Preparation process of benzoyl chloride
A technology for the preparation of benzoyl chloride, which is applied in the field of preparation and purification of benzoyl chloride, can solve the problems of equipment volume affecting production capacity, low utilization rate of light energy, high power consumption of light source, etc., and achieve resource saving and low processing cost , the effect of shortening the reaction time
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Embodiment 1
[0028] Put 1300 kg of toluene into the chlorination reaction kettle, open the steam valve of the jacket of the reaction kettle, raise the temperature of the material in the reaction kettle to 80°C, weigh 4 kg of azobisisobutyronitrile and dissolve it with 25 kg of trichlorotoluene, slowly drop into the reaction kettle, and open the valve of the chlorine gas pipeline. The chlorine gas passes through the flow meter from the bottom of the chlorination reaction kettle through the distributor and contacts with toluene to generate a side chain chlorination reaction. Adjust the jacket steam or cooling water valve of the chlorination kettle to maintain the reaction temperature. At 80-130°C, monochlorotoluene starts to be generated, continue to pass chlorine to obtain dichlorotoluene, and finally generate trichlorotoluene. When the content of dichlorotoluene in the chlorinated material is less than 0.2%, stop the chlorine flow and use compressed air Remove a small amount of chlorination...
Embodiment 2
[0031] Put 1400 kg of toluene into the chlorination reaction kettle, open the jacket steam valve of the reaction kettle, raise the temperature of the material in the reaction kettle to 90°C, weigh 3 kg of dibenzoyl peroxide and dissolve it with 30 kg of trichlorotoluene, slowly drop into the reaction kettle, and open the valve of the chlorine gas pipeline. The chlorine gas passes through the flow meter from the bottom of the chlorination reaction kettle through the distributor and contacts with toluene to generate a side chain chlorination reaction. Adjust the jacket steam or cooling water valve of the chlorination kettle to maintain the reaction temperature. At 90-130°C, monochlorotoluene starts to be generated, continue to pass chlorine to obtain dichlorotoluene, and finally generate trichlorotoluene. When the content of dichlorotoluene in the chlorinated material is less than 0.2%, stop the chlorine flow and use compressed air Remove a small amount of chlorination and residu...
Embodiment 3
[0034]Put 1000 kilograms of benzoic acid into the reaction kettle, then drop 0.585 kilograms of zinc chloride, then pump 1680 kilograms of trichlorotoluene dechlorination crude products into the kettle, open the vacuum system on the hydrochloric acid absorption device, and heat up under stirring to make the temperature Maintained at 60°C, and the vacuum degree is 740-750mmHg, depending on the amount of hydrogen chloride produced, the liquid in the kettle is black, and the temperature is raised to 120°C for 4 hours, and the hydrogen chloride gas to be generated is discharged from the reaction kettle, and the crude product of benzoyl chloride is obtained; The benzoyl chloride crude product of the zinc chloride catalyst is placed in a rectification kettle, heated to 165°C under reduced pressure, and the top pressure of the rectification tower is controlled to be 20mmHg, the top temperature of the rectification tower is 110°C, and the reflux ratio is 2 : 1, carry out rectification,...
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