JP2013028559A5 - - Google Patents

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JP2013028559A5
JP2013028559A5 JP2011165361A JP2011165361A JP2013028559A5 JP 2013028559 A5 JP2013028559 A5 JP 2013028559A5 JP 2011165361 A JP2011165361 A JP 2011165361A JP 2011165361 A JP2011165361 A JP 2011165361A JP 2013028559 A5 JP2013028559 A5 JP 2013028559A5
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chloro
methylbenzoic acid
reaction
isopropyl
represented
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Priority to JP2011165361A priority Critical patent/JP2013028559A/en
Priority claimed from JP2011165361A external-priority patent/JP2013028559A/en
Priority to TW101124026A priority patent/TW201305104A/en
Priority to PCT/JP2012/068409 priority patent/WO2013015203A1/en
Priority to CN201280036985.2A priority patent/CN103917515A/en
Publication of JP2013028559A publication Critical patent/JP2013028559A/en
Publication of JP2013028559A5 publication Critical patent/JP2013028559A5/ja
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すなわち、本発明は、下記式(2)で表わされる3-クロロ-4-メチル安息香酸クロライドイソプロピルアルコールを反応させ、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを製造するに際し、
前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライドの0.9〜1.2倍モルの割合で使用し、また、
前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライド中に無溶媒及び反応温度60〜140℃の条件下に撹拌しながら滴下して反応させ、
得られた反応生成物を分離精製し、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを得ることを特徴とする3-クロロ-4-メチル安息香酸イソプロピルの製造方法である。
That is, the present invention may be prepared by reacting isopropyl alcohol 3-chloro-4-methylbenzoic acid chloride represented by the following formula (2), 3-chloro-4-methylbenzoic acid isopropyl represented by the following formula (1) In manufacturing,
The isopropyl alcohol is used in a proportion of 0.9 to 1.2 moles of the 3-chloro-4-methylbenzoic acid chloride, and
The isopropyl alcohol is reacted dropwise with stirring in the 3-chloro-4-methylbenzoic acid chloride under conditions of no solvent and a reaction temperature of 60 to 140 ° C. ,
The reaction product obtained was separated and purified production method of the following formula (1) to give the represented 3-chloro-4-methylbenzoic acid isopropyl in characterized Rukoto 3-chloro-4-methylbenzoic acid isopropyl It is.

Figure 2013028559
Figure 2013028559
Figure 2013028559
Figure 2013028559

また、本発明は、下記式(3)で表わされる4-メチル安息香酸クロライドを塩素及びルイス酸触媒の存在下に核塩素化し、得られた前記式(2)で表わされる3-クロロ-4-メチル安息香酸クロライドイソプロピルアルコールを反応させ、前記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを製造するに際し、
前記核塩素化反応においては、ルイス酸触媒として塩化第二鉄を0.1〜1.0重量%の割合で使用すると共に、無溶媒及び塩素導入量0.5倍モル以上の条件下に反応させ、また、
反応終点の塩素化度を0.88〜0.91の範囲に制御すると共に、反応終了後には反応容器内を速やかに窒素置換し、更に、
前記エステル化反応においては、前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライドの0.9〜1.2倍モルの割合で使用すると共に、前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライド中に無溶媒及び反応温度60〜140℃の条件下に撹拌しながら滴下して反応させ、
次いで得られた反応生成物を分離精製し、前記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを得ることを特徴とする3-クロロ-4-メチル安息香酸イソプロピルの製造方法である。
In addition , the present invention provides 4-chlorobenzoic acid chloride represented by the above formula (2) obtained by nucleating 4-methylbenzoic acid chloride represented by the following formula (3) in the presence of chlorine and a Lewis acid catalyst. - upon reacted with isopropyl alcohol methylbenzoic acid chloride, to produce a 3-chloro-4-methylbenzoic acid isopropyl represented by the formula (1),
In the nuclear chlorination reaction, ferric chloride is used as a Lewis acid catalyst in a proportion of 0.1 to 1.0% by weight, and the reaction is carried out under conditions of no solvent and a chlorine introduction amount of 0.5 times mol or more. And also
The degree of chlorination at the end of the reaction is controlled to be in the range of 0.88 to 0.91, and the reaction vessel is immediately purged with nitrogen after the completion of the reaction.
In the esterification reaction, as well as using the isopropyl alcohol at a ratio of 0.9 to 1.2 times the mole of the 3-chloro-4-methylbenzoic acid chloride, the 3-chloro-4-said isopropyl alcohol In methylbenzoic acid chloride, the reaction was conducted dropwise with stirring under conditions of no solvent and a reaction temperature of 60 to 140 ° C.
The reaction product obtained was separated and purified preparation of the formula (1) to give the represented 3-chloro-4-methylbenzoic acid isopropyl in characterized Rukoto 3-chloro-4-methylbenzoic acid isopropyl Is the method.

Claims (2)

下記式(2)で表わされる3-クロロ-4-メチル安息香酸クロライドイソプロピルアルコールを反応させ、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを製造するに際し、
前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライドの0.9〜1.2倍モルの割合で使用し、また、
前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライド中に無溶媒及び反応温度60〜140℃の条件下に撹拌しながら滴下して反応させ、
得られた反応生成物を分離精製し、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを得ることを特徴とする3-クロロ-4-メチル安息香酸イソプロピルの製造方法。
Figure 2013028559
Figure 2013028559
3-chloro-4-methylbenzoic acid chloride represented by the following formula (2) is reacted with isopropyl alcohol, when the production of 3-chloro-4-methylbenzoic acid isopropyl represented by the following formula (1),
The isopropyl alcohol is used in a proportion of 0.9 to 1.2 moles of the 3-chloro-4-methylbenzoic acid chloride, and
The isopropyl alcohol is reacted dropwise with stirring in the 3-chloro-4-methylbenzoic acid chloride under conditions of no solvent and a reaction temperature of 60 to 140 ° C. ,
The reaction product obtained was separated and purified production method of the following formula (1) to give the represented 3-chloro-4-methylbenzoic acid isopropyl in characterized Rukoto 3-chloro-4-methylbenzoic acid isopropyl .
Figure 2013028559
Figure 2013028559
下記式(3)で表わされる4-メチル安息香酸クロライドを塩素及びルイス酸触媒の存在下に核塩素化し、得られた下記式(2)で表わされる3-クロロ-4-メチル安息香酸クロライドイソプロピルアルコールを反応させ、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを製造するに際し、
前記核塩素化反応においては、ルイス酸触媒として塩化第二鉄を0.1〜1.0重量%の割合で使用すると共に、無溶媒及び塩素導入量0.5倍モル以上の条件下に反応させ、また、
反応終点の塩素化度を0.88〜0.91の範囲に制御すると共に、反応終了後には反応容器内を速やかに窒素置換し、更に、
前記エステル化反応においては、前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライドの0.9〜1.2倍モルの割合で使用すると共に、前記イソプロピルアルコールを前記3-クロロ-4-メチル安息香酸クロライド中に無溶媒及び反応温度60〜140℃の条件下に撹拌しながら滴下して反応させ、
次いで得られた反応生成物を分離精製し、下記式(1)で表わされる3-クロロ-4-メチル安息香酸イソプロピルを得ることを特徴とする3-クロロ-4-メチル安息香酸イソプロピルの製造方法。
Figure 2013028559
Figure 2013028559
Figure 2013028559
Formula 4-methyl-benzoic acid chloride of the formula (3) and Kakushio hydride in the presence of chlorine and Lewis acid catalysts, the 3-chloro-4-methylbenzoic acid chloride represented by the obtained formula (2) In producing isopropyl 3-chloro-4-methylbenzoate represented by the following formula (1) by reacting with isopropyl alcohol ,
In the nuclear chlorination reaction, ferric chloride is used as a Lewis acid catalyst in a proportion of 0.1 to 1.0% by weight, and the reaction is carried out under conditions of no solvent and a chlorine introduction amount of 0.5 times mol or more. And also
The degree of chlorination at the end of the reaction is controlled to be in the range of 0.88 to 0.91, and the reaction vessel is immediately purged with nitrogen after the completion of the reaction.
In the esterification reaction, as well as using the isopropyl alcohol at a ratio of 0.9 to 1.2 times the mole of the 3-chloro-4-methylbenzoic acid chloride, the 3-chloro-4-said isopropyl alcohol In methylbenzoic acid chloride, the reaction was conducted dropwise with stirring under conditions of no solvent and a reaction temperature of 60 to 140 ° C.
The reaction product obtained was separated and purified preparation of represented by 3-chloro-4-methylbenzoic acid to give the isopropyl characterized Rukoto 3-chloro-4-methylbenzoic acid isopropyl by the following formula (1) Method.
Figure 2013028559
Figure 2013028559
Figure 2013028559
JP2011165361A 2011-07-28 2011-07-28 Isopropyl 3-chloro-4-methylbenzoate and method for producing the same Pending JP2013028559A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP2011165361A JP2013028559A (en) 2011-07-28 2011-07-28 Isopropyl 3-chloro-4-methylbenzoate and method for producing the same
TW101124026A TW201305104A (en) 2011-07-28 2012-07-04 Isopropyl 3-chloro-4-methylbenzoate and method for producing same
PCT/JP2012/068409 WO2013015203A1 (en) 2011-07-28 2012-07-20 Isopropyl 3-chloro-4-methylbenzoate and method for producing same
CN201280036985.2A CN103917515A (en) 2011-07-28 2012-07-20 Isopropyl 3-chloro-4-methylbenzoate and method for producing same

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JP2011165361A JP2013028559A (en) 2011-07-28 2011-07-28 Isopropyl 3-chloro-4-methylbenzoate and method for producing the same

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JP2013028559A5 true JP2013028559A5 (en) 2014-09-04

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GB8400254D0 (en) * 1984-01-06 1984-02-08 Searle & Co Substituted alklidene imidazoles
JP2527961B2 (en) * 1987-04-24 1996-08-28 日本農薬株式会社 Benzoic acid ester derivative and method for producing the same
DE4339208A1 (en) * 1993-11-17 1995-05-18 Hoechst Ag Process for the preparation of alkyl fluorobenzoates in high purity and yield
JPH07330663A (en) * 1994-06-08 1995-12-19 Nippon Light Metal Co Ltd Production of 2-chloroterephthaloyl chloride
EP0995742A4 (en) * 1997-06-27 2004-08-25 Fujisawa Pharmaceutical Co Sulfonamide compounds and medicinal use thereof
WO1999016743A1 (en) * 1997-09-30 1999-04-08 Korea Research Institute Of Chemical Technology A PROCESS FOR PREPARING o-(CARBOALKOXY) PHENYLMETHANESULFONYL CHLORIDE DERIVATIVES
ITMI20020974A1 (en) * 2002-05-09 2003-11-10 Miteni Spa PROCEDURE FOR THE PREPARATION OF 4-FLUORO-ANTRANILIC ACID
WO2004014370A2 (en) * 2002-08-09 2004-02-19 Astrazeneca Ab Oxadiazoles as modulators of metabotropic glutamate receptor-5
CN1762970A (en) * 2005-09-13 2006-04-26 上海大学 Carboxylate synthesis method
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