WO2007072679A1 - Process for producing 2,4-difluoronitrobenzene - Google Patents

Process for producing 2,4-difluoronitrobenzene Download PDF

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WO2007072679A1
WO2007072679A1 PCT/JP2006/324308 JP2006324308W WO2007072679A1 WO 2007072679 A1 WO2007072679 A1 WO 2007072679A1 JP 2006324308 W JP2006324308 W JP 2006324308W WO 2007072679 A1 WO2007072679 A1 WO 2007072679A1
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difluoronitrobenzene
reaction
producing
potassium fluoride
internal temperature
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Koji Hagiya
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Sumitomo Chemical Company, Limited
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
    • C07C201/06Preparation of nitro compounds
    • C07C201/12Preparation of nitro compounds by reactions not involving the formation of nitro groups

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  • the present invention relates to a method for producing 2,4-difluoronitrobenzene.
  • 2,4-Difluoronitrobenzene is useful as an intermediate for the synthesis of medicines and agrochemicals (see US Pat. No. 4 1 645 17).
  • the production method thereof is in the presence of sulfolane or dimethyl sulfoxide.
  • a method of reacting 2,4-dichloronitrobenzene with potassium fluoride see US Pat. No. 4 1 645 17 and J. Amer. Chem. So, U, 6034 (1956)).
  • a method of reacting 2,4-dichloronitrile benzene and potassium fluoride in the presence of a phase transfer catalyst is also known (US Pat. No. 5,545,681, US Pat. Publication No. 2004-24238).
  • the present invention provides the following formula (1)
  • the present invention provides a method for producing 2,4-difluoronitrobenzene, which comprises reacting 2,4-dichloronitrobenzene with potassium fluoride in the presence of a sulfone compound represented by formula (1).
  • 2,4-dichloronitrobenzene a commercially available product may be used, or one produced by a known method such as a method of nitration of m-dichlorobenzene may be used.
  • potassium fluoride a commercially available one may be used, and for example, a potassium fluoride obtained by a known method such as a method of reacting hydroxylated hydrogen with hydrogen fluoride may be used. It is preferable to use potassium fluoride having a small particle size. It is preferable to use potassium fluoride having a low water content. Suitable potassium fluoride includes potassium fluoride produced by a spray dry method.
  • the amount of potassium fluoride used is usually 1 mol of 2,4-dichloronitrobenzene,
  • the upper limit is not particularly limited, but 2 to 5 mol is preferable with respect to 1 mol of 2,4-dichloronitrobenzene from the economical viewpoint.
  • R 1 and R 2 are the same or different and each represents an alkyl group having 1 to 3 carbon atoms.
  • the alkyl group having 1 to 3 carbon atoms include linear or branched alkyl groups such as a methyl group, an ethyl group, a propyl group, and an isopyl pill group.
  • R 1 is a methyl group (1) is preferred instrument, R 1 is a methyl group, sulfone compounds wherein R 2 is a methyl group or Echiru group (1) power beams Preferably, R 1 is a methyl group A sulfone compound (1) in which R 2 is a methyl group is more preferable.
  • Examples of the sulfone compound (1) include dimethylsulfone, methylethylsulfone, methylpropylsulfone, methylisopropylsulfone, jetylsulfone, dipropylsulfone and the like, and dimethylsulfone and methylethylsulfone are preferable. From the viewpoint of availability, dimethyl sulfone is more preferable.
  • the sulfone compound (1) a commercially available product may be used, or a sulfone compound produced by a known method such as a method of oxidizing a corresponding sulfide compound or sulfoxide compound with an oxidizing agent such as hydrogen peroxide. Also good.
  • the amount of the sulfone compound (1) used is usually 0.1 to 20 times the weight of 2,4-dichloronitrobenzene.
  • the reaction temperature is usually from 120 to 200, preferably from 150 to 200.
  • the reaction may be carried out without solvent or in the presence of an organic solvent inert to the reaction.
  • dimethyl sulfone is used as the sulfone compound (1), it is preferably carried out in the presence of an organic solvent inert to the reaction.
  • organic solvent inert to the reaction examples include ether solvents such as dioxane and diethylene glycol dimethyl ether; amide solvents such as N, N-dimethylacetamide; aromatic carbonization such as toluene, xylene, black benzene, and benzonitrile. Hydrogen solvent; aliphatic hydrocarbon solvents such as octane and decane are listed, and aromatic hydrocarbon solvents and aliphatic hydrocarbon solvents are preferred. These organic solvents inert to the reaction may be used alone or in admixture of two or more. Of these, organic solvents that are inert to the reaction and have a boiling point of 100 to 200 ° C. are preferred.
  • the amount of the organic solvent inert to the reaction is usually 0.001 to 0.5 times by weight, preferably 0.001 to 0.2 times by weight, relative to the sulfone compound (1). is there.
  • This reaction is carried out by combining 2,4-dichloronitrobenzene, potassium fluoride, a sulfone compound (1) and, if necessary, an organic solvent inert to the reaction, and keeping the reaction temperature at a predetermined temperature while stirring.
  • the mixing order is not particularly limited.
  • potassium fluoride has the property of easily absorbing moisture
  • a method for removing water contained in potassium fluoride for example, a method of mixing potassium fluoride and a sulfone compound (1) and heating to remove water; azeotrope with water such as toluene or xylene
  • azeotrope with water such as toluene or xylene
  • a method in which an organic solvent, potassium fluoride, and a sulfone compound (1) are mixed and heated to remove water as an azeotrope.
  • the reaction is usually carried out under normal pressure conditions, but may be carried out under pressurized conditions.
  • the progress of the reaction can be confirmed by ordinary analytical means such as gas chromatography or liquid chromatography.
  • potassium chloride is usually precipitated in the reaction mixture. Therefore, an organic solvent insoluble in water is added to the reaction mixture as necessary, and the precipitated lithium chloride is separated by filtration, and then water is added. In addition, an organic layer containing 2,4-difluoronitrobenzene can be obtained by liquid separation treatment. By concentrating the resulting organic layer, 2,4-difluoronitrobenzene can be extracted. Without separating the precipitated potassium chloride, the reaction mixture and water may be mixed and separated. When recovering the used sulfone compound (1), it is preferable to separate the precipitated potassium chloride and then perform a liquid separation treatment. The taken 2,4-difluoronitrobenzene may be further purified by a conventional purification means such as crystallization or column chromatography.
  • organic solvents insoluble in water examples include aromatic hydrocarbon solvents such as toluene, xylene, black benzene, etc .; aliphatic hydrocarbon solvents such as pentane, hexane, heptane, etc .; halogenations such as dichloromethane, dichloromethane, black mouth form, etc.
  • aromatic hydrocarbon solvents such as toluene, xylene, black benzene, etc .
  • aliphatic hydrocarbon solvents such as pentane, hexane, heptane, etc .
  • halogenations such as dichloromethane, dichloromethane, black mouth form, etc.
  • hydrocarbon solvents examples include hydrocarbon solvents; ether solvents such as jetyl ether and methyl tert-butyl ether; and ester solvents such as ethyl acetate, and the amount used is not particularly limited.
  • the sulfone compound (1) is contained in the aqueous layer separated from the organic layer containing 2,4-difluoronitrobenzene, and the aqueous layer is concentrated to remove water. Thus, the sulfone compound (1) can be recovered. The recovered sulfone compound (1) can be reused for the reaction between 2,4-dichloronitrobenzene and potassium fluoride. When potassium chloride is contained in the aqueous layer, the sulfone compound (1) is usually recovered after removing the potassium chloride by desalting or filtration.
  • Example EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. Yield was calculated by gas chromatography internal standard method. Example 1
  • reaction mixture was cooled to an internal temperature of 100, 10 g of xylene and 10 g of water were added, and liquid separation treatment was performed to obtain an organic layer containing 2,4-difluoronitrobenzene.
  • a 50 mL flask equipped with a reflux condenser was charged with 730 mg of the same fluorinated rhodium used in Example 1, 5 g of methylethylsulfone, and 10 g of toluene.
  • the obtained mixture was heated to an internal temperature of 130, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all of toluene was distilled off at an internal temperature of 14 O :, and the resulting mixture was cooled to an internal temperature of 100.
  • the mixture was charged with 96 mg of 2,4-dichloronitrobenzene and allowed to react at an internal temperature of 170 for 12 hours. After completion of the reaction, the reaction mixture is cooled to an internal temperature of 6 Ot :, 10 g of toluene and 10 g of water are added, liquid separation treatment is performed, and an organic layer containing 2,4-difluoronitrobenzene is added. Obtained.
  • a 5 OmL flask equipped with a reflux condenser was charged with 73.0 mg of potassium fluoride (powder product), 5 g of dimethylsulfone, and 1 Og of toluene.
  • the obtained mixture was heated to an internal temperature of 1300C, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all of toluene was distilled off at an internal temperature of 140 ° C., and the resulting mixture was cooled to an internal temperature of 100 ° C.
  • reaction mixture was cooled to an internal temperature of 100 ° C, 10 g of xylene and 10 g of water were added, and liquid separation treatment was performed to obtain an organic layer containing 2,4-difluoronitrobenzene. .
  • a 5 Oml flask equipped with a reflux condenser was charged with 73 Omg of potassium fluoride, 5 g of dimethylsulfone and 10 g of toluene as used in Example 1 above.
  • the obtained mixture was heated to an internal temperature of 1300C, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all toluene was distilled off at an internal temperature of 140 ° C, and the resulting mixture was cooled to an internal temperature of 100 ° C.
  • reaction mixture was cooled to an internal temperature of 60, and 10 g of toluene and 10 g of water were added.
  • liquid separation treatment was performed to obtain an organic layer containing '2,4-difluoronitrobenzene.
  • 2,4-difluoronitrobenzene useful as a synthetic intermediate for pharmaceuticals and agricultural chemicals can be produced.

Abstract

A process for producing 2,4-difluoronitrobenzene characterized by reacting 2,4-dichloronitrobenzene with potassium fluoride in the presence of a sulfone compound represented by the formula (1): R1-SO2-R2 (1) (wherein R1 and R2 are the same or different and each represents C1-3 alkyl).

Description

2, 4—ジフルォロニトロベンゼンの製造方法  2, 4-Difluoronitrobenzene production method
技術分野 Technical field
本発明は、 2, 4—ジフルォロニトロベンゼンの製造方法に関する。  The present invention relates to a method for producing 2,4-difluoronitrobenzene.
明 背景技術  Background art
 book
2, 4—ジフルォロニトロベンゼンは、 医農薬の合成中問体として有用であり (米国 特許第 4 1 645 1 7号明細書参照)、 その製造方法としては、 スルホランまたはジメチ ルスルホキシドの存在下に、 2, 4—ジクロロニトロベンゼンとフッ化カリウムとを反応 させる方法が知られている (米国特許第 4 1 645 1 7号明細書および J. Amer. Chem. So , U, 6034 (1956) 参照)。 また、 相間移動触媒の存在下に、 2, 4—ジクロロニ卜 口ベンゼンとフッ化カリウムとを反応させる方法も知られている (米国特許第 5 5457 68号、 米国特許公開第 2004— 24238号公報、 米国特許第 7 145 1 1 1号明細 書、米国特許第 5 502260号明細書、特開平 3— 778 50号公報および Tetrahedron, 51, 6363 (1995) 参照)。  2,4-Difluoronitrobenzene is useful as an intermediate for the synthesis of medicines and agrochemicals (see US Pat. No. 4 1 645 17). The production method thereof is in the presence of sulfolane or dimethyl sulfoxide. In addition, there is known a method of reacting 2,4-dichloronitrobenzene with potassium fluoride (see US Pat. No. 4 1 645 17 and J. Amer. Chem. So, U, 6034 (1956)). ). In addition, a method of reacting 2,4-dichloronitrile benzene and potassium fluoride in the presence of a phase transfer catalyst is also known (US Pat. No. 5,545,681, US Pat. Publication No. 2004-24238). U.S. Pat. No. 7,145,111, U.S. Pat. No. 5,502,260, JP-A-3-77850 and Tetrahedron, 51, 6363 (1995)).
発明の開示 Disclosure of the invention
本発明は、 式 (1)  The present invention provides the following formula (1)
R1-S02-R2 (1) R 1 -S0 2 -R 2 (1)
(式中、 ! 'ぉょび1 2は、 それぞれ同一または相異なって炭素数 1〜3のアルキル基を表 わす。) (In the formula,! 1 and 2 are the same or different and each represents an alkyl group having 1 to 3 carbon atoms.)
で示されるスルホン化合物の存在下、 2, 4ージクロロニトロベンゼンとフッ化カリウム とを反応させることを特徴とする 2, 4—ジフルォロニトロベンゼンの製造方法を提供す. るものである。 発明を実施するための最良の形態 The present invention provides a method for producing 2,4-difluoronitrobenzene, which comprises reacting 2,4-dichloronitrobenzene with potassium fluoride in the presence of a sulfone compound represented by formula (1). BEST MODE FOR CARRYING OUT THE INVENTION
2 , 4—ジクロロニトロベンゼンは、 市販のものを用いてもよいし、 例えば m—ジク ロロベンゼンをニトロ化する方法等の公知の方法により製造したものを用いてもよい。  As 2,4-dichloronitrobenzene, a commercially available product may be used, or one produced by a known method such as a method of nitration of m-dichlorobenzene may be used.
フッ化カリウムとしては、 市販されているものを用いてもよいし、 例えば、 水酸化力 リゥムとフッ化水素とを反応させる方法等の公知の方法により得られたものを用いても よい。 粒径の小さいフッ化カリウムを用いることが好ましい。 含水量の少ないフッ化カリ ゥムを用いることが好ましい。 好適なフッ化カリウムとしては、 スプレイドライ法で製造 されたフッ化カリウムが挙げられる。  As the potassium fluoride, a commercially available one may be used, and for example, a potassium fluoride obtained by a known method such as a method of reacting hydroxylated hydrogen with hydrogen fluoride may be used. It is preferable to use potassium fluoride having a small particle size. It is preferable to use potassium fluoride having a low water content. Suitable potassium fluoride includes potassium fluoride produced by a spray dry method.
フッ化カリウムの使用量は、 2, 4—ジクロロニトロベンゼン 1モルに対して、通常、 The amount of potassium fluoride used is usually 1 mol of 2,4-dichloronitrobenzene,
2モル以上である。 その上限は特にないが、 経済的な観点から、 2, 4—ジクロロニトロ ベンゼン 1モルに対して、 2〜 5モルが好ましい。 2 moles or more. The upper limit is not particularly limited, but 2 to 5 mol is preferable with respect to 1 mol of 2,4-dichloronitrobenzene from the economical viewpoint.
上記式 (1 ) で示されるスルホン化合物 (以下、 スルホン化合物 (1 ) と略記する。) において、 R 1および R 2はそれぞれ同一または相異なって、 炭素数 1〜3のアルキル基を 表わす。 炭素数 1〜 3のアルキル基としては、 メチル基、 ェチル基、 プロピル基、 イソプ 口ピル基等の直鎖状もしくは分枝鎖状のアルキル基が挙げられる。 R 1がメチル基である スルホン化合物 (1 ) が好ましぐ、 R 1がメチル基であり、 R 2がメチル基またはェチル基 であるスルホン化合物 (1 ) 力はり好ましく、 R 1がメチル基であり、 R 2がメチル基であ るスルホン化合物 (1 ) がさらに好ましい。 In the sulfone compound represented by the above formula (1) (hereinafter abbreviated as the sulfone compound (1)), R 1 and R 2 are the same or different and each represents an alkyl group having 1 to 3 carbon atoms. Examples of the alkyl group having 1 to 3 carbon atoms include linear or branched alkyl groups such as a methyl group, an ethyl group, a propyl group, and an isopyl pill group. Sulfone compound R 1 is a methyl group (1) is preferred instrument, R 1 is a methyl group, sulfone compounds wherein R 2 is a methyl group or Echiru group (1) power beams Preferably, R 1 is a methyl group A sulfone compound (1) in which R 2 is a methyl group is more preferable.
かかるスルホン化合物 (1 ) としては、 ジメチルスルホン、 メチルェチルスルホン、 メチルプロピルスルホン、 メチルイソプロピルスルホン、 ジェチルスルホン、 ジプロピル スルホン等が挙げられ、 ジメチルスルホン、 メチルェチルスルホンが好ましい。 入手性の 点で、 ジメチルスルホンがより好ましい。  Examples of the sulfone compound (1) include dimethylsulfone, methylethylsulfone, methylpropylsulfone, methylisopropylsulfone, jetylsulfone, dipropylsulfone and the like, and dimethylsulfone and methylethylsulfone are preferable. From the viewpoint of availability, dimethyl sulfone is more preferable.
スルホン化合物 (1 ) は、 市販のものを用いてもよいし、 対応するスルフイ ド化合物 もしくはスルホキシド化合物を過酸化水素等の酸化剤により酸化する方法等の公知の方 法により製造したものを用いてもよい。 スルホン化合物( 1 ) の使用量は、 2, 4—ジクロロニトロベンゼンに対して、通常、 0 . 1〜2 0重量倍である。 As the sulfone compound (1), a commercially available product may be used, or a sulfone compound produced by a known method such as a method of oxidizing a corresponding sulfide compound or sulfoxide compound with an oxidizing agent such as hydrogen peroxide. Also good. The amount of the sulfone compound (1) used is usually 0.1 to 20 times the weight of 2,4-dichloronitrobenzene.
反応温度は、 通常 1 2 0〜2 0 0で、 好ましくは 1 5 0〜2 0 0でである。  The reaction temperature is usually from 120 to 200, preferably from 150 to 200.
反応は、 無溶媒で実施してもよいし、 反応に不活性な有機溶媒の存在下に実施しても よい。 スルホン化合物 (1 ) としてジメチルスルホンを用いる場合には、 反応に不活性な 有機溶媒の存在下に実施することが好ましい。  The reaction may be carried out without solvent or in the presence of an organic solvent inert to the reaction. When dimethyl sulfone is used as the sulfone compound (1), it is preferably carried out in the presence of an organic solvent inert to the reaction.
反応に不活性な有機溶媒としては、 ジォキサン、 ジエチレングリコールジメチルエー テル等のエーテル溶媒; N, N—ジメチルァセトアミド等のアミド溶媒; トルエン、 キシ レン、 クロ口ベンゼン、 ベンゾニトリル等の芳香族炭化水素溶媒;オクタン、 デカン等の 脂肪族炭化水素溶媒等が挙げられ、芳香族炭化水素溶媒、脂肪族炭化水素溶媒が好ましい。 かかる反応に不活性な有機溶媒は、 それぞれ単独で用いてもよいし、 二種以上を混合して 用いてもよい。 なかでも、 反応に不活性であって、 その沸点が 1 0 0〜2 0 0 °Cである有 機溶媒が好ましい。  Examples of the organic solvent inert to the reaction include ether solvents such as dioxane and diethylene glycol dimethyl ether; amide solvents such as N, N-dimethylacetamide; aromatic carbonization such as toluene, xylene, black benzene, and benzonitrile. Hydrogen solvent; aliphatic hydrocarbon solvents such as octane and decane are listed, and aromatic hydrocarbon solvents and aliphatic hydrocarbon solvents are preferred. These organic solvents inert to the reaction may be used alone or in admixture of two or more. Of these, organic solvents that are inert to the reaction and have a boiling point of 100 to 200 ° C. are preferred.
反応に不活性な有機溶媒の使用量は、 スルホン化合物 (1 ) に対して、 通常 0 . 0 0 1〜0 . 5重量倍であり、 好ましくは 0 . 0 0 1〜0 . 2重量倍である。  The amount of the organic solvent inert to the reaction is usually 0.001 to 0.5 times by weight, preferably 0.001 to 0.2 times by weight, relative to the sulfone compound (1). is there.
本反応は、 2 , 4ージクロロニトロベンゼン、 フッ化カリウム、 スルホン化合物 (1 ) および必要により反応に不活性な有機溶媒とを 合し、 攪拌し がら、 所定の反応温度で 保持することにより実施される。 混合順序は特に限定されない。  This reaction is carried out by combining 2,4-dichloronitrobenzene, potassium fluoride, a sulfone compound (1) and, if necessary, an organic solvent inert to the reaction, and keeping the reaction temperature at a predetermined temperature while stirring. The The mixing order is not particularly limited.
本反応においては、 反応系内の水分が少ないほどスムーズに反応が進行する。 フッ化 カリウムは吸湿しやすい性質を有しているため、 フッ化カリウムに含まれる水分を予め除 去した後、 反応を実施することが好ましい。 フッ化カリウムに含まれる水分を除去する方 法としては、 例えば、 フッ化カリウムとスルホン化合物 (1 ) とを混合し、 加熱して、 水 を除去する方法; トルエン、 キシレン等の水と共沸する有機溶媒とフッ化カリウムとスル ホン化合物 (1 ) とを混合し、 加熱して、 共沸混合物として水を除去する方法;等が挙げ られる。 フッ化カリウムに含まれる水分を予め除去する場合、 水を除去して得られるフッ . 化カリウムとスルホン化合物 (1 ) とを含む混合物と 2 , 4—ジクロロニトロベンゼンと を混合することに り、 反応が実施される。 In this reaction, the reaction proceeds more smoothly as the water content in the reaction system decreases. Since potassium fluoride has the property of easily absorbing moisture, it is preferable to carry out the reaction after removing the water contained in potassium fluoride in advance. As a method for removing water contained in potassium fluoride, for example, a method of mixing potassium fluoride and a sulfone compound (1) and heating to remove water; azeotrope with water such as toluene or xylene A method in which an organic solvent, potassium fluoride, and a sulfone compound (1) are mixed and heated to remove water as an azeotrope. When water contained in potassium fluoride is removed in advance, a mixture containing potassium fluoride and sulfone compound (1) obtained by removing water and 2,4-dichloronitrobenzene and The reaction is carried out by mixing.
反応は、 通常、 常圧条件下で実施されるが、 加圧条件下に実施してもよい。 反応の進 行は、 例えばガスクロマトグラフィ一や液体ク口マトグラフィ一等の通常の分析手段によ り確認することができる。  The reaction is usually carried out under normal pressure conditions, but may be carried out under pressurized conditions. The progress of the reaction can be confirmed by ordinary analytical means such as gas chromatography or liquid chromatography.
反応終了後、 通常、 反応混合物中に塩化カリウムが析出しているため、 反応混合物に 必要に応じて水に不溶な有機溶媒を加え、 析出した塩化力リウムを瀘過により分離した後、 水を加え、 分液処理することにより、 2, 4—ジフルォロニトロベンゼンを含む有機層を 得ることができる。 得られた有機層を濃縮することにより、 2, 4—ジフルォロニトロべ ンゼンを取り出すことができる。 析出した塩化カリウムを分離することなく、 反応混合物 と水とを混合し、分液処理してもよい。用いたスルホン化合物(1 ) を回収する場合には、 析出した塩化カリウムを分離した後、 分液処理することが好ましい。 取り出した 2 , 4— ジフルォロニトロベンゼンは、 例えば晶析、 カラムクロマトグラフィ等の通常の精製手段 によりさらに精製してもよい。  After completion of the reaction, potassium chloride is usually precipitated in the reaction mixture. Therefore, an organic solvent insoluble in water is added to the reaction mixture as necessary, and the precipitated lithium chloride is separated by filtration, and then water is added. In addition, an organic layer containing 2,4-difluoronitrobenzene can be obtained by liquid separation treatment. By concentrating the resulting organic layer, 2,4-difluoronitrobenzene can be extracted. Without separating the precipitated potassium chloride, the reaction mixture and water may be mixed and separated. When recovering the used sulfone compound (1), it is preferable to separate the precipitated potassium chloride and then perform a liquid separation treatment. The taken 2,4-difluoronitrobenzene may be further purified by a conventional purification means such as crystallization or column chromatography.
水に不溶の有機溶媒としては、 トルエン、 キシレン、 クロ口ベンゼン等の芳香族炭化 水素溶媒;ペンタン、 へキサン、 ヘプタン等の脂肪族炭化水素溶媒; ジクロロメタン、 ジ クロロェタン、 クロ口ホルム等のハロゲン化炭化水素溶媒; ジェチルエーテル、 メチル t e r' t一ブチルエーテル等のエーテル溶媒;および、 酢酸ェチル等のエステル溶媒等が挙 げられ、 その使用量は特に限定されない。  Examples of organic solvents insoluble in water include aromatic hydrocarbon solvents such as toluene, xylene, black benzene, etc .; aliphatic hydrocarbon solvents such as pentane, hexane, heptane, etc .; halogenations such as dichloromethane, dichloromethane, black mouth form, etc. Examples include hydrocarbon solvents; ether solvents such as jetyl ether and methyl tert-butyl ether; and ester solvents such as ethyl acetate, and the amount used is not particularly limited.
前記分液処理において、 2, 4ージフルォロニトロベンゼンを含む有機層と分離した 水層中に、 スルホン化合物 (1 ) が含まれており、 かかる水層を濃縮して水を除去するこ とにより、 スルホン化合物 (1 ) を回収することができる。 回収したスルホン化合物 (1 ) は、 2 , 4ージクロロニトロベンゼンとフッ化カリウムとの反応に再利用することができ る。 かかる水層中に、 塩化カリウムが含まれているときは、 通常、 脱塩処理や濾過処理等 により塩化カリウムを除去した後、 スルホン化合物 (1 ) が回収される。 実施例 以下、 実施例により本発明をさらに詳細に説明するが、 本発明はこれら実施例に限定 されるものではない。 収率は、 ガスクロマトグラフィー内部標準法により算出した。 実施例 1 In the liquid separation treatment, the sulfone compound (1) is contained in the aqueous layer separated from the organic layer containing 2,4-difluoronitrobenzene, and the aqueous layer is concentrated to remove water. Thus, the sulfone compound (1) can be recovered. The recovered sulfone compound (1) can be reused for the reaction between 2,4-dichloronitrobenzene and potassium fluoride. When potassium chloride is contained in the aqueous layer, the sulfone compound (1) is usually recovered after removing the potassium chloride by desalting or filtration. Example EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. Yield was calculated by gas chromatography internal standard method. Example 1
還流冷却管を付した 5OmLフラスコに、 フッ化カリウム (スフ。レイドライ品) 73 In a 5OmL flask equipped with a reflux condenser, potassium fluoride (sulfur dry product) 73
Omg、 ジメチルスルホン 5 gおよびトルエン 10 gを仕込んだ。 得られた混合物を、 内 温 13 CTCに加熱し、 該混合物中の水分をトルエンとの共沸混合物として除去した。 その 後、 内温 140ででトルエンのほぼ全量を留去し、 得られた混合物を内温 100°Cまで冷 却した。 Omg, 5 g of dimethylsulfone and 10 g of toluene were charged. The resulting mixture was heated to an internal temperature of 13 CTC, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all of toluene was distilled off at an internal temperature of 140, and the resulting mixture was cooled to an internal temperature of 100 ° C.
該混合物に、 2, 4—ジクロロニ卜口ベンゼン 96 Omgおよびキシレン 30 Omg を仕込み、 内温 170°Cで 12時間反応させた。 還流冷却管やフラスコ内面へのジメチル スルホンの付着は見られなかった。  The mixture was charged with 96 Omg of 2,4-dichloronitric benzene and 30 Omg of xylene, and reacted at an internal temperature of 170 ° C for 12 hours. Dimethyl sulfone did not adhere to the reflux condenser or the inner surface of the flask.
反応終了後、 反応混合物を、 内温 100でまで冷却し、 キシレン 10 gおよび水 10 gを加え、 分液処理し、 2, 4—ジフルォロニトロベンゼンを含む有機層を得た。  After completion of the reaction, the reaction mixture was cooled to an internal temperature of 100, 10 g of xylene and 10 g of water were added, and liquid separation treatment was performed to obtain an organic layer containing 2,4-difluoronitrobenzene.
2, 4—ジフルォロニトロベンゼンの収率: 94% Yield of 2, 4-difluoronitrobenzene: 94%
モノフルォロクロロニトロベンゼン (2種の異性体の合計) の収率: 5% 実施例 2 Yield of monofluorochloronitrobenzene (sum of the two isomers): 5% Example 2
還流冷却管を付した 50mLフラスコに、 前記実施例 1で用いたと同じフッ化力リウ ム 730mg、 メチルェチルスルホン 5 gおよびトルエン 10 gを仕込んだ。 得られた混 合物を、 内温 130でに加熱し、 該混合物中の水分をトルエンとの共沸混合物として除去 した。 その後、 内温 14 O :でトルエンのほぼ全量を留去し、 得られた混合物を内温 10 0でまで冷却した。  A 50 mL flask equipped with a reflux condenser was charged with 730 mg of the same fluorinated rhodium used in Example 1, 5 g of methylethylsulfone, and 10 g of toluene. The obtained mixture was heated to an internal temperature of 130, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all of toluene was distilled off at an internal temperature of 14 O :, and the resulting mixture was cooled to an internal temperature of 100.
該混合物に、 2, 4—ジクロロニトロベンゼン 96 Omgを仕込み、 内温 170でで 12時間反応させた。 反応終了後、 反応混合物を内温 6 Ot:まで冷却し、 トルエン 10 g および水 10 gを加え、 分液処理し、 2, 4ージフルォロニトロベンゼンを含む有機層を 得た。 The mixture was charged with 96 mg of 2,4-dichloronitrobenzene and allowed to react at an internal temperature of 170 for 12 hours. After completion of the reaction, the reaction mixture is cooled to an internal temperature of 6 Ot :, 10 g of toluene and 10 g of water are added, liquid separation treatment is performed, and an organic layer containing 2,4-difluoronitrobenzene is added. Obtained.
2, 4—ジフルォロニトロベンゼンの収率: 90 %  Yield of 2, 4-difluoronitrobenzene: 90%
モノフルォロクロロニトロベンゼン (2種の異性体の合計) の収率: 9% 実施例 3 Yield of monofluorochloronitrobenzene (sum of the two isomers): 9% Example 3
還流冷却管を付した 5 OmLフラスコに、 フッ化カリウム (粉末品) 73.0mg、 ジ メチルスルホン 5 gおよびトルエン 1 O gを仕込んだ。 得られた混合物を、 内温 1 30°C に加熱し、 該混合物中の水分をトルエンとの共沸混合物として除去した。 その後、 内温 1 40°Cでトルエンのほぼ全量を留去し、 得られた混合 if勿を内温 1 00°Cまで冷却した。  A 5 OmL flask equipped with a reflux condenser was charged with 73.0 mg of potassium fluoride (powder product), 5 g of dimethylsulfone, and 1 Og of toluene. The obtained mixture was heated to an internal temperature of 1300C, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all of toluene was distilled off at an internal temperature of 140 ° C., and the resulting mixture was cooled to an internal temperature of 100 ° C.
該混合物に、 2, 4—ジクロロニトロベンゼン 96ひ mgおよびキシレン 30 Omg を仕込み、 内温 1 70°Cで 8時間反応させた。 還流冷却管やフラスコ内面へのジメチルス ルホンの付着は見られなかった。  The mixture was charged with 96 mg of 2,4-dichloronitrobenzene and 30 Omg of xylene and allowed to react at an internal temperature of 1700C for 8 hours. Dimethyl sulfone did not adhere to the reflux condenser or the inner surface of the flask.
反応終了後、 反応混合物を、 内温 1 00°Cまで冷却し、 キシレン 1 0 gおよび水 1 0 gを加え、 分液処理し、 2, 4—ジフルォロニトロベンゼンを含む有機層を得た。  After completion of the reaction, the reaction mixture was cooled to an internal temperature of 100 ° C, 10 g of xylene and 10 g of water were added, and liquid separation treatment was performed to obtain an organic layer containing 2,4-difluoronitrobenzene. .
2, 4—ジフルォロニトロベンゼンの収率: 89 % Yield of 2, 4-difluoronitrobenzene: 89%
モノフルォロクロロニトロベンゼン (2種の異性体の合計) の収率: 9% 実施例 4 Yield of monofluorochloronitrobenzene (sum of the two isomers): 9% Example 4
還流冷却管を付した 5 Om lフラスコに、 前記実施例 1で用いたと同じフッ化カリウム 73 Omg, ジメチルスルホン 5 gおよびトルエン 1 0 gを仕込んだ。得られた混合物を、 内温 1 30°Cに加熱し、 該混合物中の水分をトルエンとの共沸混合物として除去した。 そ の後、 内温 140°Cでトルエンのほぼ全量を留去し、 得られた混合物を内温 1 00°Cまで 冷却した。  A 5 Oml flask equipped with a reflux condenser was charged with 73 Omg of potassium fluoride, 5 g of dimethylsulfone and 10 g of toluene as used in Example 1 above. The obtained mixture was heated to an internal temperature of 1300C, and water in the mixture was removed as an azeotrope with toluene. Thereafter, almost all toluene was distilled off at an internal temperature of 140 ° C, and the resulting mixture was cooled to an internal temperature of 100 ° C.
該混合物に、 2, 4—ジクロロニトロベンゼン 96 Omgを仕込み、 内温 1 70^で 1 2時間反応させた。 還流冷却管やフラスコ内面へのジメチルスルホンの付着が見られた。  The mixture was charged with 96 Omg of 2,4-dichloronitrobenzene and reacted at an internal temperature of 1700 for 12 hours. Dimethylsulfone adhered to the reflux condenser and the inner surface of the flask.
反応終了後、 反応混合物を内温 60でまで冷却し、 トルエン 10 gおよび水 10 gを 加え、 分液処理し、' 2, 4—ジフルォロニトロベンゼンを含む有機層を得た。 After completion of the reaction, the reaction mixture was cooled to an internal temperature of 60, and 10 g of toluene and 10 g of water were added. In addition, liquid separation treatment was performed to obtain an organic layer containing '2,4-difluoronitrobenzene.
2, 4—ジフルォロニトロベンゼンの収率: 88 % Yield of 2, 4-difluoronitrobenzene: 88%
モノフルォロクロロニトロベンゼン (2種の異性体の合計) の収率: 5% 産業上の利用可能性 Yield of monofluorochloronitrobenzene (sum of the two isomers): 5% Industrial applicability
本発明によれば、 医農薬の合成中間体として有用な 2, 4—ジフルォロニトロべンゼ ンを製造することができる。  According to the present invention, 2,4-difluoronitrobenzene useful as a synthetic intermediate for pharmaceuticals and agricultural chemicals can be produced.

Claims

請 求 の 範 囲 The scope of the claims
1. 式 (1) 1. Formula (1)
R1 - S02-R2 (1) R 1 -S0 2 -R 2 (1)
(式中、 R1および R2は、 それぞれ同一または相異なって炭素数 1〜3のアルキル基を表 わす。) (In the formula, R 1 and R 2 are the same or different and each represents an alkyl group having 1 to 3 carbon atoms.)
で示されるスルホン化合物の存在下、 2, 4—ジクロロニトロベンゼンとフッ化カリウム とを反応させることを特徴とする 2, 4—ジフルォロニトロベンゼンの製造方法。 A process for producing 2,4-difluoronitrobenzene, comprising reacting 2,4-dichloronitrobenzene with potassium fluoride in the presence of a sulfone compound represented by the formula:
2. R1が、 メチル基である請求の範囲第 1項に記載の 2, 4ージフルォロニ トロベンゼンの製造方法。 2. The method for producing 2,4-difluoronitrobenzene according to claim 1 , wherein R 1 is a methyl group.
3. R1が、 メチル基であり、 R2が、 メチル基である請求の範囲第 1項に記 載の 2, 4—ジフルォロニトロベンゼンの製造方法。 3. The method for producing 2,4-difluoronitrobenzene according to claim 1 , wherein R 1 is a methyl group, and R 2 is a methyl group.
4. R1が、 メチル基であり、 R2力 ェチル基である請求の範囲第 1項に記 載の 2, 4—ジフルォロニトロベンゼンの製造方法。 4. The method for producing 2,4-difluoronitrobenzene according to claim 1 , wherein R 1 is a methyl group, and is an R 2 force ethyl group.
5. 反応に不活性な有機溶媒の存在下に反応を実施する請求の範囲第 3項 に記載の 2, 4—ジフルォロニトロベンゼンの製造方法。  5. The method for producing 2,4-difluoronitrobenzene according to claim 3, wherein the reaction is carried out in the presence of an organic solvent inert to the reaction.
6. 反応に不活性な有機溶媒が、 エーテル溶媒、 N, N—ジアルキルアミド 溶媒、 芳香族炭化水素溶媒および脂肪族炭化水素溶媒からなる群から選ばれる少なくとも 一つである請求の範囲第 5項に記載の 2, 4—ジフルォロニトロベンゼンの製造方法。  6. The organic solvent inert to the reaction is at least one selected from the group consisting of ether solvents, N, N-dialkylamide solvents, aromatic hydrocarbon solvents and aliphatic hydrocarbon solvents. A process for producing 2,4-difluoronitrobenzene as described in 1.
7. 反応に不活性な有機溶媒の使用量が、 式 (1) で示されるスルホン化合 物に対して、 0. 001〜0. 5重量倍である請求の範囲第 5項に記載の 2, 4—ジフル ォロニトロベンゼンの製造方法。  7. The method according to claim 5, wherein the amount of the organic solvent inert to the reaction is 0.001 to 0.5 times the weight of the sulfonate compound represented by the formula (1). 4—Method for producing difluoronitrobenzene.
PCT/JP2006/324308 2005-12-20 2006-11-29 Process for producing 2,4-difluoronitrobenzene WO2007072679A1 (en)

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JPS617217A (en) * 1984-06-20 1986-01-13 Shinakita Kasei Kk Novel method for preparating fluorinated aromatic compound
JPS63502181A (en) * 1986-01-06 1988-08-25 マリンクロッド・インコ−ポレイテッド Method for producing fluoroaromatic compounds in potassium fluoride dispersion
JPH046104A (en) * 1990-04-24 1992-01-10 Nippon Light Metal Co Ltd Production of anhydrous potassium flouride for synthesizing organic fluorine compound
JPH05286917A (en) * 1992-02-05 1993-11-02 Basf Ag Preparation of e-oxime ether of phenylglyoxylic ester
JPH06321886A (en) * 1993-04-08 1994-11-22 Basf Ag New halomethylbenzoyl cyanide and preparation thereof

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JPS617217A (en) * 1984-06-20 1986-01-13 Shinakita Kasei Kk Novel method for preparating fluorinated aromatic compound
JPS63502181A (en) * 1986-01-06 1988-08-25 マリンクロッド・インコ−ポレイテッド Method for producing fluoroaromatic compounds in potassium fluoride dispersion
JPH046104A (en) * 1990-04-24 1992-01-10 Nippon Light Metal Co Ltd Production of anhydrous potassium flouride for synthesizing organic fluorine compound
JPH05286917A (en) * 1992-02-05 1993-11-02 Basf Ag Preparation of e-oxime ether of phenylglyoxylic ester
JPH06321886A (en) * 1993-04-08 1994-11-22 Basf Ag New halomethylbenzoyl cyanide and preparation thereof

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