JP2002088014A - Method for producing carbocyclic aromatic carboxylic acids - Google Patents

Method for producing carbocyclic aromatic carboxylic acids

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Publication number
JP2002088014A
JP2002088014A JP2000281413A JP2000281413A JP2002088014A JP 2002088014 A JP2002088014 A JP 2002088014A JP 2000281413 A JP2000281413 A JP 2000281413A JP 2000281413 A JP2000281413 A JP 2000281413A JP 2002088014 A JP2002088014 A JP 2002088014A
Authority
JP
Japan
Prior art keywords
carbocyclic aromatic
reaction
aromatic carboxylic
carboxylic acid
alkali metal
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
JP2000281413A
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Japanese (ja)
Other versions
JP3655540B2 (en
Inventor
Ryoichi Fujibayashi
良一 藤林
Fumio Konuma
文夫 小沼
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.)
Air Water Inc
Original Assignee
Sumikin Chemical Co Ltd
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Priority to JP2000281413A priority Critical patent/JP3655540B2/en
Publication of JP2002088014A publication Critical patent/JP2002088014A/en
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Publication of JP3655540B2 publication Critical patent/JP3655540B2/en
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Abstract

PROBLEM TO BE SOLVED: To obtain a carbocyclic aromatic carboxylic acid by safely carrying out a reaction under an industrially advantageous and mild reaction condition in a high purity in a high yield. SOLUTION: A carbocyclic aromatic aldehyde is heated in a nonpolar organic solvent in the presence of an alkali metal hydroxide. Consequently, the reaction can be safely carried out under an industrially advantageous and mild condition without requiring an expensive oxidizing agent and using a specific reactor and a carbocyclic aromatic carboxylic acid can be obtained in a high purity in a high yield.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、医薬品、農薬、
液晶化合物等の合成中間体として有用な炭素環式芳香族
カルボン酸類の製造方法に関する。
TECHNICAL FIELD The present invention relates to pharmaceuticals, agricultural chemicals,
The present invention relates to a method for producing a carbocyclic aromatic carboxylic acid useful as a synthetic intermediate such as a liquid crystal compound.

【0002】[0002]

【従来の技術】炭素環式芳香族カルボン酸類は、従来、
対応する芳香族アルデヒドの過マンガン酸酸化、クロム
酸酸化などによって製造されていたが、それぞれ多量の
副生物が生成するばかりでなく、触媒による環境汚染等
の問題があり、これらに代わるいくつかの反応が提案さ
れている。
BACKGROUND OF THE INVENTION Carbocyclic aromatic carboxylic acids have hitherto been
The corresponding aromatic aldehydes were produced by permanganate oxidation, chromic acid oxidation, etc., but each produced not only a large amount of by-products, but also had problems such as environmental pollution by catalysts. A reaction has been proposed.

【0003】例えば、クミンアルデヒドを水酸化ナトリ
ウム、水酸化カリウムなどの無機アルカリ塩を用いるア
ルカリ性条件下で過酸化水素によって酸化してクミン酸
を得る方法(特開昭63−264551号公報)、飽和
もしくは不飽和の脂環式または芳香族のアルデヒド類を
ジメチルホルムアミド、γ−ピコリン等の塩基性有機溶
媒中で過酢酸、過安息香酸等の有機過酸で酸化処理し、
対応するカルボン酸類に誘導するカルボン酸類の合成方
法(特開平3−157345号公報)、水非混和性有機
溶媒中で対応する芳香族アルデヒド類を有機過酸で酸化
処理するに際して、該酸化を有機酸のアルカリ金属塩類
の存在下に行う方法(特開平7−2729号公報)が提
案されている。
For example, a method of oxidizing cumin aldehyde with hydrogen peroxide under alkaline conditions using an inorganic alkali salt such as sodium hydroxide or potassium hydroxide to obtain cumic acid (JP-A-63-264551), Or oxidizing unsaturated alicyclic or aromatic aldehydes with an organic peracid such as peracetic acid or perbenzoic acid in a basic organic solvent such as dimethylformamide or γ-picoline,
A method for synthesizing a carboxylic acid derived into a corresponding carboxylic acid (JP-A-3-157345). When oxidizing a corresponding aromatic aldehyde with an organic peracid in a water-immiscible organic solvent, the oxidation is carried out with an organic compound. A method (JP-A-7-2729) has been proposed in which the reaction is carried out in the presence of an alkali metal salt of an acid.

【0004】また、水酸化カリウムおよび水酸化ナトリ
ウムを180℃で混合溶融した中にバニリンを添加し、
バニリン酸を合成する方法(ORGANIC SYNT
HESES COLLECTIVE VOLUME
4,P974)も知られている。
[0004] Further, vanillin is added to potassium hydroxide and sodium hydroxide mixed and melted at 180 ° C,
Method for synthesizing vanillic acid (ORGANIC SYNT)
HESES COLLECTION VOLUME
4, P974) are also known.

【0005】[0005]

【発明が解決しようとする課題】上記特開昭63−26
4551号公報に開示の方法は、過酸化水素と無機アル
カリ塩を用いる反応の危険性が高く、工業的な製造方法
とは言い難い。また、特開平3−157345号公報、
特開平7−2729号公報に開示の方法は、酸化反応に
使用する過酢酸、過安息香酸等の有機過酸自体が高価で
あり、また、安全性の面からも必ずしも取扱い易いもの
ではなく、工業的に優れた方法とは言えない。
Problems to be Solved by the Invention
The method disclosed in Japanese Patent No. 4551 has a high risk of a reaction using hydrogen peroxide and an inorganic alkali salt, and cannot be said to be an industrial production method. Also, JP-A-3-157345,
In the method disclosed in JP-A-7-2729, organic peracids such as peracetic acid and perbenzoic acid used for the oxidation reaction are expensive, and are not always easy to handle from the viewpoint of safety. It is not an industrially superior method.

【0006】ORGANIC SYNTHESES C
OLLECTIVE VOLUME4,P974に開示
のアルカリ金属溶融状態でカルボン酸を合成する方法
は、原料、副原料コストの面で有利ではあるが、反応温
度が180〜190℃と苛酷で、汎用装置では対応でき
ない。また、反応の制御も難しく、工業的に優位な方法
とは言えない。
[0006] ORGANIC SYNTHESES C
The method of synthesizing a carboxylic acid in a molten state of an alkali metal disclosed in OLECTIVE VOLUME 4, P974 is advantageous in terms of raw material and auxiliary raw material costs, but the reaction temperature is as severe as 180 to 190 ° C, and cannot be used with a general-purpose device. Also, the control of the reaction is difficult, and it cannot be said to be an industrially superior method.

【0007】本発明の目的は、上記従来技術の課題を解
消し、工業的に有利な温和な反応条件で安全に反応を行
うことができ、かつ、高純度、高収率で炭素環式芳香族
カルボン酸が得られる炭素環式芳香族カルボン酸の製造
方法を提供することにある。
An object of the present invention is to solve the above-mentioned problems of the prior art, to carry out the reaction safely under mild reaction conditions which are industrially advantageous, and to obtain a carbocyclic aromatic compound with high purity and high yield. Disclosed is a method for producing a carbocyclic aromatic carboxylic acid from which an aromatic carboxylic acid can be obtained.

【0008】[0008]

【課題を解決するための手段】本発明の炭素環式芳香族
カルボン酸の製造方法は、炭素環式芳香族アルデヒド類
を酸化して対応するカルボン酸を製造する方法におい
て、炭素環式芳香族アルデヒド類を非極性有機溶媒中、
アルカリ金属水酸化物の存在下加熱することを特徴とす
る。このように、炭素環式芳香族アルデヒド類を非極性
有機溶媒中、アルカリ金属水酸化物の存在下加熱するこ
とによって、温和な反応条件で、安全に反応を行うこと
ができると共に、高純度、高収率で炭素環式芳香族カル
ボン酸を得ることができる。
The process for producing a carbocyclic aromatic carboxylic acid according to the present invention comprises a method for producing a corresponding carboxylic acid by oxidizing a carbocyclic aromatic aldehyde. Aldehydes in a non-polar organic solvent,
It is characterized by heating in the presence of an alkali metal hydroxide. Thus, by heating a carbocyclic aromatic aldehyde in a non-polar organic solvent in the presence of an alkali metal hydroxide, the reaction can be carried out safely under mild reaction conditions, and high purity, Carbocyclic aromatic carboxylic acids can be obtained in high yield.

【0009】[0009]

【発明の実施の形態】本発明において原料として使用す
る炭素環式芳香族アルデヒド類は、市場で容易に入手す
ることができるもの、または、例えば塩化ベンジルのソ
ムレー(Sommelet)反応等、常法により容易に
合成できるもので、分子内に少なくとも1つ以上のアル
デヒド基を有するものである。
BEST MODE FOR CARRYING OUT THE INVENTION The carbocyclic aromatic aldehyde used as a raw material in the present invention can be easily obtained on the market, or can be obtained by a conventional method such as the Sommelet reaction of benzyl chloride. It can be easily synthesized and has at least one aldehyde group in the molecule.

【0010】本発明において用いる原料の炭素環式芳香
族アルデヒド類には、置換基が導入されていてもよい。
置換基としては、アルキル基、アルコキシ基、水酸基、
ハロゲン等が挙げられる。アルキル基としては、炭素数
が1〜5の低級アルキル基で、メチル基、エチル基、プ
ロピル基、イソプロピル基等が好ましい。アルコキシ基
としては、炭素数が1〜5の低級アルコキシ基で、メト
キシ基、エトキシ基、プロポキシ基が好ましい。水酸基
は、アセチル基等でエステル化されていてもよい。本発
明において用いる原料の炭素環式芳香族アルデヒド類に
は、上記置換基が2つ以上導入されていてもかまわな
い。
A substituent may be introduced into the carbocyclic aromatic aldehyde as a raw material used in the present invention.
As the substituent, an alkyl group, an alkoxy group, a hydroxyl group,
Halogen and the like. The alkyl group is a lower alkyl group having 1 to 5 carbon atoms, and is preferably a methyl group, an ethyl group, a propyl group, an isopropyl group, or the like. The alkoxy group is a lower alkoxy group having 1 to 5 carbon atoms, and is preferably a methoxy group, an ethoxy group, or a propoxy group. The hydroxyl group may be esterified with an acetyl group or the like. Two or more of the above substituents may be introduced into the carbocyclic aromatic aldehyde as the raw material used in the present invention.

【0011】本発明において原料の炭素環式芳香族アル
デヒド類としては、クミンアルデヒド、ベンズアルデヒ
ド、トルアルデヒド、クロロベンズアルデヒド、ナフト
アルデヒド、ヒドロキシベンズアルデヒド、サルチルア
ルデヒド、アントラセンアルデヒド等が挙げられる。
In the present invention, examples of the carbocyclic aromatic aldehyde as a raw material include cuminaldehyde, benzaldehyde, tolualdehyde, chlorobenzaldehyde, naphthaldehyde, hydroxybenzaldehyde, saltyl aldehyde, anthracene aldehyde and the like.

【0012】本発明において使用する非極性有機溶媒と
しては、例えば、ベンゼン、トルエン、キシレン、メチ
ルナフタレン、メチルビフェニル等の芳香族炭化水素、
シクロヘキサン、シクロペンタン等の脂環式炭化水素、
ペンタン、ヘプタン等の脂肪族炭化水素、クロルベンゼ
ン、ジクロロベンゼン等のハロゲン化炭化水素、ジイソ
プロピルエーテル、メチルフェニルエーテル等のエーテ
ル類等を挙げることができる。
The non-polar organic solvent used in the present invention includes, for example, aromatic hydrocarbons such as benzene, toluene, xylene, methylnaphthalene and methylbiphenyl;
Alicyclic hydrocarbons such as cyclohexane and cyclopentane,
Examples thereof include aliphatic hydrocarbons such as pentane and heptane, halogenated hydrocarbons such as chlorobenzene and dichlorobenzene, and ethers such as diisopropyl ether and methylphenyl ether.

【0013】非極性有機溶媒の使用量は、任意に選択で
き特に制限されないが、通常、芳香族アルデヒド類1重
量部に対して約2〜20重量部の範囲が好ましい。
The amount of the nonpolar organic solvent to be used can be arbitrarily selected and is not particularly limited, but is usually preferably in the range of about 2 to 20 parts by weight per 1 part by weight of the aromatic aldehyde.

【0014】本発明で使用するアルカリ金属水酸化物と
しては、水酸化ナトリウム、水酸化カリウム、水酸化リ
チウム、水酸化セシウム、水酸化ルビジウム等を単独あ
るいは混合して使用できるが、安価で工業的に入手が容
易な水酸化ナトリウム、水酸化カリウムが好ましい。よ
り好ましくは、反応温度を低くできる水酸化カリウムで
ある。
As the alkali metal hydroxide used in the present invention, sodium hydroxide, potassium hydroxide, lithium hydroxide, cesium hydroxide, rubidium hydroxide and the like can be used alone or as a mixture. Sodium hydroxide and potassium hydroxide which are easily available are preferred. More preferably, potassium hydroxide can lower the reaction temperature.

【0015】アルカリ金属水酸化物の使用量は、原料で
ある炭素環式芳香族アルデヒドに対して2〜10倍モ
ル、好ましくは3〜7倍モルである。アルカリ金属水酸
化物の使用量は、炭素環式芳香族アルデヒドに対して2
倍モル未満では反応が完結せず、10倍モルを超えると
操作面で不具合となり、且つ、経済的でない。
The amount of the alkali metal hydroxide used is 2 to 10 moles, preferably 3 to 7 moles, per mole of the carbocyclic aromatic aldehyde as the raw material. The amount of the alkali metal hydroxide used is 2 per carbocyclic aromatic aldehyde.
If the molar ratio is less than twice, the reaction is not completed. If the molar ratio exceeds 10 times, the operation becomes inconvenient and it is not economical.

【0016】使用するアルカリ金属水酸化物の形状は、
特に制限されないが、分散状態を良好に保つため、予め
粉砕するか、溶媒中ディスパーサ等で粉砕して使用する
こともできる。
The form of the alkali metal hydroxide used is
Although not particularly limited, in order to maintain a good dispersion state, it may be used by pulverizing in advance or pulverizing with a disperser or the like in a solvent.

【0017】反応温度は、特に指定されないが、アルカ
リ金属水酸化物が溶融する温度は必要でなく、40〜1
80℃で反応可能で、好ましくは60〜120℃であ
る。
The reaction temperature is not particularly specified, but the temperature at which the alkali metal hydroxide melts is not required.
The reaction can be performed at 80 ° C, preferably 60 to 120 ° C.

【0018】原料である炭素環式芳香族アルデヒド類の
仕込み方法は、最初に一括して仕込んでも反応には全く
支障はないが、反応が速やかに起こるために時間当たり
の発熱量が大きくなり、反応液の温度が急激に上昇する
恐れがある。したがって、反応温度を制御するために
は、非極性有機溶媒とアルカリ金属水酸化物を反応容器
に仕込み、所定温度に加熱したのち、原料の炭素環式芳
香族アルデヒド類を逐次装入することが望ましい。この
際、非極性有機溶媒に炭素環式芳香族アルデヒド類が溶
ける場合は、非極性有機溶媒に炭素環式芳香族アルデヒ
ド類を溶解した溶液を連続的に滴下するのが、操作性の
面から好ましい。
In the method for charging the carbocyclic aromatic aldehydes as the raw materials, the reaction is not hindered at all even if they are initially charged all at once, but the reaction takes place quickly, so that the amount of heat generated per hour increases. The temperature of the reaction solution may rise rapidly. Therefore, in order to control the reaction temperature, it is necessary to charge a nonpolar organic solvent and an alkali metal hydroxide to a reaction vessel, heat the reaction vessel to a predetermined temperature, and then sequentially charge the raw material carbocyclic aromatic aldehydes. desirable. At this time, when the carbocyclic aromatic aldehydes are dissolved in the non-polar organic solvent, it is preferable to continuously drop a solution in which the carbocyclic aromatic aldehydes are dissolved in the non-polar organic solvent from the viewpoint of operability. preferable.

【0019】反応時間は、0.5〜5時間程度であり、
適正な温度であれば0.5〜2時間で反応は完了する。
反応終了時生成した炭素環式芳香族カルボン酸類は、ア
ルカリ金属塩となり、溶媒中にスラリーとなって分散し
ている。したがって、生成した炭素環式芳香族カルボン
酸類は、任意の方法、例えば、反応完了後水を加え、炭
素環式芳香族カルボン酸アルカリ金属塩を溶解して分液
後、水層を酸析して回収するか、あるいは、水を添加し
て炭素環式芳香族カルボン酸アルカリ金属塩を溶解し、
分液前に酸析して溶媒層に炭素環式芳香族カルボン酸を
抽出分離し、溶媒を濃縮して回収することもできる。回
収した炭素環式芳香族カルボン酸は、必要に応じて公知
の方法によって精製する。
The reaction time is about 0.5 to 5 hours,
If the temperature is appropriate, the reaction is completed in 0.5 to 2 hours.
The carbocyclic aromatic carboxylic acids generated at the end of the reaction become alkali metal salts and are dispersed as a slurry in the solvent. Therefore, the generated carbocyclic aromatic carboxylic acids can be separated by any method, for example, after completion of the reaction, water is added, the alkali metal salt of the carbocyclic aromatic carboxylic acid is dissolved and separated, and then the aqueous layer is subjected to acid precipitation. Or recover, or dissolve the alkali metal salt of carbocyclic aromatic carboxylic acid by adding water,
It is also possible to carry out acid precipitation before liquid separation, to extract and separate the carbocyclic aromatic carboxylic acid in the solvent layer, and to collect and recover the solvent. The recovered carbocyclic aromatic carboxylic acid is purified, if necessary, by a known method.

【0020】[0020]

【実施例】実施例1 容量500mlの撹拌機付きフラスコにキシレン150
g、純度95%の水酸化カルウム30g(0.509モ
ル)、p−トルアルデヒド12.2g(0.102モ
ル)を仕込み、撹拌下、100℃まで昇温し、2時間撹
拌を継続して反応させた。その後、反応液に水200g
を加え、生成したp−トルイル酸カリウム塩を溶解した
のち、30分間静置後分液し、下層の水層に塩酸を加え
てpH2.0とし、析出した結晶を濾過、水洗し、乾燥
してp−トルイル酸13.7gを得た。このp−トルイ
ル酸を液体クロマトグラフを用いて分析し、面積百分率
による純度を求めた。その結果、p−トルイル酸の純度
は99.6%、収率は99モル%であった。
EXAMPLES Example 1 Xylene 150 was placed in a 500-ml flask equipped with a stirrer.
g, 30 g (0.509 mol) of 95% pure potassium hydroxide and 12.2 g (0.102 mol) of p-tolualdehyde were heated to 100 ° C. with stirring, and stirring was continued for 2 hours. Reacted. Then, 200 g of water was added to the reaction solution.
After dissolving the formed potassium p-toluate, the mixture was allowed to stand for 30 minutes and separated, and the pH of the lower aqueous layer was adjusted to 2.0 by adding hydrochloric acid. The precipitated crystals were filtered, washed with water, and dried. This gave 13.7 g of p-toluic acid. This p-toluic acid was analyzed using a liquid chromatograph, and the purity by area percentage was determined. As a result, the purity of p-toluic acid was 99.6%, and the yield was 99 mol%.

【0021】実施例2〜6 実施例1の反応溶媒のキシレンを表1に示す他の反応溶
媒に代えた以外は、実施例1と同一条件で同様の操作を
行い、実施例1と同様にp−トルイル酸の純度と収率を
求めた。その結果を表1に示す。
Examples 2 to 6 The same operation as in Example 1 was carried out under the same conditions as in Example 1 except that xylene as the reaction solvent in Example 1 was replaced with another reaction solvent shown in Table 1. The purity and yield of p-toluic acid were determined. Table 1 shows the results.

【0022】[0022]

【表1】 [Table 1]

【0023】実施例7〜13 実施例1の原料であるp−トルアルデヒドに代えて等モ
ルの表2に示す原料を用い、実施例1と同一条件で同様
の操作を行い、実施例1と同様に得られた炭素環式芳香
族カルボン酸の純度と収率を求めた。その結果を表2に
示す。
Examples 7 to 13 The same operation as in Example 1 was carried out under the same conditions as in Example 1 except that the raw materials shown in Table 2 were used in place of p-tolualdehyde as the raw material of Example 1. Similarly, the purity and yield of the obtained carbocyclic aromatic carboxylic acid were determined. Table 2 shows the results.

【0024】[0024]

【表2】 [Table 2]

【0025】比較例 実施例1の反応溶媒をキシレンからDMF、トリエチレ
ングリコールまたはスルホランに代えた以外は、実施例
1と同一条件で同様の操作を行なったが、いずれの場合
もp−トルイル酸はほとんど生成しなかった。
Comparative Example A similar operation was carried out under the same conditions as in Example 1 except that the reaction solvent in Example 1 was changed from xylene to DMF, triethylene glycol or sulfolane. In each case, p-toluic acid was used. Hardly produced.

【0026】[0026]

【発明の効果】本発明の炭素環式芳香族カルボン酸類の
製造方法は、高価な酸化剤が不要で、温和な反応条件で
安全に反応を行うことができるから、特殊な反応装置も
必要なく、高純度、高収率で炭素環式芳香族カルボン酸
を得ることができ、工業的に極めて有効な方法である。
According to the method for producing carbocyclic aromatic carboxylic acids of the present invention, an expensive oxidizing agent is not required, and the reaction can be carried out safely under mild reaction conditions. It is an industrially extremely effective method because a carbocyclic aromatic carboxylic acid can be obtained with high purity and high yield.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 炭素環式芳香族アルデヒド類を酸化して
対応するカルボン酸を製造する方法において、炭素環式
芳香族アルデヒド類を非極性有機溶媒中、アルカリ金属
水酸化物の存在下加熱することを特徴とする炭素環式芳
香族カルボン酸類の製造方法。
1. A method for producing a corresponding carboxylic acid by oxidizing a carbocyclic aromatic aldehyde, wherein the carbocyclic aromatic aldehyde is heated in a nonpolar organic solvent in the presence of an alkali metal hydroxide. A method for producing a carbocyclic aromatic carboxylic acid, which comprises the steps of:
JP2000281413A 2000-09-18 2000-09-18 Process for producing carbocyclic aromatic carboxylic acids Expired - Fee Related JP3655540B2 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002212132A (en) * 2001-01-23 2002-07-31 Mitsubishi Gas Chem Co Inc Method for producing aromatic carboxylic acids
JP2009029759A (en) * 2007-07-30 2009-02-12 Canon Inc Manufacturing method of carboxylic acid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002212132A (en) * 2001-01-23 2002-07-31 Mitsubishi Gas Chem Co Inc Method for producing aromatic carboxylic acids
JP4692702B2 (en) * 2001-01-23 2011-06-01 三菱瓦斯化学株式会社 Process for producing aromatic carboxylic acids
JP2009029759A (en) * 2007-07-30 2009-02-12 Canon Inc Manufacturing method of carboxylic acid

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