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Preparation method of p-chlorophenol

A technology for p-chlorophenol and phenol, applied in the field of preparation of p-chlorophenol, can solve problems such as a large number of by-products, low para-selectivity, easy environmental pollution, etc., and achieve the effect of high para-selectivity

Pending Publication Date: 2018-04-27
南京大学扬州化学化工研究院
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method is simple and easy to operate, but its disadvantage is that the para-selectivity is not high and a large number of by-products are generated
[0004] The sulfuryl chloride method uses sulfuryl chloride as the chlorination agent, and reacts to generate p-chlorophenol in the presence of a catalyst. The catalysts used mainly include iron trichloride, aluminum trichloride, etc., and the selectivity of the target product p-chlorophenol is very high , so this process route is a mature process commonly used in western industrialized countries, but the preparation process of the chlorinating agent sulfuryl chloride is complicated, the cost is high, it is uneconomical, and the reaction of ferric chloride is easy to pollute the environment as waste
[0005] The copper chloride method uses copper chloride as the chlorinating agent, and the selectivity of the target product of this route is relatively high. Japanese patent JPS5436221 uses copper chloride as the chlorinating agent, hydrochloric acid as the solvent, and reacts under high pressure at 130°C. The ratio reaches 10:1, but the disadvantage is that the reaction is carried out under high temperature and pressure; Acetic acid and N,N-dimethylformamide replace the water phase, copper chloride is used as the chlorinating agent, react in a pressure cooker at 180°C, and the ratio of monochlorinated products to / adjacent reaches 6:1. The disadvantage is that high temperature and high pressure are required, and The para-ortho ratio of monochlorinated products is low; Chlorine is passed into copper chloride-hydrochloric acid aqueous solution to prepare p-chlorophenol, extracted with dichloromethane after the reaction, and dichloromethane is evaporated after drying with anhydrous potassium carbonate, and the yield of p-chlorophenol is 65%. The yield of chlorophenol is low, the post-treatment is complicated, and the amount of raw material copper chloride is large, and the cost is high if it is not recycled.

Method used

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  • Preparation method of p-chlorophenol

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Experimental program
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Effect test

Embodiment 1

[0027] Under normal pressure, add 20g of phenol, 36g of copper chloride and 60g of hydrochloric acid to the chlorination reactor respectively, heat to the reaction temperature of 90°C, pass chlorine gas under the protection of nitrogen to react until the phenol is completely chlorinated, cool, and take out the upper organic phase , to obtain mixed chlorinated phenols, sampling GC analysis content, phenol conversion rate is 97.6%, p-chlorophenol selectivity is 81.1%, ortho-chlorophenol selectivity is 7.6%, and p-o-ratio reaches 10:1; Lower hydrochloric acid-chlorination After copper was added to phenol, the chlorination reaction was repeated under the same conditions, and the selectivity of p-chlorophenol remained stable at about 80% after repeated 8 times.

Embodiment 2

[0029] Under normal pressure, add 20g of phenol, 60g of copper chloride and 120g of dimethyl sulfoxide to the chlorination reactor respectively, heat the oil bath to 110°C, react for a certain period of time under the protection of nitrogen, cool and filter to obtain copper chloride Solid, sampling GC analysis content, the phenol conversion rate is 90.0%, the selectivity of p-chlorophenol is 82.0%, the selectivity of o-chlorophenol is 6.1%, and the ratio of o-to-o is as high as 12:1.

Embodiment 3

[0031] Under normal pressure, 20g of phenol, 36g of copper chloride, 40g of hydrochloric acid and 8g of dimethyl sulfoxide were respectively added to the chlorination reactor, heated to a reaction temperature of 90°C, and chlorine gas was introduced under the protection of nitrogen to react until the phenol was chlorinated completely. Cooling, take out upper organic phase, obtain organic solvent and mixed chlorinated phenol, sample GC analysis content, phenol transformation rate is 99.6%, p-chlorophenol selectivity is 83.5%, ortho-chlorophenol selectivity is 5.9%, para-ortho ratio reaches 12:1; the lower layer of hydrochloric acid-copper chloride was added to phenol and dimethyl sulfoxide and the chlorination reaction was repeated under the same conditions. After repeating 5 times, the selectivity of p-chlorophenol was maintained at about 82.5%, and the ratio of ortho was maintained at 12:1. keep it steady.

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Abstract

The invention discloses a preparation method of p-chlorophenol. The preparation method comprises feeding chlorine gas into a mixture of phenol, copper chloride and a polar solvent under the normal pressure so that the mixture undergoes a full phenol chlorination reaction, and collecting p-chlorophenol from the chlorination reaction products, wherein the polar solvent is hydrochloric acid, dimethylsulfoxide or their mixed solvent. The preparation method utilizes a one-step reaction method, copper chloride as a chlorinating agent and the polar solvent, solves the problem that the existing copper chloride method needs harsh conditions such as high temperature and high pressure and the copper chloride conversion rate is low because of use of single copper chloride, and has high para-selectivity. After the reaction, the copper chloride-polar solvent can be used for the circular chlorination reaction.

Description

technical field [0001] The invention relates to a preparation method of p-chlorophenol. Background technique [0002] P-Chlorophenol is widely used in medicine, pesticide, dyestuff and other industries, and is an important organic chemical intermediate. Because the dye intermediate 1,4-dihydroxyanthraquinone has a large demand for the raw material p-chlorophenol, the domestic production of p-chlorophenol and the research on process optimization have become a hot spot. [0003] At present, there are three preparation methods of p-chlorophenol, chlorine gas method, sulfuryl chloride method and copper chloride method. In the direct chlorination method, phenol can be chlorinated directly with chlorine gas without a catalyst to generate p-chlorophenol, o-chlorophenol and a small amount of m-chlorophenol. The reaction conditions have a great influence on the selectivity of the target product p-chlorophenol. This method is simple in process and easy to operate, but its disadvanta...

Claims

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Application Information

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IPC IPC(8): C07C37/62C07C39/28
CPCC07C37/62
Inventor 赵兵范以宁张忠良陆海孟惠恩娟周静卫松雪
Owner 南京大学扬州化学化工研究院
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