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Preparation for 6-chlorine-2-trichloromethyl pyridine

A technology of trichloromethylpyridine and picoline, applied in the direction of organic chemistry, can solve problems such as atmospheric environmental hazards, difficult industrialization, and impracticality, and achieve the goals of improving soil and plant nutrition, economical industrial production, and delaying nitrification Effect

Inactive Publication Date: 2008-12-03
ZHEJIANG AOFUTUO CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the patent No. is US4577027, the patent name is that the method introduced in "2-picoline direct liquid-phase chlorination method to produce polychlorinated pyridine mixture" is different from the methods in these documents in the past, but the patent No. is that US4577027 introduces in 100-250°C, at CCL 4 The reaction of chlorine with 2-picoline in the presence of a diluent is also impractical to obtain a mixture enriched in 6-chloro-2-trichloropicoline, which has many by-products, diluent CCL 4 A large amount of loss will cause great harm to the atmospheric environment, and after 2010 CCL 4 It will be banned from production and use, and it is also difficult to industrialize the method

Method used

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  • Preparation for 6-chlorine-2-trichloromethyl pyridine
  • Preparation for 6-chlorine-2-trichloromethyl pyridine
  • Preparation for 6-chlorine-2-trichloromethyl pyridine

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Embodiment 1

[0024] The method for preparing 6-chloro-2-trichloromethylpyridine in this embodiment mainly adopts gaseous chlorine and 2-picoline as raw materials, and adopts continuous reaction, such as figure 1 As shown, first add 200L liquid 2-picoline hydrochloride as initiator in the first reactor 1 (500L glass-lined reactor), raise the temperature to 195°C and start to feed excess chlorine gas, wherein Cl 2 Feed in at 25 kg / hour per hour, and 2-picoline is dripped on the inner wall of the second reactor 2 from the second reactor 2 along the introduction pipe 9 at 2.5 kg / hour per hour. Gaseous chlorine gas and 2-picoline hydrochloride react to generate HCL gas, HCL gas leaves the first reactor 1 and enters the second reactor 2, and reacts with 2-picoline on the inner wall of the second reactor 2 to generate 2 - picoline hydrochloride with exotherm. The second reactor 2 is temperature-controlled, using tap water as the jacket cooling water, so that the heat generated during salt format...

Embodiment 2

[0032] The method and basic steps of present embodiment and embodiment 1 are identical, adopt continuous reaction, as figure 1 shown, where changing CL 2The weight ratio to the introduced amount of 2-picoline was 4:1, chlorine gas was introduced at 10 kg / hour, and 2-picoline was introduced at a rate of 2.5 kg / hour. Reaction temperature reaches steady state in 36 hours at 195°C; the material composition when reaching steady state is 15% of 2-trichloromethylpyridine, 4.3% of 3,6-dichloro-2-trichloromethylpyridine, 6- The content of chloro-2-trichloromethylpyridine is 80%. This mixture is introduced into the chlorination reactor 10 to continue the chlorination reaction, and is irradiated with an ultraviolet lamp at a reaction temperature of 170° C. for a total of 8 hours to finally obtain A mixture of 92% chloromethylpyridine, 6.5% 3,6-dichloro-2-trichloromethylpyridine and 1.5% other impurities. Volatile matter is 85%.

Embodiment 3

[0034] The method and basic steps of present embodiment and embodiment 1 are identical, adopt continuous reaction, as figure 1 shown, where changing CL 2 The introduction weight ratio of 2-picoline was 2:1. Chlorine gas is introduced at a speed of 5 kg / hour, and 2-picoline is introduced at a speed of 2.5 kg / hour. After the reaction reaches 6 hours, it is carbonized into a black sticky tar substance. Volatile matter is 15%.

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Abstract

The invention discloses a method for preparing 6-chloro-2-trichloromethyl pyridine. The method includes the steps as follows: gaseous chlorine and 2-methylpyridine are adopted as the raw materials; initiator is added to a first reactor, and excessive gaseous chlorine is introduced into the reactor; the gaseous chlorine and the initiator react to produce HCl gas which rises into a second reactor, and is in convection with 2-methylpyridine to produce 2-methylpyridine hydrochloride under a temperature-control condition; the hydrochloride returns to the first reactor and reacts with the excessive gaseous chlorine to produce 2-trichloromethylpyridine which reacts with continuously-introduced excessive gaseous chlorine at a certain temperature until the reaction reaches a stable state to obtain a volatile 6-chloro-2-trichloromethyl pyridine enriched mixture; the mixture is extracted from the kettle bottom and refined to obtain 6-chloro-2-trichloromethyl pyridine compound; and a tail-gas recovery device is connected with the second reactor. The method has the advantages of high selectivity, high yield and environment friendliness.

Description

technical field [0001] The invention relates to a preparation method of 6-chloro-2-trichloromethylpyridine. Background technique [0002] Because 6-chloro-2-trichloromethylpyridine can be used as an intermediate of medicine and pesticides, especially in the field of fertilizers, it can be used to improve agricultural nitrogen fertilizer, delay the nitrification of NH4+, and improve soil and plant nutrition. . Therefore, people wish to find a high-efficiency preparation method. The methods for preparing 6-chloro-2-trichloromethylpyridine-enriched mixtures reported in the past include: the patent No. is US3424754, the patent name is "Preparation of 2-chloro-6-trichloromethylpyridine" and the patent No. It is US3420833, and the patent name is "Production of Polychlorinated Pyridine Compounds by Gas Phase Method". The patent No. is US3424754 by passing 2-picoline hydrochloride into chlorine gas, reacting at 200°C to obtain a 75% volatile mixture containing 90% 6-chloro-2-tric...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D213/61
CPCC07D213/61
Inventor 戴锋
Owner ZHEJIANG AOFUTUO CHEM
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