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Crystallization method of azoxystrobin

A technology of azoxystrobin and crystallization, applied in the crystallization field of azoxystrobin, can solve the problems of difficult filtration, long filtration time and high purity, and achieve the effects of low moisture content, fast filtration speed and high purity of the product

Pending Publication Date: 2022-05-13
NUTRICHEM LAB CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The object of the present invention is to provide a kind of crystallization method of azoxystrobin in order to overcome the problem that the crystal grain of butyl acetate crystallization existing in the prior art is small, filtration difficulty, long filtration time etc., the crystal grain of the crystallization obtained by this method Large, fast filtration with low product moisture content and high purity

Method used

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  • Crystallization method of azoxystrobin
  • Crystallization method of azoxystrobin
  • Crystallization method of azoxystrobin

Examples

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Effect test

preparation example 1

[0051] Add 200 g of azoxystrobin in butyl acetate solution (the content of azoxystrobin is 30% by weight) in a 500ml reaction bottle, heat up to 70°C to completely dissolve; control the temperature to 66°C, slowly cool down to 45°C in 4 hours, and keep warm After 2 hours, the solid product obtained by filtration was used as a seed crystal (hereinafter also referred to as seed crystal A).

[0052] figure 1 It is the X-ray powder diffraction pattern measured by Cu-Kα radiation at 25° C. for seed crystal A in Preparation Example 1. Such as figure 1 As shown, the 2θ values ​​of the X-ray powder diffraction pattern measured by Cu-Kα radiation of the seed crystal A at 25°C are at 7.5±0.2, 8.5±0.2, 13.3±0.2, 13.9,±0.2, 14.6±0.2, 18.2 ±0.2°, 18.5±0.2°, 19.0±0.2°, 20.6±0.2°, 21.4±0.2°, 22.5±0.2°, 22.7±0.2°, 24.4±0.2°, 26.3±0.2°, 26.8±0.2°, There are characteristic peaks at 28.8±0.2° and 30.8±0.2°.

[0053] Add 60 g of crude azoxystrobin and 200 ml of methanol into a 500 ml reaction...

Embodiment 1

[0056] Add 500 g of azoxystrobin butyl acetate solution (azoxystrobin content is 30% by weight) in a 1000 ml reaction bottle, heat up to 70° C. to completely dissolve, then cool down to 66° C., add 2 g of seed A, and keep stirring for 30 Minutes for the first stage of crystallization; then, take 5 hours to cool down to 45°C, keep warm for 2 hours to carry out the second stage of crystallization; then, take 5 hours to cool down to 5°C, keep warm for 30min for the third stage of crystallization; the third stage crystallization product Suction filtration was carried out, which took about 15 minutes, and the obtained crystals had an measured moisture content of 13% by weight. Sampling microscope shows as figure 2 As shown, the size of its crystals is 100-700um.

Embodiment 2

[0058] Add 500 g of butyl acetate solution of azoxystrobin (the content of azoxystrobin is 27% by weight) in a 1000 ml reaction bottle, heat up to 70° C. to completely dissolve, then cool down to 64° C., add 2 g of seed A, and keep stirring for 60 Minutes for the first stage of crystallization; then, take 5 hours to cool down to 45°C, keep warm for 1 hour to carry out the second stage of crystallization; then, take 5 hours to cool down to 5°C, keep warm for 30min to carry out the third stage of crystallization; the third stage crystallization product Suction filtration was carried out for about 15 minutes, and the moisture content of the obtained crystals was determined to be 13% by weight, and the crystal size was 150-800um.

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Abstract

The invention relates to the field of pesticide bactericides, and discloses a crystallization method of azoxystrobin. The crystallization method of the azoxystrobin comprises the following steps: 1) adding a seed crystal into a butyl acetate solution containing the azoxystrobin at the temperature of 60-68 DEG C, and carrying out first-stage crystallization; 2) cooling the product of the first-stage crystallization to 40-50 DEG C, and carrying out second-stage crystallization; and 3) cooling the product of the second-stage crystallization to 0-25 DEG C, and carrying out third-stage crystallization. The crystals obtained through the method are large in crystal grain, high in filtering speed, low in moisture content and high in purity.

Description

technical field [0001] The invention relates to the field of pesticide fungicides, in particular to a method for crystallizing azoxystrobin. Background technique [0002] Most of the purification methods of azoxystrobin use methanol crystallization, for example, in WO2002100837A, CN103145627A and CN102276538A, methanol is used as the purification solvent. The advantage of methanol crystallization is that it is cheap and easy to dry, but it has the disadvantage of dark product color, and the purification effect on product impurities is not ideal. [0003] CN103265496A discloses crystallization solvent with butyl acetate solvent, which has good purification effect and high yield. However, there are problems such as small crystal grains, difficulty in filtration, and long filtration time, which will affect the actual production capacity in the industrial production process. Contents of the invention [0004] The object of the present invention is to provide a kind of crysta...

Claims

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Application Information

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IPC IPC(8): C07D239/52
CPCC07D239/52C07B2200/13
Inventor 王龙赵永长闫涛孙自培潘俊辛郑亚彬乔振王磊汪春华
Owner NUTRICHEM LAB CO LTD