Process for producing benzyl chlorides chemical compound
A compound and material technology applied in the production of benzyl chloride compounds, which can solve the problems of product coking, small liquid holding capacity, high temperature heat source, etc., and achieve the effects of reaction operation control, low production cost and short process flow
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Embodiment 1
[0020] Toluene and chlorine feed are both 1.40kmol / h, the distribution ratio of chlorine in the three reactors is: 0.45:0.32:0.23, the condensation at the top of the tower: 1000L / h, the temperature of the chlorination reactor is 105°C, rectification The operating pressure of the tower is 0.025MPa, the number of trays in the rectification zone is 9, and the number of trays in the separation zone is 30. After reactive distillation, the molar composition of the material in the tower kettle is: 0.48% toluene, 99.25% benzyl chloride, 0.26% benzylidene dichloride, and 0.04% cyclochlorotoluene. The selectivity of benzyl chloride is 98.96%.
Embodiment 2
[0022] Both toluene and chlorine feed are 1.40 kmol / h, the distribution ratio of chlorine in the three reactors is: 0.45:0.32:0.23, and the condensation at the top of the tower is 1300 L / h. , the temperature of the chlorination reactor is 80°C, the operating pressure of the rectification tower is 0.01MPa, the number of trays in the rectification zone is 6, and the number of trays in the separation zone is 26. After reactive distillation, the molar composition of the material in the tower kettle is: 0.46% toluene, 99.29% benzyl chloride, 0.21% benzylidene dichloride, and 0.04% cyclochlorotoluene. The selectivity of benzyl chloride is 99.08%.
Embodiment 3
[0024]Both p-chlorotoluene and chlorine feed are 1.40kmol / h, the distribution ratio of chlorine in the four reactors is: 0.38:0.28:0.20:0.18, the amount of condensation at the top of the tower: 1000L / h, and the temperature of the chlorination reactor is 105 °C, the operating pressure of the rectification tower is 0.004MPa, the number of trays in the rectification zone is 8, and the number of trays in the separation zone is 30. After reactive distillation, the molar composition of the material in the tower kettle is: p-chlorotoluene 0.43%, p-chlorobenzyl chloride 99.07%, p-chlorobenzylidene dichloride 0.48%, cyclodichlorotoluene 0.02%. The selectivity to chlorobenzyl chloride is 98.59%.
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