Continuous preparation method of herbicide intermediate of 2, 4-dichlorophenol
A technology of dichlorophenol and intermediates, applied in the field of herbicide intermediates 2, can solve the problems of chemical synthesis reaction selection and low yield, complex stirred tank reactor structure, and difficult to disassemble the benzene nucleus, etc., to achieve The effect of improving the production site environment, production safety and controllability, and reducing energy consumption
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example 1
[0013] After heating 1,000 parts of phenol to 40°C, it enters the tail gas absorption tower to absorb residual chlorine, and then mixes with 1,500 parts of chlorine in the pre-chlorination tower and enters the chlorination tower from bottom to top. At a temperature of 40-60°C, after a continuous chlorination reaction occurs in a three-stage plate chlorination tower, the liquid material after the reaction can be flowed into a 2,4-dichlorophenol receiving tank, and the yield is 94.19%. The plate-type chlorination tower is made of glass-lined material.
[0014] The tail gas enters the tail gas absorption tower after passing through the separator, and the hydrogen chloride in the tail gas is recovered by water to be an acid with a concentration of 30.5%, and the yield is 97.19%. , Most of the chlorine is not absorbed by water, and returns to the pre-chlorination tower after passing through the water flushing pump, water seal pipe, and dryer.
Embodiment 2
[0016] After heating 1,000 parts of phenol to 40°C, it enters the tail gas absorption tower to absorb residual chlorine, and then mixes with 1,450 parts of chlorine in the pre-chlorination tower and enters the chlorination tower from bottom to top. At a temperature of 60-70°C, after a continuous chlorination reaction occurs in a 5-stage packed chlorination tower, the liquid material after the reaction can be flowed into a 2,4-dichlorophenol receiving tank, and the yield is 95.33%. The packed chlorination tower is made of graphite.
[0017] The tail gas enters the tail gas absorption tower after passing through the separator, and the hydrogen chloride in the tail gas is recovered by water to be an acid with a concentration of 30.5%, and the yield is 80.19%. , Most of the chlorine is not absorbed by water, and returns to the pre-chlorination tower after passing through the water flushing pump, water seal pipe, and dryer.
Embodiment 3
[0019] After heating 1,000 parts of phenol to 40°C, it enters the tail gas absorption tower to absorb residual chlorine, and then mixes it with 1,400 parts of chlorine in the pre-chlorination tower and enters the chlorination tower from bottom to top. At a temperature of 70-80°C, after a continuous chlorination reaction occurs in a 6-stage plate chlorination tower, the liquid material after the reaction can be flowed into a 2,4-dichlorophenol receiving tank, and the yield is 96.03%. The plate type chlorination tower is lined with PTFE.
[0020] The tail gas enters the tail gas absorption tower after passing through the separator, and the hydrogen chloride in the tail gas is recovered by water to be an acid with a concentration of 30.5%, and the yield is 88.23%. , Most of the chlorine is not absorbed by water, and returns to the pre-chlorination tower after passing through the water flushing pump, water seal pipe, and dryer.
[0021] The method of the invention is easy to oper...
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