Method and system for continuously producing 2,5-dichlorophenol
A dichlorophenol and circulatory system technology, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of long time consumption and high risk factor, and achieve the goal of shortening reaction time, reducing side reactions, and reducing costs Effect
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Embodiment 1
[0057] The present invention adopts a continuous system to realize the continuous production of 2,5-dichlorophenol, and the continuous system is as figure 1 As shown, the diazotization circulation system and the hydrolysis circulation system, the diazotization circulation system includes a diazo strong mixing device, and the upper part of the diazo strong mixing device is connected with an aniline salt storage tank and a nitrite storage tank, so The outlet of the diazo strong mixing device is connected to the diazo liquid storage tank, the diazo liquid storage tank is connected to the first heat exchanger, the first heat exchanger is connected to the diazo strong mixing device, and the first heat exchanger is connected to the diazo strong mixing device. The heater makes the material in the diazo liquid storage tank enter the diazo strong mixing device; the hydrolysis circulation system includes a hydrolysis strong mixing device, and the discharge port of the hydrolysis strong m...
Embodiment 2
[0063] Adopt the continuous system production of embodiment 1 to produce 2,5-dichlorophenol, the continuous production method is as follows:
[0064] (1) Continuously feed the aniline salt and nitrite into the diazo strong mixing device according to the molar ratio of 1:1.0, and at the same time continuously feed the back-mixed liquid according to the molar ratio of aniline salt: back-mixed liquid of 1:10, the diazo strong In the mixing device, the materials are strongly mixed according to the linear speed of 50m / s to carry out the diazotization reaction. The diazo liquid generated by the reaction flows out continuously into the diazo liquid storage tank. The residence time in the mixing device is 0.5s; part of the diazo liquid in the diazo liquid storage tank is cooled to 5°C by the first heat exchanger, and then passed into the diazo strong mixing device continuously as the back-mixed liquid according to the above ratio, so as to Keep the temperature of the system in the dia...
Embodiment 3
[0070] Adopt the continuous system production of embodiment 1 to produce 2,5-dichlorophenol, the continuous production method is as follows:
[0071] (1) The aniline salt and nitrite are continuously fed into the diazo strong mixing device according to the molar ratio of 1:1.3, and at the same time, the aniline salt: back-mixed liquid molar ratio is continuously fed into the back-mixed liquid according to the molar ratio of 1:11, and the diazoic strong In the mixing device, the materials are strongly mixed according to the linear speed of 5m / s to carry out the diazotization reaction. The diazo liquid generated by the reaction flows out continuously into the diazo liquid storage tank. The residence time in the mixing device is 10s; part of the diazo liquid in the diazo liquid storage tank is cooled to 5°C by the first heat exchanger, and then it is continuously passed into the diazo strong mixing device as the back-mixed liquid according to the above ratio, so as to keep The te...
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