Chlorobenzene directional dual-catalytic chlorination method
A technology of chlorobenzene and catalyst, which is applied in the field of directional double catalytic chlorination of chlorobenzene, can solve the problems of high energy consumption rate, increased production cost, environmental pollution, etc., and achieve the effect of mature and reliable process and reduced emission
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Embodiment 1
[0025] First, put 30 parts of dry anhydrous benzene into the chlorination reactor, then add 1 part of copper sulfide, and when the temperature rises to 55 ° C, 7 parts of chlorine gas are introduced to react, and the flow rate of chlorine gas is 12ml / s, the stirring rate in the reactor was 55r / min, and the reaction time was 1h to obtain polychlorobenzene; then add 1 part of copper sulfide, and when the temperature rose to 320°C, the stirring rate in the reactor was 100r / min, and the reaction The time is 2 hours to obtain the chlorinated solution containing chlorinated benzene; the chlorinated solution containing chlorinated benzene obtained from the chlorination reactor is transferred to the washing tank, and the temperature of the water in the washing tank is 100°C before washing After 40min, the chlorinated solution after washing was transferred to the neutralization tank; 10 parts of 18% dilute ammonia water was added to the chlorinated solution transferred to the neutraliz...
Embodiment 2
[0027] First, put 40 parts of dry anhydrous benzene into the chlorination reactor, then add 1.5 parts of zinc sulfide, and when the temperature rises to 65°C, 10 parts of chlorine gas are introduced to react, and the flow rate of chlorine gas is 12ml / s, the stirring rate in the reactor is 58r / min, and the reaction time is 1.5h to obtain polychlorobenzene; then add 1 part of zinc sulfide, and when the temperature rises to 350°C, the stirring rate in the reactor is 130r / min, The reaction time is 3h, and the chlorinated liquid containing chlorinated benzene is obtained; the chlorinated liquid containing chlorinated benzene obtained from the chlorination reactor is transferred to the washing tank, and the temperature of the water in the washing tank is 150°C. Wash with water for 45min, and transfer the chlorinated solution after washing into the neutralization tank; add 20 parts of 20% dilute ammonia water into the chlorinated solution in the neutralization tank, and the stirring ...
Embodiment 3
[0029] First, put 50 parts of dry anhydrous benzene into the chlorination reactor, then add 3 parts of antimony sulfide, and when the temperature rises to 70°C, 17 parts of chlorine gas are fed into the reaction, and the flow rate of chlorine gas is 15ml / s, the stirring rate in the reactor was 80r / min, and the reaction time was 2h to obtain polychlorobenzene; then add 3 parts of antimony sulfide, when the temperature rose to 400°C, the stirring rate in the reactor was 150r / min, and the reaction The time is 3 hours to obtain the chlorinated liquid containing chlorinated benzene; transfer the chlorinated liquid containing chlorinated benzene obtained from the chlorination reactor into the washing tank, and wash with water after the temperature of the water in the washing tank is 200°C After 60 minutes, the chlorinated solution after washing was transferred to the neutralization tank; 30 parts of 15% dilute ammonia water was added to the chlorinated solution transferred to the ne...
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