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CN1218935C - Substituted benzoyl urea insect growth regulator synthesizing method - Google Patents

Substituted benzoyl urea insect growth regulator synthesizing method Download PDF

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CN1218935C
CN1218935C CN 03153528 CN03153528A CN1218935C CN 1218935 C CN1218935 C CN 1218935C CN 03153528 CN03153528 CN 03153528 CN 03153528 A CN03153528 A CN 03153528A CN 1218935 C CN1218935 C CN 1218935C
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CN1580042A (en
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曾益良
宋建军
张平南
秦小薇
栗心贞
陈志祥
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Abstract

本发明涉及一种取代苯甲酰脲类昆虫生长调节剂的合成方法,具体的说是涉及氟铃脲、氟虫脲和除虫脲的合成方法。该方法以2,6-二氟苯甲腈为起始原料,经氟化、水解、酯化、加成而得到取代苯甲酰脲类化合物。此方法在氟化步骤使用了高活性的氟化钾和季铵盐催化剂,使得氟化反应时间大大缩短;在水解步骤使用了碱催化水解反应从而降低了对设备的特殊要求;在酯化步骤使用光气代替草酰氯,降低酯化反应成本;在加成步骤使用催化剂提高加成反应产率。该方法产率高、步骤简易、原料便宜、更适用于工业生产规模。使用此方法得到的除虫脲收率为97%,氟铃脲收率为93%,氟虫脲收率为86%。The invention relates to a synthesis method of a substituted benzoylurea insect growth regulator, in particular to a synthesis method of hexaflumuron, fluflubenzuron and diflubenzuron. The method uses 2,6-difluorobenzonitrile as a starting material to obtain substituted benzoylurea compounds through fluorination, hydrolysis, esterification and addition. This method uses highly active potassium fluoride and quaternary ammonium salt catalysts in the fluorination step, which greatly shortens the fluorination reaction time; uses a base-catalyzed hydrolysis reaction in the hydrolysis step to reduce the special requirements for equipment; in the esterification step Use phosgene instead of oxalyl chloride to reduce the cost of esterification reaction; use a catalyst in the addition step to increase the yield of the addition reaction. The method has the advantages of high yield, simple steps, cheap raw materials, and is more suitable for industrial production scale. Using this method, the yield of diflubenzuron was 97%, that of hexaflumuron was 93%, and that of diflubenzuron was 86%.

Description

取代苯甲酰脲类昆虫生长调节剂的合成方法Synthetic method of substituted benzoylurea insect growth regulator

技术领域technical field

本发明涉及一种取代苯甲酰脲类昆虫生长调节剂的合成方法,具体的说是涉及氟铃脲、氟虫脲和除虫脲的合成方法。The invention relates to a synthesis method of a substituted benzoylurea insect growth regulator, in particular to a synthesis method of hexaflumuron, fluflubenzuron and diflubenzuron.

技术背景technical background

苯甲酰基脲类化合物是通过抑制昆虫几丁质的合成来起作用的一类有效的杀虫杀螨剂,或称之为昆虫生长调节剂。其中最为常见的有美国DOW ELAN公司在1987年开发的氟铃脲(hexaflumuron)、氟虫脲、除虫脲等。Benzoylurea compounds are a class of effective insecticides and acaricides that act by inhibiting the synthesis of chitin in insects, or insect growth regulators. Among them, the most common ones are hexaflumuron (hexaflumuron), fluflubenzuron, and diflubenzuron developed by DOW ELAN Company of the United States in 1987.

这类化合物的合成大多是以2,6-二氯苯甲腈为起始原料,经氟化、水解酯化、加成而得到取代苯甲酰脲类化合物,如其反应式如下:Most of the synthesis of this type of compound uses 2,6-dichlorobenzonitrile as the starting material, through fluorination, hydrolysis, esterification, and addition to obtain substituted benzoylurea compounds, such as the reaction formula is as follows:

1)氟化:1) Fluorination:

2)水解:2) Hydrolysis:

Figure C0315352800032
Figure C0315352800032

3)酯化:3) Esterification:

Figure C0315352800033
Figure C0315352800033

4)加成:4) Bonus:

其中,in,

于登博等人在农药vol.39 No.3 2000中所述的除虫脲的合成,即是采用上述方法制得。但是此法的步骤2)的水解是采用90%的浓硫酸,因而对反应设备要求苛刻,需防酸材质所制备,潜在的危险性较大;步骤3)的酯化是使用草酰氯,成本高;得到的产物需分离提纯,步骤繁琐。The synthesis of diflubenzuron described in pesticide vol.39 No.3 2000 by Yu Dengbo et al. was obtained by the above method. But the hydrolysis of step 2) of this method is to adopt the concentrated sulfuric acid of 90%, thereby harsh to reaction equipment, needs the preparation of acid-proof material, potential danger is bigger; The esterification of step 3) is to use oxalyl chloride, cost High; the obtained product needs to be separated and purified, and the steps are cumbersome.

对于步骤1),CN85100467A中公开了由氯代苯腈制备氟代苯腈的方法,虽然较一般方法提高了产率,可以达到86%,但仍不是很高;而且该法使用全氟烷基氧杂羧酸衍生物作为催化剂,这类开环醚类的催化剂的制备繁琐,不利于工业生产。For step 1), CN85100467A discloses the method for preparing fluorobenzonitrile by chlorobenzonitrile, although the yield is improved compared with the general method, it can reach 86%, but it is still not very high; and the method uses perfluoroalkyl Oxacarboxylic acid derivatives are used as catalysts, and the preparation of such ring-opening ether catalysts is cumbersome and unfavorable for industrial production.

对于步骤3),赵永华在农药vol.40 No.11 2001中所述的氟铃脲的合成中,采用草酰氯将2,6-二氟苯甲酰胺酯化,此法成本高,得到的异酯在室温下不够稳定,为此,作者曾尝试使用便宜的光气代替草酰氯,但是反应难以进行。For step 3), Zhao Yonghua used oxalyl chloride to esterify 2,6-difluorobenzamide in the synthesis of hexaflumuron described in the pesticide vol.40 No.11 2001. The cost of this method is high, and the obtained iso Esters are not stable enough at room temperature. For this reason, the author tried to use cheap phosgene instead of oxalyl chloride, but the reaction was difficult.

陈英奇在化学反应工程与工艺vol.10 No.1 1994.12中所述的氟虫脲的合成中,步骤3)的酯化是使用草酰氯,成本高;其使用二氯甲烷作为溶剂,使得到的产物——异酯为黄色油状物,需进一步提纯才可在下一步使用;且产率仅为74%。而在步骤4)中未使用催化剂,反应时间过长;且步骤3)和步骤4)未使用同样的溶剂,增加了工业生产时的工艺条件。In the synthesis of flufenuron described in Chen Yingqi's Chemical Reaction Engineering and Technology vol.10 No.1 1994.12, the esterification of step 3) uses oxalyl chloride, which has high cost; it uses dichloromethane as a solvent, so that the obtained The product, isoester, is a yellow oil that needs further purification before it can be used in the next step; and the yield is only 74%. And in step 4) no catalyst is used, the reaction time is too long; and step 3) and step 4) do not use the same solvent, which increases the process conditions during industrial production.

综上所述,现有技术存在以下的缺陷:In summary, there are following defects in the prior art:

步骤1)的氟化是使用煅烧得到的氟化钾,不加催化剂,反应时间长达20小时,但产率低至50%;或使用全氟烷基氧杂羧酸衍生物作为催化剂,此催化剂的制备繁琐,不利于工业生产;The fluorination of step 1) is to use potassium fluoride obtained by calcining without adding a catalyst, the reaction time is as long as 20 hours, but the yield is as low as 50%; or use perfluoroalkyl oxacarboxylic acid derivatives as catalysts, this The preparation of the catalyst is cumbersome and unfavorable for industrial production;

步骤2)的水解是采用90%的浓硫酸,因而对反应设备要求苛刻,需防酸材质所制备,潜在的危险性较大;The hydrolysis of step 2) adopts 90% concentrated sulfuric acid, so the requirements for reaction equipment are harsh, and it needs to be prepared by acid-proof material, which is potentially dangerous;

步骤3)的酯化通常使用草酰氯,成本高,是使用光气的6倍;且得到的产物需从溶液中分离提纯,步骤繁琐;The esterification of step 3) usually uses oxalyl chloride, which has a high cost and is 6 times that of using phosgene; and the obtained product needs to be separated and purified from the solution, and the steps are cumbersome;

步骤4)的加成是采用氟代苯甲酰异氰酸酯与取代苯胺在无催化剂的条件下加成,反应产率不高。The addition of step 4) adopts the addition of fluorobenzoyl isocyanate and substituted aniline under the condition of no catalyst, and the reaction yield is not high.

发明内容Contents of the invention

本发明的目的在于克服已有技术合成取代苯甲酰脲类昆虫生长调节剂时,氟化反应时间长、成率低,水解反应由于使用了酸催化而对设备有特殊要求、操作有危险性,以及酯化反应成本高、产物需分离,以及加成反应成率不够高的缺陷,从而提供一种使用了高活性的氟化钾和季铵盐催化剂,使得氟化反应时间大大缩短,使用了碱催化水解反应从而降低了对设备的特殊要求,以及使用光气代替草酰氯,降低酯化反应成本,使用催化剂提高加成反应产率的取代苯甲酰脲类昆虫生长调节剂的合成方法。The purpose of the present invention is to overcome the long fluorination reaction time and low yield when synthesizing substituted benzoylurea insect growth regulators in the prior art, and the hydrolysis reaction has special requirements for equipment and dangerous operation due to the use of acid catalysis , and the disadvantages of high cost of esterification reaction, separation of products, and insufficient addition reaction rate, thus providing a catalyst using highly active potassium fluoride and quaternary ammonium salt, which greatly shortens the fluorination reaction time and uses A base-catalyzed hydrolysis reaction reduces the special requirements for equipment, and uses phosgene to replace oxalyl chloride, reduces the cost of esterification reaction, and uses a catalyst to increase the yield of addition reaction. A synthetic method for substituted benzoylurea insect growth regulators .

本发明的目的是通过如下的技术方案来实现的:The purpose of the present invention is achieved through the following technical solutions:

本发明提供一种取代苯甲酰脲类昆虫生长调节剂的合成方法,其包括如下步骤:The invention provides a kind of synthetic method that replaces benzoylurea insect growth regulator, and it comprises the steps:

1)氟化:将2,6-二氯苯腈1摩尔、450-550目无水氟化钾1.5~2.0摩尔、溶剂、催化剂A的混合物在反应釜中,于200℃加热8~10小时,过滤,将滤液分馏,得到2,6-二氟苯腈,并回收溶剂;1) Fluorination: heat a mixture of 1 mole of 2,6-dichlorobenzonitrile, 1.5-2.0 moles of anhydrous potassium fluoride of 450-550 mesh, solvent and catalyst A in a reaction kettle at 200°C for 8-10 hours , filtered, and the filtrate was fractionally distilled to obtain 2,6-difluorobenzonitrile, and the solvent was recovered;

所述溶剂为环丁砜;Described solvent is sulfolane;

所述催化剂A为四丁基氯化铵和甲基三辛基氯化铵的混合物,其中四丁基氯化铵所占重量百分比为40~60wt%;所述催化剂A用量为2,6-二氯苯腈重量的1~3wt%;The catalyst A is a mixture of tetrabutylammonium chloride and methyltrioctylammonium chloride, wherein tetrabutylammonium chloride accounts for 40 to 60 wt% by weight; the amount of catalyst A is 2,6- 1~3wt% of dichlorobenzonitrile weight;

2)水解:将步骤1)得到的2,6-二氟苯腈1摩尔、催化剂B加入反应釜中,边搅拌边滴入过量的过氧化氢,保持反应温度在40℃,滴加完毕后,再在此温度保持1小时,负压排除未反应的过氧化氢,离心机甩干反应物,得到2,6-二氟苯甲酰胺滤饼;2) Hydrolysis: Add 1 mole of 2,6-difluorobenzonitrile obtained in step 1) and Catalyst B into the reactor, add excess hydrogen peroxide dropwise while stirring, keep the reaction temperature at 40°C, after the dropwise addition is completed , then keep at this temperature for 1 hour, remove unreacted hydrogen peroxide under negative pressure, dry the reactants in a centrifuge, and obtain 2,6-difluorobenzamide filter cake;

所述催化剂B为氢氧化钠、碳酸钠、或碳酸氢钠中的一种或以重量比为1∶1的两种;所述催化剂B用量为2,6-二氟苯腈重量的1~3wt%;The catalyst B is one of sodium hydroxide, sodium carbonate, or sodium bicarbonate, or two of them in a weight ratio of 1:1; 3wt%;

3)酯化:将步骤2)得到的2,6-二氟苯甲酰胺滤饼溶于溶剂,通入过量的光气,加热回流4小时,生成2,6-二氟苯甲酰异氰酸酯;所得产物可不经提纯直接用于下一步;所述溶剂为甲苯;3) Esterification: dissolving the 2,6-difluorobenzamide filter cake obtained in step 2) in a solvent, passing through excess phosgene, and heating to reflux for 4 hours to generate 2,6-difluorobenzoyl isocyanate; The resulting product can be directly used in the next step without purification; the solvent is toluene;

4)加成:将步骤3)得到的2,6-二氟苯甲酰异氰酸酯溶于甲苯,加入等摩尔的取代苯胺、以及催化剂C,在100~110℃反应4~6小时,得到取代苯甲酰脲类昆虫生长调节剂;4) Addition: Dissolve the 2,6-difluorobenzoyl isocyanate obtained in step 3) in toluene, add equimolar substituted aniline and catalyst C, and react at 100-110°C for 4-6 hours to obtain substituted benzene Formylurea insect growth regulators;

所述的取代苯胺为4-氯苯胺、3,5-二氯-4-(1,1,2,2-四氟乙氧基)苯胺或4-(2-氯4-三氟甲基苯氧基)-2-氟苯胺;The substituted aniline is 4-chloroaniline, 3,5-dichloro-4-(1,1,2,2-tetrafluoroethoxy)aniline or 4-(2-chloro4-trifluoromethylbenzene Oxy)-2-fluoroaniline;

所述催化剂C为三乙胺或/和三乙醇胺;所述催化剂C用量为2,6-二氟苯甲酰异氰酸酯重量的1~3wt%。The catalyst C is triethylamine or/and triethanolamine; the dosage of the catalyst C is 1-3 wt% of the weight of 2,6-difluorobenzoyl isocyanate.

其反应式如下:Its reaction formula is as follows:

Figure C0315352800061
Figure C0315352800061

其中,in,

Figure C0315352800071
Figure C0315352800071

本发明提供的合成方法与现有技术相比,其优益之处在于:Compared with the prior art, the synthetic method provided by the invention has the advantages of:

1)本发明不同于已有技术是在实验室中实现,更适用于工业生产规模;1) The present invention is different from prior art and realizes in the laboratory, is more suitable for industrial production scale;

2)本发明的氟化步骤采用季铵盐为催化剂,同时使用了细粒无水氟化钾,从而使得二氟苯睛收率高达96%;且季铵盐是广为使用的相转移催化剂,便宜、易得,易于工业化生产;2) The fluorination step of the present invention adopts quaternary ammonium salt as a catalyst, and simultaneously uses fine-grained anhydrous potassium fluoride, so that the yield of difluorobenzonitrile is as high as 96%; and quaternary ammonium salt is a widely used phase transfer catalyst , cheap, easy to obtain, and easy to industrialized production;

3)本发明的水解步骤采用了碱催化,无需防酸设备,并保持高收率92%;3) The hydrolysis step of the present invention adopts alkali catalysis, does not need anti-acid equipment, and maintains a high yield of 92%;

4)本发明的酯化步骤采用了成本低廉的光气代替草酰氯,降低了成本,并保持高收率91%;而且,得到的产物无需纯化,可直接用于下一步反应;4) The esterification step of the present invention adopts low-cost phosgene to replace oxalyl chloride, which reduces the cost and maintains a high yield of 91%; moreover, the obtained product can be directly used in the next step without purification;

5)本发明的加成步骤使用与酯化步骤相同的溶剂,简化了工业操作;而且此步骤采用三乙胺或三乙醇胺作催化剂,提高了反应的产率,除虫脲收率为97%,氟铃脲收率为93%,氟虫脲收率为86%。5) The addition step of the present invention uses the same solvent as the esterification step, which simplifies industrial operations; and this step uses triethylamine or triethanolamine as a catalyst, which improves the yield of the reaction, and the yield of diflubenzuron is 97%. , the yield of hexaflumuron was 93%, and the yield of hexaflumuron was 86%.

具体实施方式Detailed ways

实施例1Example 1

1)氟化:在1000L反应釜中加入500Kg环丁砜,边搅拌边加入经喷雾干燥处理过的细粒氟化钾(450目)88.4Kg(1.5千摩尔),2,6-二氯苯腈172Kg(1千摩尔),以及由40wt%四丁基氯化铵和60wt%甲基三辛基氯化铵组成的催化剂混合物1.72Kg,于200℃加热8小时,过滤,滤去沉淀的氯化钾,将滤液分馏得到2,6-二氟苯腈133.6Kg(0.96千摩尔),产率为96.1%,含量为98.4%,并回收溶剂环丁砜;1) Fluorination: Add 500Kg sulfolane to a 1000L reactor, and add 88.4Kg (1.5 kilomoles) of fine-grained potassium fluoride (450 mesh) which has been spray-dried while stirring, and 172Kg of 2,6-dichlorobenzonitrile (1 kilomole), and the catalyst mixture 1.72Kg that is made up of 40wt% tetrabutylammonium chloride and 60wt% methyltrioctylammonium chloride, in 200 ℃ of heating 8 hours, filter, filter the potassium chloride of precipitation , the filtrate was fractionally distilled to obtain 2,6-difluorobenzonitrile 133.6Kg (0.96 kilomoles), the productive rate was 96.1%, and the content was 98.4%, and the solvent sulfolane was recovered;

2)水解:将2,6-二氟苯腈109.9Kg(0.79千摩尔),催化剂氢氧化钠1.10Kg加入反应釜中,开启热蒸气升温,在2小时内滴加72.63Kg(2.14千摩尔)过氧化氢,滴加完毕,在40℃保温1小时,负压过量的过氧化氢,反应物用离心机甩干,得到2,6-二氟苯甲酰胺滤饼114.4Kg(0.728千摩尔),产率为92.2%,含量为98.7%;2) Hydrolysis: Add 109.9Kg (0.79 kilomoles) of 2,6-difluorobenzonitrile and 1.10Kg catalyst sodium hydroxide into the reactor, turn on the hot steam to raise the temperature, and add 72.63Kg (2.14 kilomoles) dropwise within 2 hours Hydrogen peroxide, after the dropwise addition, was incubated at 40°C for 1 hour, the excess hydrogen peroxide under negative pressure, and the reactant was dried with a centrifuge to obtain 114.4Kg (0.728 kilomoles) of 2,6-difluorobenzamide filter cake , the yield is 92.2%, and the content is 98.7%;

3)酯化:将2,6-二氟苯甲酰胺滤饼98Kg(0.62千摩尔)和417.2Kg甲苯加入反应釜内,通入光气111.9Kg(1.13千摩尔),加热回流4小时,生成2,6-二氟苯甲酰异氰酸酯103.0Kg(0.56千摩尔),产率90.9%,所得产物可不经提纯直接用于下一步;3) Esterification: 98Kg (0.62 kilomoles) of 2,6-difluorobenzamide filter cake and 417.2Kg toluene were added into the reaction kettle, 111.9Kg (1.13 kilomoles) of phosgene was passed through, heated and refluxed for 4 hours, and 2,6-difluorobenzoyl isocyanate 103.0Kg (0.56 kilomoles), yield 90.9%, the resulting product can be directly used in the next step without purification;

4)加成:将上步所得的2,6-二氟苯甲酰异氰酸酯62.2Kg(0.34千摩尔),3,5-二氯-4-(1,1,2,2-四氟乙氧基)苯胺94.5Kg(0.34千摩尔),以及三乙胺0.622Kg溶于500Kg甲苯中,在100℃反应6小时,反应液经离心过滤,收集滤饼,干燥,得到氟铃脲144.7Kg(0.31千摩尔),产率92.3%,含量97.2%,将滤液进一步浓缩,还可得到氟铃脲2.3Kg,计入产率为93.8%。4) Addition: 62.2Kg (0.34 kilomoles) of 2,6-difluorobenzoyl isocyanate obtained in the previous step, 3,5-dichloro-4-(1,1,2,2-tetrafluoroethoxy Base) 94.5Kg (0.34 kilomoles) of aniline, and 0.622Kg of triethylamine were dissolved in 500Kg toluene, and reacted for 6 hours at 100°C. The reaction solution was centrifugally filtered, and the filter cake was collected and dried to obtain 144.7Kg (0.31 kilomole), productive rate 92.3%, content 97.2%, the filtrate is further concentrated, and hexaflumuron 2.3Kg can also be obtained, and the calculated productive rate is 93.8%.

实施例2Example 2

1)氟化:在1000L反应釜中加入500Kg环丁砜,边搅拌边加入经喷雾干燥处理过的细粒氟化钾(550目)117.8Kg(2千摩尔),2,6-二氯苯腈172Kg(1千摩尔),以及由60wt%四丁基氯化铵和40wt%甲基三辛基氯化铵组成的催化剂混合物5.16Kg,于200℃加热10小时,过滤,滤去沉淀的氯化钾,将滤液分馏得到2,6-二氟苯腈134.1Kg(0.965千摩尔),产率为96.5%,含量为99.3%,并回收溶剂环丁砜;1) Fluorination: Add 500Kg sulfolane in a 1000L reactor, and add 117.8Kg (2 kilomoles) of fine-grained potassium fluoride (550 mesh) which has been spray-dried while stirring, and 172Kg of 2,6-dichlorobenzonitrile (1 kilomole), and the catalyst mixture 5.16Kg that is made up of 60wt% tetrabutylammonium chloride and 40wt% methyltrioctylammonium chloride, in 200 ℃ of heating 10 hours, filter, filter the potassium chloride of precipitation , the filtrate was fractionally distilled to obtain 2,6-difluorobenzonitrile 134.1Kg (0.965 kilomoles), the productive rate was 96.5%, and the content was 99.3%, and the solvent sulfolane was recovered;

2)水解:将二氟苯腈109.9Kg(0.79千摩尔),催化剂氢氧化钠1.10Kg和碳酸钠1.10Kg加入反应釜中,开启热蒸气升温,在2小时内滴加51Kg(1.5千摩尔)过氧化氢,滴加完毕,在40℃保温1小时,负压过量的过氧化氢,反应物用离心机甩干,得到二氟苯甲酰胺滤饼112.8Kg(0.718千摩尔),产率为90.9%,含量为98.5%;2) Hydrolysis: Add 109.9Kg (0.79 kilomoles) of difluorobenzonitrile, 1.10Kg catalyst sodium hydroxide and 1.10Kg sodium carbonate to the reactor, turn on the hot steam to raise the temperature, and add 51Kg (1.5 kilomoles) dropwise within 2 hours Hydrogen peroxide, dropwise, was incubated at 40 DEG C for 1 hour, negative pressure was excessive hydrogen peroxide, and the reactant was dried with a centrifuge to obtain 112.8Kg (0.718 kilomoles) of difluorobenzamide filter cake, and the yield was 90.9%, the content is 98.5%;

3)酯化:将2,6-二氟苯甲酰胺滤饼98Kg(0.62千摩尔)和417.2Kg甲苯加入反应釜内,通入光气198.0Kg(1.2千摩尔),加热回流4小时,生成2,6-二氟苯甲酰异氰酸酯104.1Kg(0.57千摩尔),产率91.8%,所得产物可不经提纯直接用于下一步;3) Esterification: 98Kg (0.62 kilomoles) of 2,6-difluorobenzamide filter cake and 417.2Kg toluene were added into the reactor, 198.0Kg (1.2 kilomoles) of phosgene was passed through, heated and refluxed for 4 hours to generate 2,6-difluorobenzoyl isocyanate 104.1Kg (0.57 kilomoles), yield 91.8%, the resulting product can be directly used in the next step without purification;

4)加成:将上步所得的2,6-二氟苯甲酰异氰酸酯91.5Kg(0.5千摩尔),4-(2-氯4-三氟甲基苯氧基)-2-氟苯胺153Kg(0.5千摩尔),以及三乙醇胺1.83Kg溶于500Kg甲苯中,在110℃反应4小时,反应液降至室温,过滤,得到无色晶体氟虫脲209.8Kg(0.43千摩尔),产率85.1%,含量99.0%,将滤液进一步浓缩,还可得到氟虫脲2.2Kg,计入产率为86.9%。4) Addition: 91.5Kg (0.5 kilomole) of 2,6-difluorobenzoyl isocyanate obtained in the previous step, 153Kg of 4-(2-chloro4-trifluoromethylphenoxy)-2-fluoroaniline (0.5 kilomol), and 1.83Kg of triethanolamine was dissolved in 500Kg toluene, reacted for 4 hours at 110 ℃, and the reaction solution was lowered to room temperature, and filtered to obtain 209.8Kg (0.43 kilomol) of colorless crystal fiflubenzuron, with a yield of 85.1 %, the content is 99.0%, and the filtrate is further concentrated to obtain 2.2Kg of flubenzuron, and the calculated yield is 86.9%.

实施例3Example 3

1)氟化:在1000L反应釜中加入500Kg环丁砜,边搅拌边加入经喷雾干燥处理过的细粒氟化钾(500目)106.0Kg(1.8千摩尔),2,6-二氯苯腈172Kg(1千摩尔),以及由50wt%四丁基氯化铵和50wt%甲基三辛基氯化铵组成的催化剂混合物3.44Kg,于200℃加热9小时,过滤,滤去沉淀的氯化钾,将滤液分馏得到2,6-二氟苯腈133.7Kg(0.96千摩尔),产率为96.2%,含量为98.8%,并回收溶剂环丁砜;1) Fluorination: Add 500Kg sulfolane to a 1000L reactor, and add 106.0Kg (1.8 kilomoles) of fine-grained potassium fluoride (500 mesh) that has been spray-dried while stirring, and 172Kg of 2,6-dichlorobenzonitrile (1 kilomole), and the catalyst mixture 3.44Kg that is made up of 50wt% tetrabutylammonium chloride and 50wt% methyltrioctylammonium chloride, in 200 ℃ of heating 9 hours, filter, filter the potassium chloride of precipitation , the filtrate was fractionally distilled to obtain 2,6-difluorobenzonitrile 133.7Kg (0.96 kilomoles), the productive rate was 96.2%, and the content was 98.8%, and the solvent sulfolane was recovered;

2)水解:将2,6-二氟苯腈109.9Kg(0.79千摩尔),催化剂碳酸氢钠1.65Kg和碳酸钠1.65Kg加入反应釜中,开启热蒸气升温,在2小时内滴加102Kg(3.0千摩尔)过氧化氢,滴加完毕,在40℃保温1小时,负压过量的过氧化氢,反应物用离心机甩干,得到2,6-二氟苯甲酰胺滤饼115.1Kg(0.733千摩尔),产率为92.8%,含量为98.8%;2) Hydrolysis: 109.9Kg (0.79 kilomoles) of 2,6-difluorobenzonitrile, 1.65Kg of catalyst sodium bicarbonate and 1.65Kg of sodium carbonate were added to the reactor, and the hot steam was turned on to raise the temperature, and 102Kg ( 3.0 kilomoles) hydrogen peroxide, dropwise, at 40 ℃ of insulation 1 hour, negative pressure is excessive hydrogen peroxide, and reactant is dried with centrifuge, obtains 2,6-difluorobenzamide filter cake 115.1Kg ( 0.733 kilomol), the productive rate is 92.8%, and the content is 98.8%;

3)酯化:将2,6-二氟苯甲酰胺滤饼98Kg(0.62千摩尔)和417.2Kg甲苯加入反应釜内,通入光气148.5Kg(1.51千摩尔),加热回流4小时,生成2,6-二氟苯甲酰异氰酸酯106.1Kg(0.58千摩尔),产率93.5%,所得产物可不经提纯直接用于下一步;3) Esterification: 98Kg (0.62 kilomoles) of 2,6-difluorobenzamide filter cake and 417.2Kg toluene were added into the reaction kettle, 148.5Kg (1.51 kilomoles) of phosgene was passed through, heated and refluxed for 4 hours to generate 2,6-difluorobenzoyl isocyanate 106.1Kg (0.58 kilomoles), yield 93.5%, the resulting product can be directly used in the next step without purification;

4)加成:将上步所得的2,6-二氟苯甲酰异氰酸酯91.5Kg(0.5千摩尔),4-氯苯胺63.5Kg(0.5千摩尔),以及三乙醇胺1.37Kg和三乙胺1.37Kg溶于500Kg甲苯中,在105℃反应5小时,反应液降至室温,过滤,得到白色晶体除虫脲148.8Kg(0.48千摩尔),产率96.0%,含量98.0%,将滤液进一步浓缩,还可得到除虫脲2.2Kg,计入产率为97.4%。4) Addition: 91.5Kg (0.5 kilomoles) of 2,6-difluorobenzoyl isocyanate obtained in the previous step, 63.5Kg (0.5 kilomoles) of 4-chloroaniline, 1.37Kg triethanolamine and 1.37 kilomoles triethylamine Kg was dissolved in 500Kg toluene, reacted at 105°C for 5 hours, the reaction solution was cooled to room temperature, and filtered to obtain 148.8Kg (0.48 kilomoles) of white crystal diflubenzuron, with a yield of 96.0% and a content of 98.0%. The filtrate was further concentrated, 2.2 Kg of diflubenzuron can also be obtained, and the calculated yield is 97.4%.

Claims (1)

1. A synthetic method of a substituted benzoyl urea insect growth regulator comprises the following steps:
1) fluorination: heating a mixture of 1 mol of 2, 6-dichlorobenzonitrile, 1.5-2.0 mol of 450-mesh 550-mesh anhydrous potassium fluoride, a solvent and a catalyst A in a reaction kettle at 200 ℃ for 8-10 hours, filtering, fractionating the filtrate to obtain 2, 6-difluorobenzonitrile, and recovering the solvent;
the solvent is sulfolane;
the catalyst A is a mixture of tetrabutylammonium chloride and methyl trioctyl ammonium chloride, wherein the tetrabutylammonium chloride accounts for 40-60 wt%; the amount of the catalyst A is 1-3 wt% of the weight of the 2, 6-dichlorobenzonitrile;
2) hydrolysis: adding 1 mol of 2, 6-difluorobenzonitrile obtained in the step 1) and a catalyst B into a reaction kettle, dripping excessive hydrogen peroxide while stirring, keeping the reaction temperature at 40 ℃, keeping the temperature for 1 hour after finishing dripping, removing unreacted hydrogen peroxide under negative pressure, and spin-drying a reactant by a centrifuge to obtain a 2, 6-difluorobenzamide filter cake;
the catalyst B is one or two of sodium hydroxide, sodium carbonate or sodium bicarbonate in a weight ratio of 1: 1; the amount of the catalyst B is 1-3 wt% of the weight of the 2, 6-difluorobenzonitrile;
3) esterification: dissolving the 2, 6-difluorobenzamide filter cake obtained in the step 2) in a solvent, introducing excessive phosgene, and heating and refluxing for 4 hours to generate 2, 6-difluorobenzoyl isocyanate; the obtained product can be directly used in the next step without purification;
the solvent is toluene;
4) addition: dissolving the 2, 6-difluorobenzoyl isocyanate obtained in the step 3) in toluene, adding equimolar substituted aniline and a catalyst C, and reacting at 100-110 ℃ for 4-6 hours to obtain a substituted benzoyl urea insect growth regulator;
the substituted aniline is 4-chloroaniline, 3, 5-dichloro-4- (1, 1, 2, 2-tetrafluoroethoxy) aniline or 4- (2-chloro-4-trifluoromethylphenoxy) -2-fluoroaniline;
the catalyst C is triethylamine or/and triethanolamine; the amount of the catalyst C is 1-3 wt% of the weight of the 2, 6-difluorobenzoyl isocyanate.
CN 03153528 2003-08-15 2003-08-15 Substituted benzoyl urea insect growth regulator synthesizing method Expired - Fee Related CN1218935C (en)

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JP5061635B2 (en) * 2007-02-15 2012-10-31 ダイキン工業株式会社 Process for producing 4-fluoro-1,3-dioxolan-2-one
CN101462980B (en) * 2009-01-05 2013-01-09 扬州天辰精细化工有限公司 Industrial production method of 2,6-difluorobenzamide
CN101456827B (en) * 2009-01-05 2012-07-04 扬州天辰精细化工有限公司 Industrial production method of 2,6-difluorobenzene nitrile
CN103012162B (en) * 2012-12-25 2014-12-03 大连奇凯医药科技有限公司 Preparation method of pentafluoroaniline
US8907146B2 (en) * 2013-02-04 2014-12-09 Honeywell International Inc. Process for the preparation of 1-chloro-3,3,3-trifluoropropene using a phase transfer catalyst
CN104788341B (en) * 2014-01-17 2017-01-04 上海泰禾国际贸易有限公司 A kind of method preparing 2,6-difluorobenzonilyile
CN108623491B (en) * 2017-03-24 2020-12-22 联化科技股份有限公司 Preparation method of halogenated benzamide compound
CN111116399A (en) * 2019-12-20 2020-05-08 杨向党 Process for producing 2, 6-difluorobenzamide
CN112920088A (en) * 2021-02-01 2021-06-08 京博农化科技有限公司 Synthetic method of diflubenzuron impurities for quantitative and qualitative analysis
CN113368896B (en) * 2021-06-11 2022-07-29 河北威远生物化工有限公司 Catalyst for diflubenzuron synthesis and preparation method of diflubenzuron
CN113620841A (en) * 2021-08-03 2021-11-09 南京硕达生物科技有限公司 Method for preparing 2, 6-difluorobenzonitrile
CN113666844A (en) * 2021-09-22 2021-11-19 德州绿霸精细化工有限公司 Method for continuously producing 2, 6-difluorobenzoyl isocyanate
CN113929595B (en) * 2021-11-12 2024-09-06 江苏新河农用化工有限公司 Preparation method of 2, 6-difluorobenzonitrile

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