Novel chloroxylenol production process by high-temperature chlorination process
A technology for chlorinated m-xylenol and high-temperature chlorination, applied in chemical instruments and methods, organic chemistry, preparation of organic compounds, etc., can solve the problems of large environmental impact of boiling point solvents, large environmental pressure, and operator hazards, etc. Achieve the effect of continuous and stable production process, improve production efficiency and reduce work intensity
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Embodiment 1
[0028] The raw material 3,5-dimethylphenol is poured into the preheater through the flow meter, the temperature is raised to 90-100°C, and then it enters the upper part of the chlorination tower and is sprayed down through the distributor, and the chlorinating agent and the raw material 3,5-di According to the molar ratio of 1:1.05~1:1.1, methyl phenol enters the lower part of the chlorination tower after gasification, and is evenly distributed through the distributor; at this time, the raw material 3,5-dimethylphenol is mixed with the chlorination tower from the upper part. The bottom-up chlorinating agent gas contacts and produces the target product 4-chloro-3,5-dimethylphenol product. The material in the chlorination tower is forced to circulate externally by a circulation pump, and a heat exchanger is installed at the outlet of the circulation pump to adjust the temperature inside the chlorination tower, and the feeding, discharging, and temperature adjustment of the chlori...
Embodiment 2
[0030] The raw material 3,5-xylenol is heated and melted in the drying room, then pumped into the raw material storage tank, and then pumped at a rate of 0.3m through the feed pump. 3 / h into the preheater to preheat to 100°C and then enter the chlorination tower. A regulating valve and a flow meter are installed on the feed pipeline, and the feed flow can be adjusted through the distributed control system. The chlorinating agent sulfuryl chloride passes through the feed pump, regulating valve and flow meter from the sulfuryl chloride storage tank at a rate of 0.183m 3 The flow rate of / h is heated to 70°C through the vaporizer. The liquid 3,5-dimethylphenol is sprayed down from the upper part of the chlorination tower, and the gaseous chlorinating agent sulfuryl chloride passes through the sparger and then goes upwards to fully contact with the liquid 3,5-dimethylphenol to react instantly to form 4-chloro- 3,5-Dimethylphenol. The regulating valve of the discharge pipeline c...
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Abstract
Description
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Application Information
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