Process for preparing 2,6- dichlor-4-trifluoromethyl aniline
A technology of trifluoromethylaniline and trichlorobenzotrifluoride, which is applied in the field of preparation 2, can solve the problems of high reaction temperature and strong dependence on basic catalysts, achieve low reaction temperature, high reaction yield, and increase yield Effect
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Embodiment 1
[0020] Preparation of 2,6-dichloro-4-trifluoromethylaniline:
[0021] Put 200g of 3,4,5-trichlorobenzotrifluoride and 145g of water into a 1000ml autoclave respectively, then close the reactor, fill it with 380g of liquid ammonia, close the valve after adding, turn on the stirring, and slowly raise the temperature to 160°C, the pressure rises to 10Mpa, and timed heat preservation is carried out. During the heat preservation period, the reaction temperature is controlled to 165°C, the pressure is 11.5Mpa, and the heat preservation time is 8h. After the heat preservation is completed, the pressure is released and the ammonia is discharged.
[0022] After the reaction material was washed with water, the reaction crude product was rectified, and 20.4 g of unreacted raw material 3,4,5-trichlorobenzotrifluoride was recovered to obtain 120 g of 2,6-dichloro-4-trifluoromethylaniline with a content of 99.24%. Yield 72.48%.
Embodiment 2- Embodiment 6
[0024] Device and operating steps are the same as in Example 1, and the results are shown in Table 1
[0025] Test results under different process conditions in table 1
[0026]
Embodiment 7
[0028] Put 200.0kg of 3,4,5-trichlorobenzotrifluoride, 130.0kg of water, and 360.0kg of liquid ammonia into a 1000L high-pressure reactor, close the reactor after feeding, start stirring, slowly raise the temperature to 170°C, and the initial pressure When the temperature is 0.2Mpa, start timing and heat preservation. During the heat preservation period, the reaction temperature is controlled at 170±5°C, the pressure is between 11.0-12.0Mpa, and the time is 9h. After the heat preservation is over, the material is cooled to 100°C, and the pressure in the primary absorption tank is controlled at Pressure relief and ammonia discharge between 0 and 1.8Mpa, and cooling with frozen brine. During the process of ammonia discharge, when the pressure in the primary absorption tank is greater than 1.8Mpa, it will enter the secondary absorption tank for absorption, during which the secondary absorption is controlled. The pressure in the tank is between 0 and 1.2Mpa. After the pressure reli...
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