the method of Example 1, a Ni / TS-1 catalyst was prepared, in which the mass percentages of nickel loading were 5.0%, 7.5%, and 10.0% respectively.
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[0020] Example 3 Weigh TS-1, Ni / TS-1, V / TS-1, Cu / TS-1, Ce / TS-1, Ti / TS-1 (the metal loading percentages are all 2.5%) 0.3g in six 50mL two-necked flasks, add 5mL benzene and 10mL 25% ammonia water, stir and heat to 70℃, add 2mL30%H 2 O 2 , Then add 2mL 30% H every 24 minutes 2 O 2 , Add a total of 10mL 30% H 2 O 2 , The reaction time is 2 hours, and the effects of different metal-supported catalysts on the yield of aniline and the selectivity of aniline are obtained. The results are shown in Table 1.
[0021] Table 1 The influence of different metal supported catalysts on the yield and selectivity of aniline
[0022]
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