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Method for producing 2,4-dichlorotoluene by using parachlorotoluene

A technology of p-chlorotoluene and dichlorotoluene, applied in chemical instruments and methods, molecular sieve catalysts, organic chemistry, etc., can solve the problems of low product yield, many by-products, and acidic wastewater, and achieve high product yield, The method is simple and the effect is good

Inactive Publication Date: 2016-03-02
NANJING ZHONGTENG CHEM
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

This method has low selectivity of 2,4-dichlorotoluene in industrial production, many by-products, many acid waste water, and large catalyst consumption
[0004] (2) Obtained by isomerization of dichlorotoluene, and the isomerized products are separated by mesoporous molecular sieves. The production cost of this method is relatively high, and it is difficult to realize industrial production
[0005] (3) Using 3-chloro-p-toluidine as raw material, carry out diazotization reaction with sodium nitrite to obtain 2-chloro-4-diazonium methyl salt, and use cuprous chloride to convert the diazo group into chlorine , after separation and purification, 2,4-dichlorotoluene is obtained, the method is complex and the product yield is low
[0006] (4) Using p-chlorotoluene and chlorine gas as raw materials and using NaKL zeolite as a catalyst, one-step direct chlorination synthesis of 2,4-dichlorotoluene in a fixed-bed continuous reactor. The conversion rate of toluene and the yield of 2,4-dichlorotoluene are low, only about 55%

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0020] (a) Preparation of chlorination catalyst: After 5 parts of iron powder, 10 parts of aluminum trichloride and 80 parts of L-type molecular sieves are mixed, they are mixed with silica sol, and then processed at 80° C. for 4 to 6 hours to obtain a chlorination catalyst; ;

[0021] (b) chlorination of p-chlorotoluene: add p-chlorotoluene in reactor, add chlorination catalyst, open and stir and make catalyzer be evenly distributed in material, open the chlorine flowmeter valve of chlorine buffer tank, to be equipped with ortho-chlorotoluene Chlorine gas is introduced into the reaction kettle, the tail gas absorption circulating water pump is turned on to absorb the tail gas produced after the reaction, the flow rate of chlorine gas is controlled, and the molar ratio of p-chlorotoluene and chlorine gas in the reaction kettle is controlled at 1:0.6, and the temperature in the reaction is controlled at 40 ± 5°C; the reaction time of chlorine flow is controlled at 15 hours, the...

Embodiment 2

[0025] (a) Preparation of chlorination catalyst: after 10 parts of iron powder, 20 parts of aluminum trichloride and 60 parts of L-type molecular sieves are mixed, then mixed with silica sol, and then processed at 120° C. for 4 to 6 hours to obtain a chlorination catalyst;

[0026] (b) chlorination of p-chlorotoluene: add p-chlorotoluene in reactor, add chlorination catalyst, open and stir and make catalyzer be evenly distributed in material, open the chlorine flowmeter valve of chlorine buffer tank, to be equipped with ortho-chlorotoluene Chlorine gas is introduced into the reaction kettle, the tail gas absorption circulating water pump is turned on to absorb the tail gas produced after the reaction, the flow rate of chlorine gas is controlled, and the molar ratio of p-chlorotoluene and chlorine gas in the reaction kettle is controlled at 1:0.8, and the temperature in the reaction is controlled at 40± 5°C; the reaction time of chlorine flow is controlled at 15-18 hours, stop c...

Embodiment 3

[0030] (a) Preparation of chlorination catalyst: after mixing 8 parts of iron powder, 15 parts of aluminum trichloride and 70 parts of L-type molecular sieves, they are mixed with silica sol, and then processed at 100° C. for 4 to 6 hours to obtain a chlorination catalyst;

[0031] (b) chlorination of p-chlorotoluene: add p-chlorotoluene in reactor, add chlorination catalyst, open and stir and make catalyzer be evenly distributed in material, open the chlorine flowmeter valve of chlorine buffer tank, to be equipped with ortho-chlorotoluene Chlorine gas is introduced into the reaction kettle, the tail gas absorption circulating water pump is turned on to absorb the tail gas produced after the reaction, the flow rate of chlorine gas is controlled, and the molar ratio of p-chlorotoluene and chlorine gas in the reaction kettle is controlled at 1:0.7, and the temperature in the reaction is controlled at 40± 5°C; the reaction time of chlorine flow is controlled at 16 hours, the chlor...

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Abstract

The invention discloses a method for producing 2,4-dichlorotoluene by using parachlorotoluene. The method comprises the steps of (a) adding a chlorination catalyst; (b) chlorinating the parachlorotoluene; and (c) separating components. According to the method, a mixture of iron powder, aluminum trichloride and a L-type molecular sieve is taken as the catalyst for a chlorination reaction, so that the selectivity for 2,4-dichlorotoluene is effectively promoted. The production of poly-chlorotoluene such as benzotrichloride and tetrachlorotoluene is effectively inhibited due to a low reaction temperature, and the yield of 2,4-dichlorotoluene is improved. Moreover, the method is simple and convenient; the operation is easy; the effects are good; and the product yield is high.

Description

technical field [0001] The invention belongs to the technical field of organic chemistry and relates to a method for producing 2,4-dichlorotoluene from p-chlorotoluene. Background technique [0002] 2,4-Dichlorotoluene is a colorless and transparent liquid. It is an important chemical raw material, mainly used in organic synthesis, pharmaceutical and dye industries, and is also a good high-boiling organic solvent. At present, the synthesis routes at home and abroad mainly include the following: kind: [0003] (1) Using p-chlorotoluene and chlorine gas as raw materials, it is prepared by chlorination reaction under the catalysis of Lewis acid. The method has low selectivity of 2,4-dichlorotoluene in industrial production, many by-products, many acid waste water, and large catalyst consumption. [0004] (2) Obtained by isomerization of dichlorotoluene, and the isomerized products are separated by mesoporous molecular sieves. The production cost of this method is relatively h...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C25/08C07C17/12C07C17/35B01J29/76
Inventor 钟华陆敏山陈秀珍蔡伟忠
Owner NANJING ZHONGTENG CHEM
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