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Process for preparing symmetric tetrachloro pyridine

A technology of tetrachloropyridine and chloropyridine is applied in the preparation field of symmetrical tetrachloropyridine, can solve the problems of low yield of symmetrical tetrachloropyridine, high reaction temperature and high production cost, achieves large industrial practical value and simple process , The effect of low production cost

Inactive Publication Date: 2007-04-11
盐城恒盛化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Chinese patent CN1421436 introduces the use of pentachloropyridine as a starting material, and in the presence of inorganic ammonium salts, it is reduced to tetrachloropyridine with zinc or iron powder in a solvent, because pentachloropyridine is obtained by reacting pyridine or polychloropyridine with chlorine gas Compared with directly making symmetrical tetrachloropyridine with pyridine or polychloropyridine and chlorine, it is obviously uneconomical from the perspective of raw material utilization, which will inevitably lead to excessive production costs of products
Chinese patent CN1421435 discloses the production technique that uses pyridine and chlorine as starting raw material to prepare symmetrical tetrachloropyridine, but the reaction product that obtains is the mixture of tetrachloropyridine (about 60%) and pentachloropyridine (about 38%) or The mixture with pentachloropyridine as the main component still needs to undergo reduction reaction to obtain tetrachloropyridine. In addition, the reaction temperature of this preparation method is too high (270-500 ° C), which also increases the difficulty of practical application.
But there is not high (81.21%) that causes the total yield of symmetric tetrachloropyridine because of the longer process route, and the deficiency that content is on the low side (93%)

Method used

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  • Process for preparing symmetric tetrachloro pyridine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Add 325.6g of 2,6-dichloropyridine, 90.8g of 2-chloropyridine, chlorine Fe 20g, heat until the material melts, turn on the stirrer, continue heating to 170°C, start to feed chlorine gas, keep the temperature and pressure in the primary reactor at about 200°C and 0.04Mpa respectively, and the secondary reactor And the temperature and pressure in the third-stage reactor are about 200°C and about 0.075Mpa, and the appropriate material reflux velocity is controlled, and at the same time, the tail gas in the third-stage reactor is controlled to be free of unreacted chlorine. When the content of symmetrical tetrachloropyridine in the material in the primary reactor reaches 40%, keep other reaction conditions unchanged, but control the temperature and pressure in the primary reactor at about 215°C and 0.06Mpa respectively; And when the content of symmetrical tetrachloropyridine in the material in the primary reactor reaches 80%, it is necessary to control the temperature and p...

Embodiment 2

[0025] The equipment and feeding method are the same as in Example 1, but the initial feeding amount in the reactor is changed to 2,6-dichloropyridine 444g, ferric chloride 20g, and the operation mode is the same as in Example 1. When the primary reactor reaches the end of the reaction , to obtain 670 g of the reaction mixture material, which contains 97.01% of the chlorinated product. GC analysis showed that it contained 97.24% of symmetrical tetrachloropyridine, 0.89% of 2,3,6-trichloropyridine, 1.78% of pentachloropyridine, and 0.09% of other chloropyridine. The conversion rate of symmetrical tetrachloropyridine is 97.14%.

Embodiment 3

[0027]The equipment and feeding method are the same as in Example 1, but the initial feeding amount in the reactor is changed to 485.2 g of polychloropyridine mixture (containing 3-chloropyridine 7.06%, 2-chloropyridine 4.68%, 3,5-dichloropyridine 6.10%, 2,6-dichloropyridine 67.11%, 2,3,5-trichloropyridine 9.39%, 2,3,6-trichloropyridine 5.66%), iron trichloride 22g, the operation method is the same as in Example 1, when a When the first-stage reactor reaches the end of the reaction, 738.8 g of the reaction mixture material can be obtained, which contains 97.02% of the chlorinated product. GC analysis showed that it contained 96.92% of symmetrical tetrachloropyridine, 0.94% of 2,3,6-trichloropyridine, 2.07% of pentachloropyridine, and 0.07% of other chloropyridine. The conversion rate of symmetrical tetrachloropyridine is 97.01%.

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Abstract

The process of preparing symmetric tetrachloro pyridine includes the chlorination reaction of chloro pyridine containing 1-3 chlorine atoms and chlorine at 170-250 deg.c in the presence of iron powder or Lewis acid as catalyst for 8-48 hr. The preparation process uses chlorine in the liquid phase chlorination reaction to chlorinate chloropyridine, dichloropyridine, trichloropyridine, etc, and has single pass conversion rate up to 97 %, simple technological process, low production cost and excellent industrial application value.

Description

(1) Technical field [0001] The invention relates to a preparation method of symmetrical tetrachloropyridine. (2) Background technology [0002] Symmetrical tetrachloropyridine, also known as 2,3,5,6-tetrachloropyridine, has a molecular structure as shown in the figure below: [0003] [0004] Due to the presence of multiple electron-withdrawing groups in its molecular structure, the chlorine at the 2-position has a relatively high reactivity and becomes a commercially valuable pyridine derivative, which can be used in the synthesis of herbicides, fungicides and insecticides . Because symmetric tetraclopyridine can be used as an important starting material for the highly efficient, low-toxicity, broad-spectrum insecticide "chlorpyrifos", which ranks first in terms of sales volume and sales in the world, so far, domestic and foreign industry insiders have little interest in this chemical. A large amount of research has been done in the preparation, and multiple preparatio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D213/61
Inventor 冯亚华周宗祥
Owner 盐城恒盛化工有限公司
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