WO2012024920A1 - Method for preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole - Google Patents

Method for preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole Download PDF

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WO2012024920A1
WO2012024920A1 PCT/CN2011/071577 CN2011071577W WO2012024920A1 WO 2012024920 A1 WO2012024920 A1 WO 2012024920A1 CN 2011071577 W CN2011071577 W CN 2011071577W WO 2012024920 A1 WO2012024920 A1 WO 2012024920A1
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acidic medium
acid
solid
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赵永长
于慧梅
宋蕾
朱笑坤
陈建伟
王文军
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NUTRICHEM INTERNATIONAL CO Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D231/00Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings
    • C07D231/02Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings
    • C07D231/10Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D231/14Heterocyclic compounds containing 1,2-diazole or hydrogenated 1,2-diazole rings not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D231/44Oxygen and nitrogen or sulfur and nitrogen atoms

Definitions

  • the present invention relates to a process for the preparation of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole. Background technique
  • fipronil The structure of fipronil is novel and its mechanism of action is unique. Its mechanism is mainly to control the metabolism of chloride by ⁇ -aminobutyric acid (GABA) receptor. It has contact, stomach poisoning and moderate systemic action. It is on lepidoptera and flies. A series of pests such as the genus Coleoptera have high insecticidal activity. Moreover, it has many advantages such as no cross-resistance and safety of use with existing insecticides.
  • GABA ⁇ -aminobutyric acid
  • the agent can be applied to the soil or foliar spray: Applying to the soil can effectively control the corn root beetle, golden worm and the ground tiger; when the leaf is sprayed, it has high levels of the diamondback moth, the cabbage butterfly, the rice glutinous horse, etc. It is effective and has a long-lasting effect.
  • 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylthiopyrazole is an important intermediate for the preparation of fipronil, After the trifluoromethylthio group of the intermediate is oxidized to a trifluoromethylsulfinyl group, fipronil is obtained.
  • the object of the present invention is to overcome the shortcomings of the prior art solvent recovery, and to provide a solvent-recoverable preparation of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl). a method of 4-trifluoromethylsulfinylpyrazole.
  • CN1332730A proposes to recover trifluoroacetic acid by adding chlorobenzene and distilling off trifluoroacetic acid, it is inevitable to introduce a large amount of water into the reaction system by using hydrogen peroxide as an oxidizing agent. Acetic acid and water easily form an azeotropic mixture, so that the recovered trifluoroacetic acid is contained There is a large amount of water, plus trifluoroacetic acid and water miscible, the recovered trifluoroacetic acid has a water content of more than 8%.
  • the invention provides a preparation method of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole,
  • the 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole has the formula ( ⁇ ) shown below Structure:
  • the preparation method of the 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole comprises an acidic medium
  • the solid oxidant is represented by the formula (I)
  • the invention adopts a solid oxidant instead of hydrogen peroxide as an oxidant, reduces the water content in the recovered acidic medium (such as trifluoroacetic acid), realizes the recycling of an acidic medium (such as trifluoroacetic acid), and is suitable for industrial production. Further, the method of the present invention has the advantages of mild reaction conditions and high safety by using a solid oxidizing agent instead of hydrogen peroxide as an oxidizing agent. Detailed ways
  • the compound represented by the following formula (I) is contacted with a solid oxidizing agent in the presence of an acidic medium, and the reaction medium is recovered to obtain a compound represented by the formula ( ⁇ ).
  • the reaction process is as follows:
  • the molar ratio of the compound of the formula (I) to the solid oxidizing agent may be 1: 0.9-6.0, preferably 1 : 1-3, more preferably 1: 1.2 - 1.7, still more preferably 1: 1.3 - 1.5.
  • the solid oxidizing agent may be various oxidizing agents capable of oxidizing a trifluoromethylthio group to a trifluoromethylsulfinyl group at room temperature, preferably including sodium perborate, potassium peroxymonosulfate or sodium percarbonate. And one or more of calcium peroxide and magnesium peroxide, further preferably potassium peroxymonosulfate and/or sodium perborate, wherein the sodium perborate may be hydrated sodium perborate having 1 or 4 crystal waters. .
  • the acidic medium may be a liquid acidic medium and may be selected from one or more of the organic carboxylic acids having the following structural formula:
  • R is halogen or hydrogen
  • R, X, and Y may be the same or different.
  • the halogen may be fluorine, chlorine, bromine or iodine, preferably fluorine.
  • the acidic medium may be one or more of trifluoroacetic acid, difluoroacetic acid, dichloroacetic acid, monofluorodichloroacetic acid and difluoromonochloroacetic acid, further preferably trifluoroacetic acid, difluoroacetic acid One or more of acetic acid and difluoromonochloroacetic acid.
  • the present inventors have found that while using at least one of R, X and Y as an acidic medium of fluorine, hydrated sodium perborate having one or four crystal waters is used as a solid oxidant, and the recovery is lowered.
  • the water content of the acidic medium also reduces the corrosion of the glass container. This may be due to the presence of by-product sodium borate or, possibly, due to the lower water content in the reaction system, which inhibits the production of small amounts of hydrofluoric acid by-products from the fluorine-containing acidic medium, thereby reducing corrosion of the glass container.
  • the acidic medium be an acidic medium in which at least one of R, X and Y is fluorine, and the solid oxidant is hydrated sodium perborate.
  • the inventors have also found that when dichloroacetic acid is used as an acidic medium, compared with the use of a fluorine-containing acidic medium, Reduces corrosion of the glass container.
  • the reason may be that a small amount of hydrofluoric acid by-product produced by a fluorine-containing acidic medium corrodes the glass container, and the use of dichloroacetic acid does not cause corrosion of the glass container due to the absence of the above-mentioned hydrofluoric acid by-product.
  • the use of dichloroacetic acid in combination with various solid oxidants does not present the problem of corrosion of the glass container. Therefore, in the present invention, it is also preferred that the acidic medium is dichloroacetic acid.
  • an aqueous solution of sulfuric acid when used as an acidic medium, it also has better selectivity and yield, and, compared to trifluoroacetic acid, difluoroacetic acid, dichloroacetic acid, monofluorodichloroacetic acid, difluoroacetic acid.
  • An acidic medium such as monochloroacetic acid, which is much easier to obtain in an aqueous solution of sulfuric acid and which is relatively inexpensive, is more suitable for industrial production. Therefore, the acidic medium may also be an aqueous sulfuric acid solution, and the aqueous sulfuric acid solution may have a concentration of 70 to 90% by weight, preferably 80 to 88% by weight.
  • the weight ratio of the compound of the formula (I) to the acidic medium may be from 1:2 to 10, preferably from 1:3 to 8, more preferably from 1:3.5 to 5.
  • the oxidation reaction condition of the compound represented by the formula (I) and the solid oxidizing agent may be carried out by adding the compound of the formula (I) to an acidic medium at -10 ° C to 50 ° C until it is sufficiently dissolved.
  • the solid oxidizing agent is added, and the reaction temperature may be -10 ° C to 50 ° C, preferably 5 to 20 ° C, and more preferably 8 to 12 ° C.
  • the reaction time may be from 1 to 48 hours, preferably from 4 to 6 hours.
  • the oxidizing agent is added in portions, which is more favorable for improving the selectivity of the reaction.
  • the solid oxidizing agent may be added in 3 to 6 portions, wherein the first time is added to the solid oxidizing agent equimolar to the compound represented by the formula (I), and the remaining amount of the solid oxidizing agent may be equally divided into 2 to 5 parts.
  • the mixture obtained by contacting the solid oxidizing agent with the compound of the formula (I) may be contacted with a reducing agent to remove excess oxidizing agent.
  • the reducing agent may be one or more of insurance powder, sodium sulfite, sulfur dioxide and other reducing agents, preferably insurance powder and/or sodium sulfite.
  • the reducing agent is added in such a manner that the amount of the reducing agent is added so as to be able to remove the excess oxidizing agent.
  • a reducing agent may be added so that the mixture just does not allow the starch potassium iodide test paper to change color.
  • the acidic medium when the acidic medium is an organic carboxylic acid represented by the above structural formula, the acidic medium can be distilled off under reduced pressure after removing an excessive amount of the oxidizing agent.
  • the reaction liquid after removing excess oxidant may be diluted with water at a temperature of -5 ° C to 5 ° C, and then filtered to obtain a solid.
  • the product wherein the weight ratio of the amount of water used for dilution to the aqueous solution of sulfuric acid is 1-3:1.
  • the method provided by the present invention may further comprise recrystallizing the product after distilling off the acidic medium under reduced pressure.
  • the solvent used for the recrystallization may be one or more of toluene, chlorobenzene, ethyl acetate, and an alcohol having 1 to 4 carbon atoms.
  • the method of recrystallization may be: firstly purifying the solid product of the acidic medium under water pressure to remove residual acid and inorganic salt, and then dissolving the solid product by heating with a solvent until the solid is completely dissolved, and slowly cooling the clear solution. Recrystallization from 0 to 5 ° C, then at 0-5 ° C for 2 hours, filtering to obtain crystal Body product.
  • the amount of water for washing may be 0.8 to 3 parts by weight
  • the amount of solvent used for recrystallization may be 0.2 to 2 parts by weight, based on 1 part by weight of the product obtained by distilling off the acidic medium under reduced pressure.
  • the present invention is more advantageous in the recovery of trifluoroacetic acid than the hydrogen peroxide and trifluoroacetic acid systems because of the large amount of water present in the system due to oxidation using a solid oxidizing agent.
  • the solid obtained by filtration was heated to 300 g of chlorobenzene to completely dissolve, and then slowly cooled at 0-5 ° C, and then kept for 2 hours, filtered and dried to obtain 122 g of a white solid, which was detected by GC.
  • the main component of the white solid is 5-amino-3-cyano- 1-(2,6-Dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole having a purity of 95% and a yield of 93%.
  • the temperature of the reaction system was maintained at 10-12 ° C, and 49.9 g (concentration: 30%, 0.44 mol) H 2 0 2 was slowly added dropwise, time control At 2h; keep the temperature at 10-12 ° C for 5h, GC to monitor the completion of the reaction, until the conversion of raw materials is greater than 98%; add 350g of chlorobenzene, azeotropic distillation under reduced pressure to recover a mixture of trifluoroacetic acid, chlorobenzene and water 440 g of trifluoroacetic acid having a water content of 8.5% was obtained by liquid separation. After the azeotropic distillation under reduced pressure, the chlorobenzene was distilled under reduced pressure until no fraction was obtained.
  • the reaction was further incubated for 3 hours, and the degree of reaction was monitored by GC until the conversion of the raw material was more than 98%, and sodium sulfite was added in portions. In order to remove the oxide, (0.1g per batch), the reaction was terminated. The total amount of sodium sulfite added was such that the reaction system could not change the color of the starch potassium iodide test paper, and the mixture was stirred for 5 minutes, and trifluoroacetic acid was distilled under reduced pressure to obtain water content.
  • the reaction was further incubated for 3 h, and the degree of completion of the reaction was monitored by GC until the conversion of the raw material was more than 99%, and sodium sulfite was added in portions to remove the oxide (0.1 g per batch) to terminate the reaction.
  • the degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and sodium sulfite was added in portions to remove the oxide (0.1 g per batch). To terminate the reaction. Control the batch or total amount of sodium sulfite added, so that the reaction system can not just change the color of the starch potassium iodide test paper, stir for 5 minutes, dichloroacetic acid is distilled off under reduced pressure to obtain 420 g of anhydrous dichloroacetic acid.
  • the degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and sodium sulfite was added in portions to remove oxides (0.1 g per batch). To terminate the reaction. Control the batch or total amount of sodium sulfite added so that the reaction system just does not change the color of the starch potassium iodide test paper, stir for 5 minutes, and recover by distillation under reduced pressure to obtain a water content of less than 2% by weight of trifluoroacetic acid.
  • the white solid was mainly 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoro Methylsulfinylpyrazole, purity 96%, yield 89.2%.
  • the above experiment was repeated 10 times using the above 1000 ml reaction flask, and it was found that the bottom of the reaction bottle contacting the reaction solution was no longer transparent and the edges were blurred, indicating that the reaction system had a certain glass. Corrosion effect.
  • the degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and the SO 2 gas was introduced to remove the oxide to terminate the reaction. Control the total amount of S0 2 gas inflow, so that the reaction system just can not make the starch potassium iodide test paper discoloration, stir for 5 minutes, put the reaction bottle in an ice water bath, add 1800g water to the reaction droplet, at the reaction liquid temperature After being reduced to 0 °, it was filtered to give a white solid, 110 g, which was determined by GC.
  • the main component of the white solid was 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl) -4-trifluoromethylsulfinylpyrazole, purity 91%, yield 84%.

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Abstract

Disclosed is a method for preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole (Fipronil) (II). This method comprises oxidating 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylthiopyrazole (formula (I)) used as a material by a solid oxidant in an acidic medium, recovering the reaction medium and obtaining Fipronil.

Description

一种制备 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基 吡唑的方法  Method for preparing 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole

技术领域 Technical field

本发明涉及一种制备 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲 基亚磺酰基吡唑的方法。 背景技术  The present invention relates to a process for the preparation of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole. Background technique

5-氨基 -3-氰基小 (2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 商品 名为锐劲特, 通用名氟虫腈, 是法国罗纳-普朗克公司于 1987-1989年研制开发 的苯基吡唑类杀虫剂。  5-amino-3-cyano small (2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole, trade name Regent, common name Nitrile, a phenylpyrazole insecticide developed by Rhône-Planck in France from 1987 to 1989.

氟虫腈结构新颖, 作用机理独特, 其机理主要是以 γ-氨基丁酸 (GABA)受体 为靶标控制氯化物代谢, 具有触杀、 胃毒和中度内吸作用, 对鳞翅目、 蝇类和鞘 翅目等一系列害虫具有很高的杀虫活性。而且具有与现有杀虫剂无交互抗性、使 用安全等多个优点。 该药剂可施于土壤, 也可叶面喷雾: 施于土壤能有效防治玉 米根叶甲、 金针虫和地老虎; 叶面喷洒时, 对小菜蛾、 菜粉蝶、 稻蓟马等均有高 水平防效, 且持效期长。  The structure of fipronil is novel and its mechanism of action is unique. Its mechanism is mainly to control the metabolism of chloride by γ-aminobutyric acid (GABA) receptor. It has contact, stomach poisoning and moderate systemic action. It is on lepidoptera and flies. A series of pests such as the genus Coleoptera have high insecticidal activity. Moreover, it has many advantages such as no cross-resistance and safety of use with existing insecticides. The agent can be applied to the soil or foliar spray: Applying to the soil can effectively control the corn root beetle, golden worm and the ground tiger; when the leaf is sprayed, it has high levels of the diamondback moth, the cabbage butterfly, the rice glutinous horse, etc. It is effective and has a long-lasting effect.

5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲硫基吡唑是制备氟虫 腈的重要中间体,将该中间体的三氟甲硫基氧化为三氟甲基亚磺酰基后, 即得到 氟虫腈。  5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylthiopyrazole is an important intermediate for the preparation of fipronil, After the trifluoromethylthio group of the intermediate is oxidized to a trifluoromethylsulfinyl group, fipronil is obtained.

早期的文献报道中, 采用间氯过氧苯甲酸和 /或双氧水作氧化剂, 二氯甲烷 作溶剂,将 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲硫基吡唑氧化成 氟虫腈, 这种方法的缺点是, 所需时间较长, 大约需要 2天, 同时使用的间氯过 氧苯甲酸相当昂贵, 难以进行大规模工业化生产。  In the early literature, 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoro) was obtained using m-chloroperoxybenzoic acid and/or hydrogen peroxide as the oxidizing agent and dichloromethane as the solvent. Oxidation of methylphenyl)-4-trifluoromethylthiopyrazole to fipronil. The disadvantage of this method is that it takes a long time, about 2 days, and the use of m-chloroperoxybenzoic acid is quite expensive. It is difficult to carry out large-scale industrial production.

文献 CN1332730A公开了采用三氟乙酸作溶剂,双氧水作氧化剂,发现有较 好的选择性和收率。但是三氟乙酸溶剂本身相当昂贵, 使用时必须回收套用, 才 能实现真正的工业化生产。然而,实验证明,该方法中三氟乙酸的回收相当困难。 发明内容  Document CN1332730A discloses the use of trifluoroacetic acid as a solvent and hydrogen peroxide as an oxidizing agent, and it has been found to have better selectivity and yield. However, the trifluoroacetic acid solvent itself is quite expensive and must be recycled for use in order to achieve true industrial production. However, experiments have shown that the recovery of trifluoroacetic acid in this process is quite difficult. Summary of the invention

本发明的目的在于克服现有技术溶剂回收困难的缺点,提供一种溶剂回收容 易的制备 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑 的方法。  The object of the present invention is to overcome the shortcomings of the prior art solvent recovery, and to provide a solvent-recoverable preparation of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl). a method of 4-trifluoromethylsulfinylpyrazole.

本发明的发明人发现,尽管 CN1332730A提出了通过加入氯苯,蒸去三氟乙 酸的方法来回收三氟乙酸,但由于采用双氧水作氧化剂, 不可避免地在反应体系 中引入大量的水,三氟乙酸和水容易形成共沸混合物, 使得回收的三氟乙酸中含 有大量的水, 再加上三氟乙酸与水互溶, 回收的三氟乙酸含水量在 8%以上。 同 时,用含水的三氟乙酸作溶剂进行氟虫腈的氧化反应,以及使用双氧水作氧化剂, 都会在氧化反应体系中引入大量的水,从而导致反应转化率和选择性较低。因此, 难以实现三氟乙酸的循环利用。 The inventors of the present invention have found that although CN1332730A proposes to recover trifluoroacetic acid by adding chlorobenzene and distilling off trifluoroacetic acid, it is inevitable to introduce a large amount of water into the reaction system by using hydrogen peroxide as an oxidizing agent. Acetic acid and water easily form an azeotropic mixture, so that the recovered trifluoroacetic acid is contained There is a large amount of water, plus trifluoroacetic acid and water miscible, the recovered trifluoroacetic acid has a water content of more than 8%. At the same time, the oxidation reaction of fipronil with aqueous trifluoroacetic acid as a solvent and the use of hydrogen peroxide as an oxidant introduce a large amount of water into the oxidation reaction system, resulting in low reaction conversion and selectivity. Therefore, it is difficult to achieve recycling of trifluoroacetic acid.

本发明提供了一种 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基 亚磺酰基吡唑的制备方法,该 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟 甲基亚磺酰基吡唑具有如下式 (Π) 所示的结构:  The invention provides a preparation method of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole, The 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole has the formula (Π) shown below Structure:

Figure imgf000003_0001
Figure imgf000003_0001

( 11 )。  (11).

其中,该 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡 唑的制备方法包括在酸性介质中, 在氧化反应条件下, 使固态氧化剂与式 ( I ) 所示  Wherein the preparation method of the 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole comprises an acidic medium In the oxidation reaction conditions, the solid oxidant is represented by the formula (I)

Figure imgf000003_0002
Figure imgf000003_0002

( I )  (I)

本发明采用固态氧化剂代替双氧水做氧化剂, 降低了回收的酸性介质(如三 氟乙酸) 中的含水量, 实现了酸性介质(如三氟乙酸) 的循环使用, 适于进行工 业化生产。 并且, 本发明的方法通过采用固态氧化剂代替双氧水做氧化剂, 具有 反应条件温和、 安全性高的优点。 具体实施方式  The invention adopts a solid oxidant instead of hydrogen peroxide as an oxidant, reduces the water content in the recovered acidic medium (such as trifluoroacetic acid), realizes the recycling of an acidic medium (such as trifluoroacetic acid), and is suitable for industrial production. Further, the method of the present invention has the advantages of mild reaction conditions and high safety by using a solid oxidizing agent instead of hydrogen peroxide as an oxidizing agent. Detailed ways

按照本发明, 在酸性介质存在下, 将下式( I )所示的化合物与固态氧化剂 接触, 回收反应介质, 分离得到式 (Π ) 所示的化合物, 反应过程如下式所示: According to the present invention, the compound represented by the following formula (I) is contacted with a solid oxidizing agent in the presence of an acidic medium, and the reaction medium is recovered to obtain a compound represented by the formula (Π). The reaction process is as follows:

Figure imgf000004_0001
按照本发明, 所述式 ( I ) 化合物与固态氧化剂的摩尔比可以 1 : 0.9-6.0, 优选可以为 1 : 1-3, 进一步优选为 1 : 1.2-1.7, 更进一步优选为 1 : 1.3-1.5。
Figure imgf000004_0001
According to the present invention, the molar ratio of the compound of the formula (I) to the solid oxidizing agent may be 1: 0.9-6.0, preferably 1 : 1-3, more preferably 1: 1.2 - 1.7, still more preferably 1: 1.3 - 1.5.

按照本发明,固态氧化剂可以为各种能够将三氟甲硫基氧化为三氟甲基亚磺 酰基的常温下成固态的氧化剂, 优选可以包括过硼酸钠、 过一硫酸氢钾、 过碳酸 钠、 过氧化钙、 过氧化镁中的一种或多种, 进一步优选为过一硫酸氢钾和 /或过 硼酸钠, 其中过硼酸钠可以为具有 1个或者 4个结晶水的水合过硼酸钠。  According to the present invention, the solid oxidizing agent may be various oxidizing agents capable of oxidizing a trifluoromethylthio group to a trifluoromethylsulfinyl group at room temperature, preferably including sodium perborate, potassium peroxymonosulfate or sodium percarbonate. And one or more of calcium peroxide and magnesium peroxide, further preferably potassium peroxymonosulfate and/or sodium perborate, wherein the sodium perborate may be hydrated sodium perborate having 1 or 4 crystal waters. .

所述酸性介质可以为液态酸性介质,可以选自具有如下结构式的有机羧酸中 的一种或多种:

Figure imgf000004_0002
The acidic medium may be a liquid acidic medium and may be selected from one or more of the organic carboxylic acids having the following structural formula:
Figure imgf000004_0002

R表示 ^到 C6 (优选 d到 C4) 的烷基、 d到 C6 (优选 d到 C4) 的卤代 烃基、 卤素或者氢, X和 Y表示卤素或者氢。 更优选 R、 X和 Y中至少之一为 卤素。 Represents R ^ to C 6 (d preferably to C 4) alkyl, d to C 6 (d preferably to C 4) a halogenated hydrocarbon group, a halogen or a hydrogen, X and Y represents a halogen or hydrogen. More preferably, at least one of R, X and Y is a halogen.

当 R为卤素或者为氢时, R、 X、 Y可以相同, 也可以不同。  When R is halogen or hydrogen, R, X, and Y may be the same or different.

所述卤素可以为氟、 氯、 溴或碘, 优选为氟。  The halogen may be fluorine, chlorine, bromine or iodine, preferably fluorine.

优选情况下, 所述酸性介质可以为三氟乙酸、 二氟乙酸、 二氯乙酸、 一氟二 氯乙酸和二氟一氯乙酸中的一种或多种,进一步优选为三氟乙酸、二氟乙酸和二 氟一氯乙酸中的一种或多种。  Preferably, the acidic medium may be one or more of trifluoroacetic acid, difluoroacetic acid, dichloroacetic acid, monofluorodichloroacetic acid and difluoromonochloroacetic acid, further preferably trifluoroacetic acid, difluoroacetic acid One or more of acetic acid and difluoromonochloroacetic acid.

本发明人发现,在使用所述 R、X和 Y中的至少一者为氟的酸性介质的同时, 使用具有 1个或者 4个结晶水的水合过硼酸钠作为固态氧化剂,在降低了回收的 酸性介质的含水量的同时,还降低了玻璃容器的腐蚀。原因可能是因为副产物硼 酸钠的存在, 或者也可能是因为反应体系中较低含水量, 抑制了由含氟酸性介质 产生小量氢氟酸副产物, 从而减少了对玻璃容器的腐蚀。 因此, 本发明优选酸性 介质为 R、 X和 Y中的至少一者为氟的酸性介质, 固态氧化剂为水合过硼酸钠。  The present inventors have found that while using at least one of R, X and Y as an acidic medium of fluorine, hydrated sodium perborate having one or four crystal waters is used as a solid oxidant, and the recovery is lowered. The water content of the acidic medium also reduces the corrosion of the glass container. This may be due to the presence of by-product sodium borate or, possibly, due to the lower water content in the reaction system, which inhibits the production of small amounts of hydrofluoric acid by-products from the fluorine-containing acidic medium, thereby reducing corrosion of the glass container. Accordingly, it is preferred in the present invention that the acidic medium be an acidic medium in which at least one of R, X and Y is fluorine, and the solid oxidant is hydrated sodium perborate.

本发明人还发现,在使用二氯乙酸为酸性介质时,与使用含氟酸性介质相比, 降低了玻璃容器的腐蚀。原因可能是因为由含氟酸性介质产生的小量氢氟酸副产 物, 会对玻璃容器的腐蚀, 而使用二氯乙酸由于不存在上述氢氟酸副产物, 从而 不会对玻璃容器产生腐蚀, 由此也可以看出, 二氯乙酸与各种固态氧化剂配合使 用均不存在玻璃容器腐蚀的问题。因此,本发明也可以优选酸性介质为二氯乙酸。 The inventors have also found that when dichloroacetic acid is used as an acidic medium, compared with the use of a fluorine-containing acidic medium, Reduces corrosion of the glass container. The reason may be that a small amount of hydrofluoric acid by-product produced by a fluorine-containing acidic medium corrodes the glass container, and the use of dichloroacetic acid does not cause corrosion of the glass container due to the absence of the above-mentioned hydrofluoric acid by-product. It can also be seen that the use of dichloroacetic acid in combination with various solid oxidants does not present the problem of corrosion of the glass container. Therefore, in the present invention, it is also preferred that the acidic medium is dichloroacetic acid.

本发明人又发现,在使用硫酸水溶液为酸性介质时, 也具有较好的选择性和 收率, 而且, 相比三氟乙酸、 二氟乙酸、 二氯乙酸、 一氟二氯乙酸、 二氟一氯乙 酸等酸性介质, 硫酸水溶液的获得要容易得多, 而且价格较为低廉, 因此更适于 进行工业化生产。 因此, 所述酸性介质也可以为硫酸水溶液, 所述硫酸水溶液的 浓度可以为 70-90重量%, 优选可以为 80-88重量%。  The inventors have also found that when an aqueous solution of sulfuric acid is used as an acidic medium, it also has better selectivity and yield, and, compared to trifluoroacetic acid, difluoroacetic acid, dichloroacetic acid, monofluorodichloroacetic acid, difluoroacetic acid. An acidic medium such as monochloroacetic acid, which is much easier to obtain in an aqueous solution of sulfuric acid and which is relatively inexpensive, is more suitable for industrial production. Therefore, the acidic medium may also be an aqueous sulfuric acid solution, and the aqueous sulfuric acid solution may have a concentration of 70 to 90% by weight, preferably 80 to 88% by weight.

按照本发明, 所述式 ( I ) 化合物与酸性介质的重量比可以为 1 : 2-10, 优 选为 1 : 3-8, 进一步优选为 1 : 3.5-5。  According to the present invention, the weight ratio of the compound of the formula (I) to the acidic medium may be from 1:2 to 10, preferably from 1:3 to 8, more preferably from 1:3.5 to 5.

按照本发明,将式( I )所示的化合物与固态氧化剂的氧化反应条件可以为, 在 -10°C到 50°C下, 将式 ( I ) 化合物加入酸性介质中, 待其充分溶解后, 加入 固态氧化剂, 反应温度可以为 -10°C到 50°C,优选 5-20°C,进一步优选为 8-12°C。 反应时间可以为 1-48小时, 优选为 4-6小时。  According to the present invention, the oxidation reaction condition of the compound represented by the formula (I) and the solid oxidizing agent may be carried out by adding the compound of the formula (I) to an acidic medium at -10 ° C to 50 ° C until it is sufficiently dissolved. The solid oxidizing agent is added, and the reaction temperature may be -10 ° C to 50 ° C, preferably 5 to 20 ° C, and more preferably 8 to 12 ° C. The reaction time may be from 1 to 48 hours, preferably from 4 to 6 hours.

在固体氧化剂的加入过程中,将氧化剂分批加入, 更有利于提高反应的选择 性。 例如, 可以分 3-6批加入固体氧化剂, 其中第 1次的加入与式 ( I )所示的 化合物等摩尔的固体氧化剂, 剩余量的固体氧化剂可以平均分为 2-5份。  In the process of adding the solid oxidant, the oxidizing agent is added in portions, which is more favorable for improving the selectivity of the reaction. For example, the solid oxidizing agent may be added in 3 to 6 portions, wherein the first time is added to the solid oxidizing agent equimolar to the compound represented by the formula (I), and the remaining amount of the solid oxidizing agent may be equally divided into 2 to 5 parts.

按照本发明, 固态氧化剂与式( I )所示的化合物接触后所得混合物可以与 还原剂接触, 以去除过量的氧化剂。  According to the present invention, the mixture obtained by contacting the solid oxidizing agent with the compound of the formula (I) may be contacted with a reducing agent to remove excess oxidizing agent.

其中, 所述还原剂可以为保险粉、 亚硫酸钠、 二氧化硫及其它还原剂中的一 种或多种, 优选为保险粉和 /或亚硫酸钠。  Wherein, the reducing agent may be one or more of insurance powder, sodium sulfite, sulfur dioxide and other reducing agents, preferably insurance powder and/or sodium sulfite.

其中, 所述还原剂的加入方式和加入量以能够恰好去除过量的氧化剂为准, 例如可以加入还原剂使得所述混合物恰好不能够让淀粉碘化钾试纸变色为准。  Wherein, the reducing agent is added in such a manner that the amount of the reducing agent is added so as to be able to remove the excess oxidizing agent. For example, a reducing agent may be added so that the mixture just does not allow the starch potassium iodide test paper to change color.

按照本发明, 当所述酸性介质为上述结构式所示有机羧酸时, 可以在去除过 量的氧化剂后, 减压蒸出酸性介质。  According to the present invention, when the acidic medium is an organic carboxylic acid represented by the above structural formula, the acidic medium can be distilled off under reduced pressure after removing an excessive amount of the oxidizing agent.

按照本发明,当所述酸性介质为硫酸水溶液时,可以在去除过量的氧化剂后, 在 -5°C到 5°C的温度下, 用水稀释去除过量的氧化剂后的反应液, 然后过滤得到 固体产物, 其中, 稀释用的水的用量与硫酸水溶液的重量比为 1-3:1。  According to the present invention, when the acidic medium is an aqueous sulfuric acid solution, after removing excess oxidant, the reaction liquid after removing excess oxidant may be diluted with water at a temperature of -5 ° C to 5 ° C, and then filtered to obtain a solid. The product, wherein the weight ratio of the amount of water used for dilution to the aqueous solution of sulfuric acid is 1-3:1.

本发明提供的方法还可以包括将减压蒸出酸性介质后的产物进行重结晶。 其中, 所述重结晶所用溶剂可以为甲苯、 氯苯、 乙酸乙酯和碳原子数为 1-4 的醇中的一种或多种。  The method provided by the present invention may further comprise recrystallizing the product after distilling off the acidic medium under reduced pressure. The solvent used for the recrystallization may be one or more of toluene, chlorobenzene, ethyl acetate, and an alcohol having 1 to 4 carbon atoms.

所述重结晶的方法可以为: 先用水清洗减压蒸出酸性介质的固体产物, 以去 除其中的残余酸和无机盐, 再用溶剂加热溶解固体产物直到固体全部溶解, 将该 澄清溶液缓慢冷却至 0-5 °C, 然后在 0-5 °C下保温 2小时进行重结晶, 过滤得晶 体产物。其中, 相对于 1重量份的所述减压蒸出酸性介质后的产物, 清洗用的水 的用量可以为 0.8-3重量份, 重结晶时所用溶剂的用量可以为 0.2-2重量份。 The method of recrystallization may be: firstly purifying the solid product of the acidic medium under water pressure to remove residual acid and inorganic salt, and then dissolving the solid product by heating with a solvent until the solid is completely dissolved, and slowly cooling the clear solution. Recrystallization from 0 to 5 ° C, then at 0-5 ° C for 2 hours, filtering to obtain crystal Body product. Here, the amount of water for washing may be 0.8 to 3 parts by weight, and the amount of solvent used for recrystallization may be 0.2 to 2 parts by weight, based on 1 part by weight of the product obtained by distilling off the acidic medium under reduced pressure.

本发明由于使用固态氧化剂进行氧化,体系中不存在大量的水, 因此与双氧 水和三氟乙酸体系相比, 更有利与三氟乙酸的回收套用。  The present invention is more advantageous in the recovery of trifluoroacetic acid than the hydrogen peroxide and trifluoroacetic acid systems because of the large amount of water present in the system due to oxidation using a solid oxidizing agent.

下面的实施例将对本发明作进一步的说明。需要说明的是, 以下实施例只给 出了本发明的优选或特定的实施方式, 本发明的范围并不局限于以下实施例中。 实施例 1  The invention will be further illustrated by the following examples. It is to be noted that the following examples are merely preferred or specific embodiments of the invention, and the scope of the invention is not limited to the following examples. Example 1

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基) -4-三氟甲硫基吡唑 126.3g ( 0.3mol), 三氟乙酸 500g, 搅拌溶解, 冷却至 10 V。 将反应体系的温度维持在 10-12°C, 一次加入一水过硼酸钠 (NaB03_H20) 41.9g ( 0.42mol) 后, 反应 6h, 气相色谱 (GC ) 监测反应进行程度, 直至原料 转化率大于 98%, 分批加入亚硫酸钠以去除氧化物 (每批 0.1g), 以终止反应, 亚硫酸钠的加入总量使反应体系恰好不能使淀粉碘化钾试纸变色为准, 再搅拌 5 分钟, 减压蒸馏回收三氟乙酸, 得到含水量小于 1重量%的三氟乙酸 410g, 向蒸 除溶剂后的固体中加入 500g水, 搅拌 30min, 降温至 0°C以下, 过滤, 将过滤所 得固体在 300g氯苯中加热至完全溶解, 再缓慢冷却 0-5 °C, 再保温 2小时, 过滤 并干燥, 得到白色固体 122g, 通过 GC检测, 该白色固体主要成分为 5-氨基 -3- 氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度为 95%, 收率 为 93%。 采用上述 1000ml反应瓶重复上述实验 10次, 发现该反应瓶底部内壁 仍然非常光滑, 没有磨痕和发毛现象, 说明反应瓶没有发生明显的腐蚀作用。 对比例 1 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4trifluoromethylanilinophenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol) 500 g of trifluoroacetic acid, dissolved by stirring, and cooled to 10 V. The temperature of the reaction system was maintained at 10-12 ° C, and sodium perborate monohydrate (NaB0 3 _H 2 0) 41.9 g (0.42 mol) was added in one portion. The reaction was carried out for 6 h, and the degree of reaction was monitored by gas chromatography (GC) until the conversion of the raw material was more than 98%. Sodium sulfite was added in portions to remove the oxide (0.1 g per batch) to terminate the reaction, and the total amount of sodium sulfite added did not allow the reaction system to just happen. The starch potassium iodide test paper was discolored, and the mixture was stirred for 5 minutes. The trifluoroacetic acid was distilled under reduced pressure to obtain 410 g of trifluoroacetic acid having a water content of less than 1% by weight. 500 g of water was added to the solid after evaporation of the solvent, and the mixture was stirred for 30 minutes. To below 0 ° C, filtration, the solid obtained by filtration was heated to 300 g of chlorobenzene to completely dissolve, and then slowly cooled at 0-5 ° C, and then kept for 2 hours, filtered and dried to obtain 122 g of a white solid, which was detected by GC. The main component of the white solid is 5-amino-3-cyano- 1-(2,6-Dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole having a purity of 95% and a yield of 93%. The above 1000 ml reaction flask was used to repeat the above After 10 experiments, it was found that the inner wall of the bottom of the reaction bottle was still very smooth, and there was no wear and hairiness, indicating that the reaction bottle did not have obvious corrosive effect.

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基) -4-三氟甲硫基吡唑 126.3g ( 0.3mol), 三氟乙酸 500g, 搅拌溶解, 冷却至 10 。C。 将反应体系的温度维持在 10-12°C, 缓慢滴加 49.9g (浓度为 30%, 0.44mol) H202, 时间控制在 2h; 保持温度在 10-12°C搅拌 5h, GC监测反应完成程度, 直 至原料转化率大于 98%; 加入氯苯 350g, 减压共沸蒸馏回收三氟乙酸、 氯苯与 水的混合液, 分液得到含水量为 8.5%的三氟乙酸 440g, 减压共沸蒸馏结束后, 继续减压蒸馏氯苯到无馏分, 向蒸除溶剂后的固体中加入 500g水,搅拌 30min, 降温至 0°C以下,过滤,将过滤所得固体在浓度为 95重量%的乙醇水溶液中加热 至完全溶解, 再缓慢冷却 0-5 °C, 再保温 2小时, 再过滤得到白色固体, 烘干得 到固体产物 112.5g白色固体,提供 GC检测,该白色固体主要成分为备 5-氨基 -3- 氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度 94%, 收率 86%。采用上述 1000ml反应瓶重复上述实验 10次, 发现该接触反应液的反应瓶 底部不再透明, 边缘模糊, 说明反应体系对玻璃有一定腐蚀作用。 实施例 2 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4trifluoromethylanilinophenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol) 500 g of trifluoroacetic acid, dissolved by stirring, cooled to 10 ° C. The temperature of the reaction system was maintained at 10-12 ° C, and 49.9 g (concentration: 30%, 0.44 mol) H 2 0 2 was slowly added dropwise, time control At 2h; keep the temperature at 10-12 ° C for 5h, GC to monitor the completion of the reaction, until the conversion of raw materials is greater than 98%; add 350g of chlorobenzene, azeotropic distillation under reduced pressure to recover a mixture of trifluoroacetic acid, chlorobenzene and water 440 g of trifluoroacetic acid having a water content of 8.5% was obtained by liquid separation. After the azeotropic distillation under reduced pressure, the chlorobenzene was distilled under reduced pressure until no fraction was obtained. 500 g of water was added to the solid after evaporation of the solvent, and the mixture was stirred for 30 minutes. 0 ° C or less, filtered, the filtered solid was heated to 95% by weight in an aqueous ethanol solution to completely dissolve, and then slowly cooled 0-5 ° C, and then kept for 2 hours, and then filtered to obtain a white solid, dried to obtain a solid The product, 112.5 g of a white solid, was subjected to GC detection. The white solid was mainly composed of 5-amino-3-cyano-1-(2) 6-Dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole, purity 94%, yield 86%. The above experiment was repeated 10 times using the above 1000 ml reaction flask, and the contact was found. Reaction bottle The bottom is no longer transparent and the edges are blurred, indicating that the reaction system has a certain corrosive effect on the glass. Example 2

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基) -4-三氟甲硫基吡唑 126.3g ( 0.3mol), 三氟乙酸 500g, 搅拌溶解, 冷却至 10 V。 将反应体系的温度维持在 10-12 °C, 先加入 29.95g —水合过硼酸钠 (NaB03 H20) (0.3mol), 保温搅拌 3小时, 再将 12.8g ( 0.13mol) 一水合过硼 酸钠平均分成 4份, 分 4次加入。 再保温反应 3h, GC监测反应进行程度, 直至 原料转化率大于 98%, 分批加入亚硫酸钠以去除氧化物, (每批 0.1g), 以终止反 应。亚硫酸钠的加入总量使反应体系恰好不能使淀粉碘化钾试纸变色为准, 再搅 拌 5分钟, 减压蒸馏回收三氟乙酸, 得到含水量小于 1重量%的三氟乙酸 415g, 向蒸除溶剂后的固体中加入 500g水, 搅拌 30min, 降温至 0°C以下, 过滤, 将 过滤所得固体在 120g 甲醇中加热至完全溶解, 再缓慢冷却至 0-5 °C, 再保温 2 小时, 过滤并干燥, 得到白色固体 119g, 通过 GC检测, 该白色固体主要成分为 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度 96%, 收率 91%。采用上述 1000ml反应瓶重复上述实验 10次, 发现该反应瓶底 部内壁仍然非常光滑, 没有磨痕和发毛现象, 说明反应瓶没有发生明显的腐蚀作 用。 实施例 3 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4trifluoromethylanilinophenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol) ), 500g of trifluoroacetic acid, dissolved by stirring, cooled to 10 V. Maintain the temperature of the reaction system at 10-12 °C, first add 29.95g of sodium perborate hydrate (NaB0 3 H 2 0) (0.3mol), keep warm After stirring for 3 hours, 12.8 g (0.13 mol) of sodium perborate monohydrate was divided into 4 portions and added in 4 portions. The reaction was further incubated for 3 hours, and the degree of reaction was monitored by GC until the conversion of the raw material was more than 98%, and sodium sulfite was added in portions. In order to remove the oxide, (0.1g per batch), the reaction was terminated. The total amount of sodium sulfite added was such that the reaction system could not change the color of the starch potassium iodide test paper, and the mixture was stirred for 5 minutes, and trifluoroacetic acid was distilled under reduced pressure to obtain water content. 415g of trifluoroacetic acid is less than 1% by weight, 500g of water is added to the solid after evaporation of the solvent, stirred for 30min, cooled to below 0 °C, filtered, and the solid obtained by filtration is heated to completely dissolve in 120g of methanol, and then slowly cooled. To 0-5 ° C, keep warm for 2 hours, filter and dry 119 g of a white solid were obtained, which was determined by GC. The white solid was mainly composed of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethyl Sulfonylpyrazole, purity 96%, yield 91%. The above experiment was repeated 10 times using the above 1000 ml reaction bottle, and it was found that the inner wall of the bottom of the reaction bottle was still very smooth, without abrasion and hairiness, indicating that the reaction bottle did not appear obvious. Corrosion effect. Example 3

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基)—4-三氟甲硫基吡唑 126.3g ( 0.3mol), 三氟乙酸 500g, 搅拌溶解, 冷却至 10 °C。在 3小时内平均分 5次加入 64.7g四水合过硼酸钠(NaBO3_4H2O) ( 0.42mol)。 将反应体系的温度维持在 10-12°C, 再保温反应 3h, GC监测反应完成程度, 直 至原料转化率大于 99%, 分批加入亚硫酸钠以去除氧化物 (每批 0.1g), 以终止 反应。控制亚硫酸钠加入的批次或总量, 以使反应体系恰好不能使淀粉碘化钾试 纸变色为准, 再搅拌 5分钟, 减压蒸馏回收三氟乙酸, 得到含水量少于 1重量% 的三氟乙酸 405g, 向蒸除溶剂后的固体中加入 500g水, 搅拌 30min, 降温至 0 °C以下, 过滤, 将过滤所得固体在 250g的浓度为 95重量%的乙醇水溶液中加热 至完全溶解, 再缓慢冷却至 0-5 °C, 再保温 2小时, 过滤并干燥, 得到白色固体 124.5g, 通过 GC检测, 该白色固体主要成分为 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三 氟甲基苯基) -4-三氟甲基亚磺酰基吡唑, 纯度 97%, 收率 94%。 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4-trifluoromethylanilinylphenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol) 500 g of trifluoroacetic acid, dissolved by stirring, and cooled to 10 ° C. 64.7 g of sodium perborate tetrahydrate (NaBO 3 _4H 2 O) (0.42 mol) was added in 5 portions over a period of 3 hours. At 10-12 ° C, the reaction was further incubated for 3 h, and the degree of completion of the reaction was monitored by GC until the conversion of the raw material was more than 99%, and sodium sulfite was added in portions to remove the oxide (0.1 g per batch) to terminate the reaction. The total amount or the total amount, so that the reaction system just does not change the color of the starch potassium iodide test paper, and the mixture is stirred for 5 minutes, and trifluoroacetic acid is distilled off under reduced pressure to obtain 405 g of trifluoroacetic acid having a water content of less than 1% by weight, and the solvent is distilled off. 500g of water was added to the subsequent solid, stirred for 30min, cooled to below 0 °C, filtered, and the solid obtained by filtration was heated to 250 g of a 95% by weight aqueous solution of ethanol to completely dissolve, and then slowly cooled to 0-5 °C. , kept for another 2 hours, filtered and dried to give a white solid 124 .5g, the main component of the white solid by GC detection is 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfin Acylpyrazole, purity 97%, yield 94%.

采用上述 1000ml反应瓶重复上述实验 10次,发现该反应瓶底部内壁仍然非 常光滑, 没有磨痕和发毛现象, 说明反应瓶没有发生明显的腐蚀作用。 实施例 4 The above experiment was repeated 10 times using the above 1000 ml reaction bottle, and it was found that the inner wall of the bottom of the reaction bottle was still very smooth, and there was no abrasion and hairiness, indicating that the reaction bottle did not have obvious corrosive effect. Example 4

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基)—4-三氟甲硫基吡唑 126.3g (0.3mol), 二氯乙酸 (Cl2CHCOOH) 500g, 搅拌 溶解, 冷却至 10 °C。 在 3 小时内平均分 4 次加入过一硫酸氢钾 (2K2S05 KHS04 K2S04 ) 240g (0.39mol)。 将反应体系的温度维持在 10-12°C, 再保温反应 5h, GC监测反应完成程度, 直至原料转化率大于 98%,, 分批加入 亚硫酸钠以去除氧化物 (每批 0.1g), 以终止反应。 控制亚硫酸钠加入的批次或 总量, 以使反应体系恰好不能使淀粉碘化钾试纸变色为准, 再搅拌 5分钟, 减压 蒸馏回收二氯乙酸, 得到无水二氯乙酸 420g, 向蒸除溶剂后的固体中加入 500g 水, 搅拌 30min, 降温至 0°C以下, 过滤, 将过滤所得固体在 250g的 95重量% 浓度的乙醇水溶液中加热至完全溶解, 再缓慢冷却至 0-5 °C, 再保温 2小时, 过 滤并干燥,得到白色固体 110g,通过 GC检测,该白色固体主要成分为 5-氨基 -3- 氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度 92%, 收率 84%。采用上述 1000ml反应瓶重复上述实验 10次, 发现该反应瓶底部内壁仍然 非常光滑, 没有磨痕和发毛现象, 说明反应瓶没有发生明显的腐蚀作用。 实施例 5 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4-trifluoromethylanilinylphenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol). ), dichloroacetic acid (Cl 2 CHCOOH) 500g, dissolved by stirring, cooled to 10 ° C. Add potassium peroxymonosulfate (2K 2 S0 5 KHS0 4 K 2 S04 ) 240g (0.39mol) in 4 hours in 3 hours. The temperature of the reaction system was maintained at 10-12 ° C, and the reaction was further incubated for 5 h. The degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and sodium sulfite was added in portions to remove the oxide (0.1 g per batch). To terminate the reaction. Control the batch or total amount of sodium sulfite added, so that the reaction system can not just change the color of the starch potassium iodide test paper, stir for 5 minutes, dichloroacetic acid is distilled off under reduced pressure to obtain 420 g of anhydrous dichloroacetic acid. 500 g of water was added to the solid after evaporation of the solvent, stirred for 30 min, cooled to below 0 ° C, filtered, and the solid obtained by filtration was heated to 250 g of a 95% by weight aqueous solution of ethanol to completely dissolve, and then slowly cooled to 0-5. °C, kept for another 2 hours, filtered and dried to give a white solid 110g The main component of the white solid was 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyridinium by GC. The azole was 92% pure and the yield was 84%. The above experiment was repeated 10 times using the above 1000 ml reaction bottle, and it was found that the inner wall of the bottom of the reaction bottle was still very smooth, and there was no abrasion and hairiness, indicating that the reaction bottle did not have obvious corrosive effect. Example 5

向 1000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基)—4-三氟甲硫基吡唑 126.3g ( 0.3mol ), 一氟二氯乙酸 100g 和氯乙酸 (ClCH2COOH) 500g的混合液, 搅拌到溶解, 冷却至 10°C。 一次加入过碳酸钠 (2Na2C03-3H202) 114.24g ( 0.42mol)。 将反应体系的温度维持在 10-12°C, 再 保温反应 6h, GC监测反应完成程度, 直至原料转化率大于 98%, 分批加入亚硫 酸钠以去除氧化物(每批 0.1g), 以终止反应。控制亚硫酸钠加入的批次或总量, 以使反应体系恰好不能使淀粉碘化钾试纸变色为准, 再搅拌 5分钟, 减压蒸馏回 收得到含水量少于 2重量%三氟乙酸和氯乙酸的混合溶剂 430g,向蒸除溶剂后的 固体中加入 500g水, 搅拌 30min, 降温至 0°C以下, 过滤, 将过滤所得固体在 250g的浓度为 95重量%乙醇水溶液中加热至完全溶解, 再缓慢冷却至 0-5°C, 再保温 2小时, 过滤并干燥, 得到白色固体 117g, 通过 GC检测, 该白色固体主 要成分为 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度 96%, 收率 89.2%。采用上述 1000ml反应瓶重复上述实验 10次, 发现接触 反应液的反应瓶底部不再透明,边缘模糊,说明反应体系对玻璃有一定腐蚀作用。 实施例 6 To a 1000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4-trifluoromethylanilinylphenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol) a mixture of 100 g of monofluorodichloroacetic acid and 500 g of chloroacetic acid (ClCH 2 COOH), stirred until dissolved, and cooled to 10 ° C. Once added sodium percarbonate (2Na 2 C0 3 -3H 2 0 2 ) 114.24 g ( 0.42 mol). The temperature of the reaction system was maintained at 10-12 ° C, and the reaction was further incubated for 6 h. The degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and sodium sulfite was added in portions to remove oxides (0.1 g per batch). To terminate the reaction. Control the batch or total amount of sodium sulfite added so that the reaction system just does not change the color of the starch potassium iodide test paper, stir for 5 minutes, and recover by distillation under reduced pressure to obtain a water content of less than 2% by weight of trifluoroacetic acid. 430 g of a mixed solvent of chloroacetic acid, 500 g of water was added to the solid after evaporation of the solvent, stirred for 30 min, cooled to below 0 ° C, filtered, and the solid obtained by filtration was heated to a complete dissolution in 250 g of a 95% by weight aqueous solution of ethanol. , slowly cool to 0-5 ° C, and then keep warm for 2 hours, filter Drying gave 117 g of a white solid, which was identified by GC. The white solid was mainly 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoro Methylsulfinylpyrazole, purity 96%, yield 89.2%. The above experiment was repeated 10 times using the above 1000 ml reaction flask, and it was found that the bottom of the reaction bottle contacting the reaction solution was no longer transparent and the edges were blurred, indicating that the reaction system had a certain glass. Corrosion effect. Example 6

向 2000ml反应瓶中依次加入 5- (氨基 -3氰基 -1-(2,6-二氯 -4三氟甲基苯胺苯 基) -4-三氟甲硫基吡唑 126.3g (0.3mol), 浓度为 80重量%的硫酸 900g, 搅拌到 溶解, 冷却至 10°C。 一次加入一水过硼酸钠 (NaB03 H20 ) 41.9g ( 0.42mol)。 将反应体系的温度维持在 10-12°C, 再保温反应 6h, GC监测反应完成程度, 直 至原料转化率大于 98%, 通入 S02气体以去除氧化物, 以终止反应。 控制 S02 气体通入的总量, 以使反应体系恰好不能使淀粉碘化钾试纸变色为准, 再搅拌 5 分钟, 将反应瓶置于冰水浴中, 向反应液滴加入 1800g水, 在反应液温度降至 0 °〇后过滤,得到白色固体 110g,通过 GC检测,该白色固体主要成分为 5-氨基 -3- 氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺酰基吡唑, 纯度 91%, 收率 84%。 To a 2000 ml reaction flask was added 5-(amino-3cyano-1-(2,6-dichloro-4-trifluoromethylanilinophenyl)-4-trifluoromethylthiopyrazole 126.3 g (0.3 mol). ), 900g of sulfuric acid at a concentration of 80% by weight, stirred to Dissolve and cool to 10 °C. Sodium perborate monohydrate (NaB0 3 H 2 0 ) 41.9 g (0.42 mol) was added in one portion. The temperature of the reaction system was maintained at 10-12 ° C, and the reaction was further incubated for 6 hours. The degree of completion of the reaction was monitored by GC until the conversion of the raw material was greater than 98%, and the SO 2 gas was introduced to remove the oxide to terminate the reaction. Control the total amount of S0 2 gas inflow, so that the reaction system just can not make the starch potassium iodide test paper discoloration, stir for 5 minutes, put the reaction bottle in an ice water bath, add 1800g water to the reaction droplet, at the reaction liquid temperature After being reduced to 0 °, it was filtered to give a white solid, 110 g, which was determined by GC. The main component of the white solid was 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl) -4-trifluoromethylsulfinylpyrazole, purity 91%, yield 84%.

Claims

权利要求书 Claim 1、一种制备下式( II )所示的 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4- 三氟甲基亚磺酰基吡唑的方法,  1. A 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinic acid represented by the following formula (II) Acylpyrazole method,
Figure imgf000010_0001
Figure imgf000010_0001
( II )  (II) 其特征在于,该 5-氨基 -3-氰基 -1-(2,6-二氯 -4-三氟甲基苯基 )-4-三氟甲基亚磺 酰基吡唑的制备方法包括在酸性介质中,在氧化反应条件下, 使用固态氧化剂与 物接触,  Characterized in that the preparation method of 5-amino-3-cyano-1-(2,6-dichloro-4-trifluoromethylphenyl)-4-trifluoromethylsulfinylpyrazole is included in In an acidic medium, a solid oxidant is used to contact the object under the oxidation reaction conditions.
Figure imgf000010_0002
Figure imgf000010_0002
2、 根据权利要求 1所述的方法, 其中, 所述式 ( I ) 化合物与固态氧化剂 的摩尔比为 1: 0.9-6.0。  The method according to claim 1, wherein the molar ratio of the compound of the formula (I) to the solid oxidizing agent is 1: 0.9-6.0. 3、 根据权利要求 1或 2所述的方法, 其中, 所述固态氧化剂为过硼酸钠、 过一硫酸氢钾、 过碳酸钠、 过氧化钙、 过氧化镁中的一种或多种。  The method according to claim 1 or 2, wherein the solid oxidizing agent is one or more of sodium perborate, potassium peroxymonosulfate, sodium percarbonate, calcium peroxide, and magnesium peroxide. 4、 根据权利要求 3所述的方法, 其中, 所述过硼酸钠为具有 1个或者 4个 结晶水的水合过硼酸钠。 4. The method according to claim 3, wherein the sodium perborate is hydrated sodium perborate having one or four water of crystallization. 5、 根据权利要求 1所述的方法, 其中, 酸性介质与式 ( I ) 化合物的重量 比为 2-10: 1。 5. The method according to claim 1, wherein the weight ratio of the acidic medium to the compound of the formula (I) is from 2 to 10:1. 6、 根据权利要求 1或 5所述的方法, 其中, 所述酸性介质选自具有如下结 构式的有机羧酸中的一种或多种:
Figure imgf000011_0001
6. The method according to claim 1 or 5, wherein the acidic medium is selected from one or more of the group consisting of organic carboxylic acids having the following structural formula:
Figure imgf000011_0001
其中, R表示 C1到 C6的烷基、 C1到 C6的卤代烃基、 卤素或者氢, X和 Y各自表示卤素或者氢。  Wherein R represents a C1 to C6 alkyl group, a C1 to C6 halogenated hydrocarbon group, a halogen or a hydrogen, and X and Y each represent a halogen or a hydrogen.
7、 根据权利要求 6所述的方法, 其中, 所述酸性介质为三氟乙酸、 二氟乙 酸、 二氯乙酸、 一氟二氯乙酸和二氟一氯乙酸中的一种或多种。 7. The method according to claim 6, wherein the acidic medium is one or more of trifluoroacetic acid, difluoroacetic acid, dichloroacetic acid, monofluorodichloroacetic acid, and difluoromonochloroacetic acid. 8、 根据权利要求 6所述的方法, 其中, 所述 R、 X和 Y为氟, 所述固态氧 化剂为具有 1个或者 4个结晶水的水合过硼酸钠。 8. The method according to claim 6, wherein said R, X and Y are fluorine, and said solid oxide agent is hydrated sodium perborate having one or four water of crystallization. 9、 根据权利要求 1或 5所述的方法, 其中, 所述酸性介质为硫酸水溶液, 所述硫酸水溶液的浓度为 70-90重量%。 The method according to claim 1 or 5, wherein the acidic medium is an aqueous sulfuric acid solution, and the aqueous sulfuric acid solution has a concentration of 70 to 90% by weight. 10、 根据权利要求 1所述的方法, 其中, 所述氧化反应条件包括, 反应温度 为 -10°C到 50°C, 反应时间为 1-48小时。 The method according to claim 1, wherein the oxidation reaction conditions include a reaction temperature of from -10 ° C to 50 ° C and a reaction time of from 1 to 48 hours. 11、根据权利要求 6所述的方法,其中,该方法还包括将固态氧化剂与式( I ) 所示的化合物接触后所得混合物与还原剂接触, 然后减压蒸出酸性介质。 The method according to claim 6, wherein the method further comprises contacting the mixture obtained by contacting the solid oxidizing agent with the compound represented by the formula (I) with a reducing agent, and then distilling off the acidic medium under reduced pressure. 12、 根据权利要求 11所述的方法, 其中, 所述还原剂为保险粉、 亚硫酸钠 和二氧化硫中的一种或多种。 The method according to claim 11, wherein the reducing agent is one or more of a safety powder, sodium sulfite, and sulfur dioxide. 13、 根据权利要求 11所述的方法, 其中, 该方法还包括将减压蒸出酸性介 质后的产物进行重结晶, 所述重结晶所用溶剂为甲苯、 氯苯、 乙酸乙酯和碳原子 数为 1-4的醇中的一种或多种。 13. The method according to claim 11, wherein the method further comprises recrystallizing a product obtained by distilling off the acidic medium under reduced pressure, wherein the solvent used for the recrystallization is toluene, chlorobenzene, ethyl acetate and carbon atoms. One or more of the alcohols of 1-4.
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