Method for producing p-chorotoluene by using element selenium as catalyst
A technology for p-chlorotoluene and a catalyst is applied in the field of producing p-chlorotoluene, can solve problems such as difficulty in industrial application, and achieve the effects of easy production process control, simple process flow and low production cost
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Embodiment 1
[0028] Preparation of catalyst and chlorination reaction
[0029] In a four-necked flask equipped with a reflux condenser, a chlorine pipe, a stirring and a thermometer, 0.5 g of iron powder, 0.8 g of selenium powder and 0.7 ml of benzyl chloride were added, and then 400 ml of toluene was added. Begin to pass chlorine gas at room temperature, and control the temperature not to exceed 40 °C. The chlorine gas feeding rate is 150-160 ml / min, and the feeding time is about 6 hours. At this time, the iron powder and selenium powder are all dissolved, the conversion rate of toluene is between 60-70%, and there is a large amount of the reaction material system. of oil is produced. The catalyst prepared above was stored for later use.
[0030] Take 40 ml of the above uniformly mixed catalyst (should be quickly measured after full stirring to avoid catalyst sedimentation), add 400 ml of fresh toluene, and place it in a four-necked flask equipped with a reflux condenser, a chlorine pip...
Embodiment 2
[0036] Chlorination
[0037] According to the experimental method of Example 1, an appropriate amount of one of antimony trichloride, ferric chloride and zinc chloride is added in an amount of 0.05-0.1 g, and the time of the chlorination reaction can be shortened to 5 hours. After testing, its ratio to the adjacent position is similar to that of Example 1, and the number of applications can also reach 20-80 times.
Embodiment 3
[0039] Industrialized catalyst preparation and chlorination reaction
[0040] In a 3000L reaction kettle equipped with a reflux condenser, a chlorine pipe, stirring and a thermometer, 4.0Kg of iron powder, 6.4Kg of selenium powder and 6.5L of benzyl chloride were added, and then 1600L of toluene was added. The catalyst for the cyclic chlorination of toluene is prepared by introducing chlorine gas. The preparation method is controlled as in Example 1.
[0041] 10,000 L of dry toluene was put into a reaction tower with a diameter of 1.3 m and a height of 12 m, and then 250 L of the above-mentioned catalyst was put into the reaction tower, and the reaction was carried out with chlorine. The external circulation is cooled, the temperature is controlled not to exceed 55°C, and the reaction end point is detected by chromatography. The results are: the ratio of ortho-position is 57:43, the conversion rate is more than 99.0%, and the dichlorotoluene is less than 2.5%.
[0042] Af...
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