Purifying device and purifying method for producing chlorothalonil with less than 10ppm of hexachlorobenzene
A technology of chlorothalonil and hexachlorobenzene, which is applied in the purification/separation of carboxylic acid nitrile, organic chemistry and other directions, can solve the problems of non-degradation of hexachlorobenzene, environmental hazards, etc., and achieves low hexachlorobenzene content, low equipment investment, Simple effect of purification device
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Embodiment 1
[0077] This embodiment provides a purification device for producing chlorothalonil with hexachlorobenzene not exceeding 10 ppm. The purification device includes a raw material supply unit, a purification unit and a product collection unit connected in sequence.
[0078] Described purifying unit comprises rectifying tower 8, refining kettle 9 and condenser 10, and the tower bottom outlet of rectifying tower 8 is connected with the inlet of refining kettle 9, and the outlet of refining kettle 9 is connected with condenser 10. The feed port is connected, the material of the rectification tower 8, the refining kettle 9 and the condenser 10 is 304 stainless steel, the outer wall of the rectification tower 8 is provided with heat tracing pipes, and the top of the rectification tower 8 is provided with a tubular condenser 10, the bottom of the rectifying tower 8 is provided with a tube-and-tube reboiler, the outer wall of the refining kettle 9 is provided with a jacket, and the interi...
Embodiment 2
[0084] This embodiment provides a purification device for producing chlorothalonil with no more than 10 ppm of hexachlorobenzene. The schematic diagram of the purification device is as follows figure 1 As shown, the purification device includes a raw material supply unit, a purification unit and a product collection unit connected in sequence.
[0085] Described purifying unit comprises rectifying tower 8, refining kettle 9, condenser 10, front fraction catcher 13 and front fraction vacuum pump 16, and the outlet at the bottom of rectifying tower 8 is connected with the inlet of refining kettle 9, The discharge opening of refining still 9 is connected with the feed inlet of condenser 10, and the material of described rectifying tower 8, refining still 9, front fraction catcher 13 and condenser 10 is 304 stainless steel, and described rectifying tower 8 The outer wall of the rectifying tower 8 is provided with a heat tracing pipe, the top of the rectifying tower 8 is provided w...
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