JPH07138247A - Production of o,o'-diacyltartaric acid anhydride - Google Patents

Production of o,o'-diacyltartaric acid anhydride

Info

Publication number
JPH07138247A
JPH07138247A JP5314563A JP31456393A JPH07138247A JP H07138247 A JPH07138247 A JP H07138247A JP 5314563 A JP5314563 A JP 5314563A JP 31456393 A JP31456393 A JP 31456393A JP H07138247 A JPH07138247 A JP H07138247A
Authority
JP
Japan
Prior art keywords
reaction
acid
chloride
tartaric acid
component
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP5314563A
Other languages
Japanese (ja)
Other versions
JP3149652B2 (en
Inventor
Toshihiro Fujino
年弘 藤野
Haruyo Satou
治代 佐藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP31456393A priority Critical patent/JP3149652B2/en
Publication of JPH07138247A publication Critical patent/JPH07138247A/en
Application granted granted Critical
Publication of JP3149652B2 publication Critical patent/JP3149652B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To produce O,O'-diacyltartaric acid anhydride in high purity and yield at a low cost by reacting a specific aromatic carboxylic acid with tartaric acid in the presence of a chlorinating agent and a catalyst. CONSTITUTION:The objective O,O'-diacyltartaric acid anhydride of formula II can be produced by reacting (A) an aromatic carboxylic acid of formula I (R<1> and R<2> are H, a halogen or a 1-3C alkyl) with (B) tartaric acid in the presence of (C) a chlorinating agent (preferably thionyl chloride) and (D) a catalyst (preferably a Lewis acid selected from ferric chloride, zinc chloride, aluminum chloride and boron trifluoride) at 40-170 deg.C (preferably 60-150 deg.C). The molar ratio of the component A to the component B is 1.8-4, preferably 2.0-2.4 and that of the component C to the component A is 1.4-3, preferably 1.5-2.0. The amount of the component D is 0.001-0.2mol, preferably 0.002-0.10mol based on 1mol of the component B.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、O,O´−ジアシル酒
石酸無水物の製造方法に関し、特に、O,O´−ジアシ
ル酒石酸無水物の工業的に有利な製造方法に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing O, O'-diacyltartaric anhydride, and more particularly to an industrially advantageous method for producing O, O'-diacyltartaric anhydride.

【0002】[0002]

【従来の技術】従来、O,O´−ジアシル酒石酸無水物
の代表例である、O,O´−ジベンゾイル酒石酸無水物
を製造する方法として、(1)酒石酸と大過剰の塩化ベ
ンゾイルとを無溶媒下に於いて反応させる方法(J.A
m.Chem.Soc.,55,2605(193
3))、(2)酒石酸と2倍モルの塩化ベンゾイルとを
溶媒存在下に反応させ、次いで塩化チオニルを加えて反
応を行う方法に於いて、反応させるに際して塩化鉄、塩
化亜鉛或いは塩化アルミニウム等の触媒を添加する方法
(HU34720)などが提案されている。
2. Description of the Related Art Conventionally, as a method for producing O, O'-dibenzoyltartaric anhydride, which is a typical example of O, O'-diacyltartaric anhydride, (1) tartaric acid and a large excess of benzoyl chloride are used. Method of reacting in a solvent (JA
m. Chem. Soc. , 55, 2605 (193
3)), (2) Tartaric acid and 2-fold molar benzoyl chloride are reacted in the presence of a solvent, and then thionyl chloride is added to carry out the reaction. In the reaction, iron chloride, zinc chloride, aluminum chloride, etc. The method of adding the catalyst of (HU34720) is proposed.

【0003】[0003]

【発明が解決しようとする課題】(1)法においては、
酒石酸と塩化ベンゾイルの混合物を加熱して反応させる
際に、反応混合物が固化する等操作性が悪く工業的な製
造法には適さない。(2)法は操作性が良好であり、ま
た(1)法より低い温度でも反応が進行し工業的には好
ましい方法である。しかしながら、高価な酸ハロゲン化
物を使用するために製造コストが高く、より安価な製造
方法の開発が望まれていた。
[Problems to be Solved by the Invention] In the method (1),
When a mixture of tartaric acid and benzoyl chloride is heated and reacted, the reaction mixture is not suitable for industrial production because the reaction mixture solidifies and the operability is poor. The method (2) has good operability, and the reaction proceeds even at a lower temperature than the method (1), which is an industrially preferable method. However, since the expensive acid halide is used, the manufacturing cost is high, and the development of a cheaper manufacturing method has been desired.

【0004】本発明の目的は、操作性が良好で工業的生
産に適し、高価な酸ハロゲン化物を用いずに安価に行う
ことができ、高収率、高純度でO,O´−ジアシル酒石
酸無水物を得ることができるO,O´−ジアシル酒石酸
無水物の製造方法を提供することである。
The object of the present invention is that the operability is good, it is suitable for industrial production, it can be carried out inexpensively without using an expensive acid halide, and high yield, high purity of O, O'-diacyltartaric acid is obtained. An object of the present invention is to provide a method for producing an O, O'-diacyltartaric acid anhydride capable of obtaining an anhydride.

【0005】[0005]

【課題を解決するための手段】本出願人は、先に、カル
ボン酸類と酒石酸とをクロル化剤の存在下で反応させる
ことによりO,O´−ジアシル酒石酸無水物を製造する
方法を発明し、特許出願した(特願平4−321019
号)。この方法は、カルボン酸をそのまま用いることが
でき(すなわち、高価な酸ハロゲン化物が不要)、操作
性が良好で、高収率、高純度でO,O´−ジアシル酒石
酸無水物を製造することができる優れた方法である。
The present applicant previously invented a method for producing an O, O'-diacyl tartaric anhydride by reacting a carboxylic acid and tartaric acid in the presence of a chlorinating agent. Filed a patent application (Japanese Patent Application No. 4-321019)
issue). In this method, a carboxylic acid can be used as it is (that is, an expensive acid halide is unnecessary), operability is good, and O, O′-diacyltartaric anhydride can be produced in high yield and high purity. It is an excellent way to

【0006】本願発明者らは、特願平4−321019
号に記載された方法のうち、芳香族カルボン酸類を出発
原料として用いる場合に、触媒を用いることによりO,
O´−ジアシル酒石酸無水物をより高収率かつ高純度に
得ることができることを見出し、本発明を完成した。
[0006] The inventors of the present application filed Japanese Patent Application No. 4-321019.
In the method described in No. 1, when an aromatic carboxylic acid is used as a starting material, a
The inventors have found that O'-diacyl tartaric anhydride can be obtained in higher yield and higher purity, and have completed the present invention.

【0007】すなわち、本発明は、下記一般式(II)That is, the present invention has the following general formula (II)

【化1】 (式中R1 、R2 は水素原子、ハロゲン原子又は炭素数
1〜3のアルキル基を示し、R1 とR2 が同一でも、異
なってもよい。)で示される芳香族カルボン酸類と酒石
酸とをクロル化剤及び触媒の存在下に反応させる下記一
般式(I)
[Chemical 1] (In the formula, R 1 and R 2 represent a hydrogen atom, a halogen atom or an alkyl group having 1 to 3 carbon atoms, and R 1 and R 2 may be the same or different.) And tartaric acid The following general formula (I) is used to react with and in the presence of a chlorinating agent and a catalyst.

【化2】 (式中R1 、R2 は一般式(II)のR1 、R2 と同じも
のであり、水素原子、ハロゲン原子又は炭素数1〜3の
アルキル基を示す。)で示されるO,O´−ジアシル酒
石酸無水物の製造方法を提供する。
[Chemical 2] (Is the same as the R 1, R 2 in the formula R 1, R 2 is the formula (II), a hydrogen atom, a halogen atom or an alkyl group having 1 to 3 carbon atoms.) O indicated by, O A method for producing ′ -diacyl tartaric anhydride is provided.

【0008】以下、本発明を詳細に説明する。The present invention will be described in detail below.

【0009】本発明の方法では、反応原料として上記式
(II) で示される芳香族カルボン酸類を用いる。芳香族
カルボン酸類の使用量は酒石酸に対して通常1.8倍モ
ル乃至4倍モル、好ましくは2.0倍モル乃至2.4倍
モルである。これより使用量が少ないと未反応の酒石酸
が製品中に混入して製品純度を低下させるので好ましく
ない。これより使用量が多いと使用薬品費用が高くなる
ので好ましくない。
In the method of the present invention, an aromatic carboxylic acid represented by the above formula (II) is used as a reaction raw material. The amount of the aromatic carboxylic acid used is usually 1.8 times to 4 times, and preferably 2.0 times to 2.4 times the mol of tartaric acid. If the amount used is less than the above range, unreacted tartaric acid is mixed in the product to lower the product purity, which is not preferable. If the amount used is larger than this, the cost of chemicals used will increase, which is not preferable.

【0010】本発明の方法においては、反応の際にクロ
ル化剤を共存させる。クロル化剤としては次のようなも
のがあげられる。例えば五塩化燐、三塩化燐、塩化チオ
ニルであり、中でも塩化チオニルが好ましい。クロル化
剤の添加量は芳香族カルボン酸類に対して通常1.4倍
モル乃至3倍モル、好ましくは1.5倍モル乃至2.0
倍モルである。
In the method of the present invention, a chlorinating agent is allowed to coexist during the reaction. Examples of the chlorinating agent include the following. Examples thereof include phosphorus pentachloride, phosphorus trichloride, and thionyl chloride, with thionyl chloride being preferred. The amount of the chlorinating agent added is usually 1.4 times to 3 times, preferably 1.5 times to 2.0 times the aromatic carboxylic acid.
It is twice the mole.

【0011】本発明の方法では反応の際に触媒を共存さ
せる。触媒としては塩化鉄、塩化アルミニウム、塩化亜
鉛、三フッ化ホウ素等のルイス酸が挙げられる。触媒の
使用量は酒石酸に対して通常0.001乃至0.2倍モ
ル、好ましくは0.002乃至0.10倍モルであり、
反応開始時に一括して添加してもよく、また反応開始時
にその一部を添加し、更に反応の途中に追加してもよ
い。
In the method of the present invention, a catalyst is allowed to coexist during the reaction. Examples of the catalyst include Lewis acids such as iron chloride, aluminum chloride, zinc chloride and boron trifluoride. The amount of the catalyst used is usually 0.001 to 0.2 times mol, preferably 0.002 to 0.10 times mol, relative to tartaric acid,
It may be added all at once at the start of the reaction, or a part thereof may be added at the start of the reaction and further added during the reaction.

【0012】本発明においては、反応に際して有機溶媒
を共存させてもさせなくてもよいが、有機溶媒を共存さ
せると、生成したO,O´−ジアシル酒石酸無水物が反
応槽内で固化すること無く、操作性良く反応を行うこと
ができるので好ましい。加える有機溶媒としては次のよ
うなものがあげられる。例えば、ヘプタン、オクタン、
ノナンのような脂肪族炭化水素化合物、ベンゼン,トル
エン、キシレンのような芳香族炭化水素化合物であり、
中でもベンゼン,トルエン、キシレンが好ましい。な
お、2種以上の溶媒を併用することも可能である。溶媒
は酒石酸に対して通常0.5乃至10倍重量、好ましく
は1乃至5倍重量の量で使用される。これより少ない
と、反応の際に生成したO,O´−ジアシル酒石酸無水
物のスラリ−濃度が高くなり、撹拌が困難になるので好
ましくない。またこれより多いと反応容積の大きい装置
が必要になり、生産性が悪くなるので好ましくない。有
機溶媒を加える時機は、反応開始時或いは反応途中のい
ずれでも良いが、好ましくは反応開始時である。
In the present invention, an organic solvent may or may not be allowed to coexist during the reaction, but when the organic solvent coexists, the produced O, O'-diacyl tartaric anhydride solidifies in the reaction tank. It is preferable because the reaction can be carried out with good operability without the use. Examples of the organic solvent to be added include the following. For example, heptane, octane,
Aliphatic hydrocarbon compounds such as nonane, aromatic hydrocarbon compounds such as benzene, toluene, xylene,
Among them, benzene, toluene and xylene are preferable. It is also possible to use two or more solvents in combination. The solvent is usually used in an amount of 0.5 to 10 times, preferably 1 to 5 times the weight of tartaric acid. If it is less than this range, the concentration of the slurry of O, O'-diacyltartaric acid anhydride produced during the reaction becomes high and stirring becomes difficult, which is not preferable. On the other hand, if the amount is larger than this, an apparatus having a large reaction volume is required and productivity is deteriorated, which is not preferable. The organic solvent may be added either at the start of the reaction or during the reaction, but it is preferably at the start of the reaction.

【0013】芳香族カルボン酸類と酒石酸とを反応させ
る場合の反応方法としては、例えば酒石酸、芳香族カル
ボン酸類および必要に応じて溶媒を加えた混合物を適当
な温度に昇温したのち塩化チオニルを徐々に加え、次い
で触媒を加えた後、更に加熱して熟成反応を行う方法、
酒石酸、芳香族カルボン酸類、触媒および必要に応じて
溶媒を加えた混合物を適当な温度に昇温したのち塩化チ
オニルを徐々に加え、更に熟成反応を行う方法がある。
また酒石酸、芳香族カルボン酸類、触媒、塩化チオニル
および必要に応じて溶媒を加えた混合物を、所定の温度
まで徐々に昇温させたのち、更に熟成反応を行う方法も
ある。触媒はこのように反応開始時に添加してもよく、
或いは反応の途中に添加してもよい。また反応開始時に
添加し、更に反応途中に追加してもよい。
As a reaction method for reacting an aromatic carboxylic acid and tartaric acid, for example, a mixture of tartaric acid, an aromatic carboxylic acid and, if necessary, a solvent is heated to an appropriate temperature and then thionyl chloride is gradually added. In addition to the above, after adding a catalyst, further heating to perform an aging reaction,
There is a method in which a mixture obtained by adding tartaric acid, aromatic carboxylic acids, a catalyst and, if necessary, a solvent is heated to an appropriate temperature, and then thionyl chloride is gradually added to carry out an aging reaction.
There is also a method in which a mixture obtained by adding tartaric acid, an aromatic carboxylic acid, a catalyst, thionyl chloride and, if necessary, a solvent is gradually heated to a predetermined temperature and then subjected to an aging reaction. The catalyst may thus be added at the beginning of the reaction,
Alternatively, it may be added during the reaction. It may be added at the start of the reaction and further added during the reaction.

【0014】本発明の方法は、一般的には40乃至17
0℃、好ましくは60乃至150℃にて行われる。反応
温度が低い場合には反応を完結させるのに長時間を要
し、また反応温度が高い場合には短時間で反応を完結さ
せることができるが同時に分解反応が起きる。すなわ
ち、反応温度が上記範囲の下限付近である場合には、反
応時間は通常20ないし50時間程度であり、上記範囲
の上限付近の場合には反応時間は通常1ないし3時間程
度であり、その間の温度の場合には、反応時間もその間
になる。
The method of the present invention is generally 40 to 17
It is carried out at 0 ° C., preferably 60 to 150 ° C. When the reaction temperature is low, it takes a long time to complete the reaction, and when the reaction temperature is high, the reaction can be completed in a short time, but at the same time, the decomposition reaction occurs. That is, when the reaction temperature is near the lower limit of the above range, the reaction time is usually about 20 to 50 hours, and when near the upper limit of the above range, the reaction time is usually about 1 to 3 hours. In case of the temperature of, the reaction time is also in the meantime.

【0015】このようにして得られた反応混合物をその
まま、或いは溶媒を添加、或いは追加した後に冷却し、
析出した結晶を濾別することによってO,O´−ジアシ
ル酒石酸無水物が取得できる。
The reaction mixture thus obtained is cooled as it is, or after adding or adding a solvent, it is cooled,
O, O'-diacyl tartaric acid anhydride can be obtained by filtering the precipitated crystals.

【0016】[0016]

【実施例】以下、実施例により本発明を説明するが、本
発明はこれらの実施例により限定されるものではない。
EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples.

【0017】実施例1 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g及び安息香酸53.7g
を入れ、内容物を90℃に加熱した。次いでその温度を
保ちながら、滴下ロ−トから塩化チオニル83.7gを
6時間かけて添加した後、更に105〜110℃で1時
間熟成して反応を行った。反応混合物を室温まで冷却
し、析出した結晶を濾別したのち乾燥して、薄黄色結晶
のO,O´−ジベンゾイル−D−酒石酸無水物61.8
gを得た。高速液体クロマトグラフィ−で分析したとこ
ろ、O,O´−ジベンゾイル−D−酒石酸無水物の純度
は100%であった。(収率90.9%)
Example 1 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 53.7 g of benzoic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel.
And the contents were heated to 90 ° C. Next, while maintaining the temperature, 83.7 g of thionyl chloride was added from a dropping funnel over 6 hours, and then the reaction was carried out by further aging at 105 to 110 ° C for 1 hour. The reaction mixture was cooled to room temperature, the precipitated crystals were separated by filtration and dried to give pale yellow crystals of O, O'-dibenzoyl-D-tartaric anhydride 61.8.
g was obtained. When analyzed by high performance liquid chromatography, the purity of O, O'-dibenzoyl-D-tartaric acid anhydride was 100%. (Yield 90.9%)

【0018】実施例2 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g及びp−トルイル酸5
9.9gを入れ、内容物を90℃に加熱した。次いで、
その温度を保ちながら、滴下ロ−トから塩化チオニル8
3.7gを6時間かけて添加した後、更に105〜11
0℃で1時間熟成して反応を行った。反応混合物を室温
まで冷却し、析出した結晶を濾別したのち乾燥して、薄
黄色結晶のO,O´−ジ−p−トルオイル−D−酒石酸
無水物67.2gを得た。(純度100%、収率91.
3%)
Example 2 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 5 p-toluic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel.
9.9g was added and the contents were heated to 90 ° C. Then
While maintaining the temperature, thionyl chloride 8 was added from the dropping funnel.
After adding 3.7 g over 6 hours, a further 105-11
The reaction was carried out by aging at 0 ° C. for 1 hour. The reaction mixture was cooled to room temperature, the precipitated crystals were separated by filtration and dried to obtain 67.2 g of light yellow crystals of O, O′-di-p-toluoyl-D-tartaric acid anhydride. (Purity 100%, yield 91.
3%)

【0019】実施例3 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g、塩化チオニル83.7
g及び安息香酸53.7gを入れ、内容物を攪拌しなが
ら3時間かけて90℃まで昇温した。更に内容物を90
℃に保ちながら4時間熟成を行い、次いで105〜11
0℃に昇温して1時間熟成を行った。反応混合物を室温
まで冷却し、析出した結晶を濾別したのち乾燥して、薄
黄色結晶のO,O´−ジベンゾイル−D−酒石酸無水物
62.3gを得た。(純度100%、収率91.6%)
Example 3 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 83.7 thionyl chloride were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel.
g and 53.7 g of benzoic acid were added, and the contents were heated to 90 ° C. over 3 hours with stirring. 90 more contents
Aging for 4 hours while maintaining at ℃, then 105 ~ 11
The temperature was raised to 0 ° C. and aging was carried out for 1 hour. The reaction mixture was cooled to room temperature, and the precipitated crystals were filtered off and dried to obtain 62.3 g of O, O'-dibenzoyl-D-tartaric anhydride as pale yellow crystals. (Purity 100%, Yield 91.6%)

【0020】実施例4 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g、塩化チオニル83.7
g及びp−トルイル酸59.9gを入れ、内容物を攪拌
しながら3時間かけて90℃まで昇温した。更に内容物
を90℃に保ちながら4時間熟成を行い、次いで105
〜110℃に昇温して1時間熟成を行った。反応混合物
を室温まで冷却し、析出した結晶を濾別したのち乾燥し
て、薄黄色結晶のO,O´−ジ−p−トルオイル−D−
酒石酸無水物67.7gを得た。(純度100%、収率
92.0%)
Example 4 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 83.7 thionyl chloride were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel.
g and p-toluic acid 59.9 g were added, and the content was heated to 90 ° C. over 3 hours while stirring. Further, the contents were aged for 4 hours while maintaining the temperature at 90 ° C., then 105
The temperature was raised to ˜110 ° C. and aging was carried out for 1 hour. The reaction mixture was cooled to room temperature, and the precipitated crystals were separated by filtration and dried to give pale yellow crystals of O, O'-di-p-toluoyl-D-.
67.7 g of tartaric anhydride was obtained. (Purity 100%, Yield 92.0%)

【0021】実施例5 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化亜鉛0.10g及び安息香酸53.7gを
入れ、内容物を90℃に加熱した。次いでその温度を保
ちながら、滴下ロ−トから塩化チオニル83.7gを6
時間かけて添加した後、更に105〜110℃で1時間
熟成して反応を行った。反応混合物を室温まで冷却し、
析出した結晶を濾別したのち乾燥して、白色結晶のO,
O´−ジベンゾイル−D−酒石酸無水物58.1gを得
た。(純度100%、収率85.4%)
Example 5 30 g of D-tartaric acid, 70 g of toluene, 0.10 g of zinc chloride and 53.7 g of benzoic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel, and the contents were heated to 90 ° C. Heated to. Then, while maintaining the temperature, 63.7 g of thionyl chloride was added from the dropping funnel.
After the addition over a period of time, the reaction was carried out by further aging at 105 to 110 ° C. for 1 hour. The reaction mixture is cooled to room temperature,
The precipitated crystals are separated by filtration and dried to give white crystals of O,
58.1 g of O'-dibenzoyl-D-tartaric anhydride was obtained. (Purity 100%, Yield 85.4%)

【0022】実施例6 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、三フッ化ホウ素を46%含有するジエチルエー
テル溶液1.4g及び安息香酸53.7gを入れ、内容
物を90℃に加熱した。次いでその温度を保ちながら、
滴下ロ−トから塩化チオニル83.7gを6時間かけて
添加した後、更に105〜110℃で1時間熟成して反
応を行った。反応混合物を室温まで冷却し、析出した結
晶を濾別したのち乾燥して、白色結晶のO,O´−ジベ
ンゾイル−D−酒石酸無水物62.0gを得た。(純度
100%、収率91.2%)
Example 6 In a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel, 30 g of D-tartaric acid, 70 g of toluene, 1.4 g of a diethyl ether solution containing 46% of boron trifluoride and 53 of benzoic acid. 0.7 g was added and the contents were heated to 90 ° C. Then while maintaining that temperature,
After adding 83.7 g of thionyl chloride from the dropping funnel over 6 hours, the reaction was carried out by further aging at 105 to 110 ° C. for 1 hour. The reaction mixture was cooled to room temperature, the precipitated crystals were filtered off and dried to obtain 62.0 g of white crystals of O, O'-dibenzoyl-D-tartaric acid anhydride. (Purity 100%, Yield 91.2%)

【0023】実施例7 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g及び3,4−ジメチル安
息香酸66.0gを入れ、内容物を90℃に加熱した。
次いでその温度を保ちながら、滴下ロ−トから塩化チオ
ニル83.7gを6時間かけて添加した後、更に105
〜110℃で1時間熟成して反応を行った。反応混合物
を室温まで冷却し、析出した結晶を濾別したのち乾燥し
て、薄黄色結晶のO,O´−ジ−(3,4−ジメチルベ
ンゾイル)−D−酒石酸無水物71.4gを得た。(純
度100%、収率90.1%)
Example 7 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 66.0 g of 3,4-dimethylbenzoic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel. Then, the contents were heated to 90 ° C.
Then, while maintaining the temperature, 83.7 g of thionyl chloride was added from the dropping funnel over 6 hours, and then a further 105
The reaction was carried out by aging at ˜110 ° C. for 1 hour. The reaction mixture was cooled to room temperature, and the precipitated crystals were separated by filtration and dried to obtain 71.4 g of light yellow crystals of O, O'-di- (3,4-dimethylbenzoyl) -D-tartaric acid anhydride. It was (Purity 100%, Yield 90.1%)

【0024】実施例8 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化第二鉄0.12g及び2−クロロ安息香酸
68.8gを入れ、内容物を90℃に加熱した。次いで
その温度を保ちながら、滴下ロ−トから塩化チオニル8
3.7gを6時間かけて添加した後、更に105〜11
0℃で1時間熟成して反応を行った。反応混合物を室温
まで冷却し、析出した結晶を濾別したのち乾燥して、薄
黄色結晶のO,O´−ジ(2−クロロベンゾイル)−D
−酒石酸無水物74.3gを得た。(純度100%、収
率90.8%)
Example 8 30 g of D-tartaric acid, 70 g of toluene, 0.12 g of ferric chloride and 68.8 g of 2-chlorobenzoic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel, The contents were heated to 90 ° C. Then, while maintaining that temperature, thionyl chloride 8 was added from the dropping funnel.
After adding 3.7 g over 6 hours, a further 105-11
The reaction was carried out by aging at 0 ° C. for 1 hour. The reaction mixture was cooled to room temperature, the precipitated crystals were filtered off and dried to give pale yellow crystals of O, O'-di (2-chlorobenzoyl) -D.
74.3 g of tartaric anhydride were obtained. (Purity 100%, Yield 90.8%)

【0025】実施例9 攪拌機、温度計、コンデンサーおよび滴下ロートを装着
した300mlの反応器にD−酒石酸30g、トルエン
70g、塩化アルミニウム0.10g及び安息香酸5
3.7gを入れ、内容物を90℃に加熱した。次いでそ
の温度を保ちながら、滴下ロ−トから塩化チオニル8
3.7gを6時間かけて添加した後、更に105〜11
0℃で1時間熟成して反応を行った。反応混合物を室温
まで冷却し、析出した結晶を濾別したのち乾燥して、白
色結晶のO,O´−ジベンゾイル−D−酒石酸無水物5
8.9gを得た。(純度100%、収率86.6%)
Example 9 30 g of D-tartaric acid, 70 g of toluene, 0.10 g of aluminum chloride and 5 parts of benzoic acid were placed in a 300 ml reactor equipped with a stirrer, a thermometer, a condenser and a dropping funnel.
3.7 g was added and the contents were heated to 90 ° C. Then, while maintaining that temperature, thionyl chloride 8 was added from the dropping funnel.
After adding 3.7 g over 6 hours, a further 105-11
The reaction was carried out by aging at 0 ° C. for 1 hour. The reaction mixture was cooled to room temperature, and the precipitated crystals were filtered off and dried to give white crystals of O, O′-dibenzoyl-D-tartaric acid anhydride 5
8.9 g was obtained. (Purity 100%, Yield 86.6%)

【0026】[0026]

【発明の効果】本発明により、安価、高収率、高純度に
O,O´−ジアシル酒石酸無水物を製造することができ
る方法が提供された。
Industrial Applicability According to the present invention, there has been provided a method capable of producing O, O'-diacyl tartaric acid anhydride at low cost, high yield and high purity.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 下記一般式(II) 【化1】 (式中R1 、R2 は水素原子、ハロゲン原子又は炭素数
1〜3のアルキル基を示し、R1 とR2 が同一でも、異
なってもよい。)で示される芳香族カルボン酸類と酒石
酸とをクロル化剤及び触媒の存在下に反応させる下記一
般式(I) 【化2】 (式中R1 、R2 は一般式(II)のR1 、R2 と同じも
のであり、水素原子、ハロゲン原子又は炭素数1〜3の
アルキル基を示す。)で示されるO,O´−ジアシル酒
石酸無水物の製造方法。
1. The following general formula (II): (In the formula, R 1 and R 2 represent a hydrogen atom, a halogen atom or an alkyl group having 1 to 3 carbon atoms, and R 1 and R 2 may be the same or different.) And tartaric acid To react with chlorinating agent and catalyst in the following general formula (I) (Is the same as the R 1, R 2 in the formula R 1, R 2 is the formula (II), a hydrogen atom, a halogen atom or an alkyl group having 1 to 3 carbon atoms.) O indicated by, O A method for producing ′ -diacyl tartaric anhydride.
【請求項2】 前記クロル化剤が塩化チオニルである請
求項1記載の製造方法。
2. The method according to claim 1, wherein the chlorinating agent is thionyl chloride.
【請求項3】 前記触媒がルイス酸である請求項1又は
2記載の製造方法。
3. The production method according to claim 1, wherein the catalyst is a Lewis acid.
【請求項4】 前記ルイス酸が塩化第二鉄、塩化亜鉛、
塩化アルミニウム又は三フッ化ホウ素である請求項3記
載の製造方法。
4. The Lewis acid is ferric chloride, zinc chloride,
The manufacturing method according to claim 3, which is aluminum chloride or boron trifluoride.
JP31456393A 1993-11-19 1993-11-19 Process for producing O, O'-diacyltartaric anhydride Expired - Fee Related JP3149652B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31456393A JP3149652B2 (en) 1993-11-19 1993-11-19 Process for producing O, O'-diacyltartaric anhydride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31456393A JP3149652B2 (en) 1993-11-19 1993-11-19 Process for producing O, O'-diacyltartaric anhydride

Publications (2)

Publication Number Publication Date
JPH07138247A true JPH07138247A (en) 1995-05-30
JP3149652B2 JP3149652B2 (en) 2001-03-26

Family

ID=18054793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31456393A Expired - Fee Related JP3149652B2 (en) 1993-11-19 1993-11-19 Process for producing O, O'-diacyltartaric anhydride

Country Status (1)

Country Link
JP (1) JP3149652B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004262846A (en) * 2003-03-03 2004-09-24 New Japan Chem Co Ltd Method for producing 4-chloroformyl-cyclohexane-1,2-dicarboxylic anhydride

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004262846A (en) * 2003-03-03 2004-09-24 New Japan Chem Co Ltd Method for producing 4-chloroformyl-cyclohexane-1,2-dicarboxylic anhydride

Also Published As

Publication number Publication date
JP3149652B2 (en) 2001-03-26

Similar Documents

Publication Publication Date Title
US4379766A (en) Silyl esters of carboxylic acids by phase transfer catalysts
EP0006999B1 (en) A process for the production of 2-chlorobenzonitrile derivatives
JP3149652B2 (en) Process for producing O, O&#39;-diacyltartaric anhydride
US3953531A (en) Alkylhydroquinone and process for producing the same
JP4913962B2 (en) Process for producing phenylethynylphthalic anhydride derivative
JP3149651B2 (en) Process for producing O, O&#39;-diacyltartaric anhydride
JPH0616656A (en) Production of fluorinated phthalic acid anhydride
KR940000060B1 (en) Process of synthesis of acylcyanamides
US5451687A (en) Process for producing O,O&#39;-diacyltartaric anhydride and process for producing O,O&#39;-diacyltartaric acid
EP0953564B1 (en) Process for preparing 2-cyanobiphenyl compound
JP3379979B2 (en) Method for producing 2- (2,4-dihydroxyphenyl) -2- (4-hydroxyphenyl) propane
JP3640319B2 (en) Method for producing benzamide derivative
GB1561464A (en) Oxidation of alkaryl compounds
JPH04273887A (en) Preparation of monohaloalkanoylferrocene
US4297301A (en) Process for the manufacture of organic acid chlorides
JP3876933B2 (en) Method for producing hydrogen sulfate ester
JPH0665260A (en) Production of sodium bistrimethylsilylamide
JP3849837B2 (en) Synthesis method of dimethyltin dichloride
JP4571740B2 (en) Method for producing 1,6-dicyanohexane
JP2773627B2 (en) Process for producing O, O&#39;-diacyltartaric anhydride
JP2861122B2 (en) Method for producing pyrazolecarboxylic acid esters
JP2540167B2 (en) Method for producing maleimide
JPH10291964A (en) Production of diphenyl phthalate
JPS61171476A (en) Novel phenothiazine derivative
JPH06219998A (en) Production of fluorinated organic quaternary ammonium salt

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090119

Year of fee payment: 8

LAPS Cancellation because of no payment of annual fees