Preparation method of tetrachloro-terephthalonitrile with low hexachlorobenzene content
A technology of tetrachloroterephthalonitrile and terephthalonitrile, which is applied in the field of preparation of chemical intermediate tetrachloroterephthalonitrile, can solve the problems of unfavorable environmental protection, many intermediate products, and many wastes, and achieve The process and operation are practical, the steps are simple, and the chlorine flow is reasonable.
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Embodiment 1
[0013] Put the metered amount of terephthalonitrile into the vaporizer for vaporization. After the vaporization of isophthalonitrile, it is taken out of the vaporizer by nitrogen gas and mixed with chlorine gas, and then enters the fluidized bed and fixed bed equipped with special chlorination catalyst in turn. react. The molar ratio of the intake air is isophthalonitrile: nitrogen: chlorine = 1:6:4.2, the reaction temperature of the fluidized bed and the fixed bed are respectively controlled at 310°C and 342°C, and the pressure is 0.003MP. After the reaction, the reaction The mixed gas is sent to the receiver, and tetrachloroterephthalonitrile is obtained after condensing and drying, with a yield of 95.3%, a content of 99.2%, and HCB of 15.2ppm.
Embodiment 2
[0015] Put the measured amount of terephthalonitrile into the vaporizer for vaporization. After the terephthalonitrile is vaporized, it will be taken out of the vaporizer by nitrogen gas and mixed with chlorine gas, and then enter the fluidized bed and fixed bed equipped with special chlorination catalysts. react. The molar ratio of the intake air is isophthalonitrile: nitrogen: chlorine = 1:7:5, the reaction temperature of the fluidized bed and the fixed bed are respectively controlled at 320°C and 345°C, and the pressure is 0.004MP. After the reaction, the reaction The mixed gas is sent to the receiver, and tetrachloroterephthalonitrile is obtained after condensing and drying, with a yield of 96.2%, a content of 99.5%, and HCB of 12 ppm.
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