JPH0224263B2 - - Google Patents

Info

Publication number
JPH0224263B2
JPH0224263B2 JP57208255A JP20825582A JPH0224263B2 JP H0224263 B2 JPH0224263 B2 JP H0224263B2 JP 57208255 A JP57208255 A JP 57208255A JP 20825582 A JP20825582 A JP 20825582A JP H0224263 B2 JPH0224263 B2 JP H0224263B2
Authority
JP
Japan
Prior art keywords
acid
reaction
benzene
cation exchange
mandelic acid
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.)
Expired - Lifetime
Application number
JP57208255A
Other languages
Japanese (ja)
Other versions
JPS5998033A (en
Inventor
Takehiko Kakimoto
Tetsuo Yonezawa
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.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP57208255A priority Critical patent/JPS5998033A/en
Publication of JPS5998033A publication Critical patent/JPS5998033A/en
Publication of JPH0224263B2 publication Critical patent/JPH0224263B2/ja
Granted 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

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

マンデル酸は農薬あるいは医薬の中間体として
有用な化学物質である。しかして該酸の製造法と
して古くよりベンズアルデヒドと青酸を反応させ
て得られるマンデル酸ニトリルを酸で加水分解す
る方法が知られている。 しかし青酸という猛毒な化合物を取り扱わねば
ならないことは作業衛生面、廃水処理面等で多大
の注意が必要であり工業的方法としては好ましい
とは言えない。 そこで本出願人は先にかかる有害な原料を使用
せず工業的有利にマンデル酸を製造する方法とし
てグリオキシル酸1モルに対して硫酸0.1モル以
上1モル未満、及び酢酸0.5〜10モルの共存下で
グリオキシル酸とベンゼンを反応させる方法を提
案した。該方法においてマンデル酸の収率はグリ
オキシル酸に対し60%程度である。 ところが今回、本出願人は更に収率良くマンデ
ル酸を製造出来る方法を見出し本発明を完成し
た。即ち、本発明は実質的に無水状態で陽イオン
交換樹脂の存在下、グリオキシル酸とベンゼンを
反応させてマンデル酸ベンジル誘導体を得、次い
で該誘導体を加水分解してマンデル酸を製造する
もので、マンデル酸の収率はグリオキシル酸に対
し最高で90%にも達し極めて効率良くマンデル酸
が得られるのである。 本発明の方法を化学式で示せば次の通りであ
る。 まず本発明を実施するに際して触媒として陽イ
オン交換樹脂を使用する。 該樹脂としてはスルホン酸型の強酸性陽イオン
交換樹脂が最も有利に用いられるが、カルボン酸
型、リン酸型等の弱酸性陽イオン交換樹脂の使用
も可能である。強酸性陽イオン交換樹脂の具体例
としては、アンバリースリト15、アンバーリスト
XN−1004、アンバーライトIR−120B、アンバ
ーライトIR−122、アンバーライトIR−124、ア
ンバーライトIRC−84(いずれもローム・アン
ド・ハース社製)、ドウライトC20、ドウライト
C10、ドウライトCC3(いずれもケミカル・プロ
セス社製)、ダウエツクス50WX8、ダウエツクス
MSC−1、ダウエツクスCCR−2(いずれもダ
ウ・ケミカル社製)、その他レバチツト(バイエ
ル社製)、ナルサイト(ナシヨナルアメリカン社
製)、パームチツト(パームチツト社製)、ウオル
フアチツト(フアルベニンド社製)、ダイヤイオ
ン(三菱化成社製)等がある。上記陽イオン交換
樹脂はその平均孔径が50〜1000Å程度のものが特
に有利に使用される。 これらはグリオキシル酸に対して50〜300重量
%程度の量で用いられる。 反応は実質的に無水状態で行わなければならな
い。グリオキシル酸は通常40%程度の水溶液とし
て販売されているので、予めこれを脱水濃縮して
グリオキシル酸1水和物、グリオキシル酸無水物
とした後、過剰のベンゼンと混合して反応を行な
えば良い。ベンゼンは原料と反応溶媒を兼ねる。
又、グリオキシル酸水溶液をそのまま使用する場
合はベンゼンと該液を混合し、一旦ベンゼンと水
とを共沸脱水してから反応を開始すれば良い。い
ずれにしても反応を効率良く進行させるためには
系中の水の量を5重量%以下に減少させなければ
ならない。反応時にかかる量より以上の水が存在
するとマンデル酸の収率は著しく低下する。 ベンゼンはグリオキシル酸に対して3倍〜20倍
モル程度の範囲で使用される。反応温度は50〜80
℃、反応時間は5〜50時間が好ましい。反応の進
行につれて水が副生するので好ましくは反応は脱
水下に実施される。 反応時に酢酸を助触媒として使用すると効果的
である。その使用量はグリオキシル酸1モルに対
し10モル以下、好ましくは2〜5モルである。 特に無水酢酸の使用は系内の水の補促剤として
の作用をも発揮するので有利である。10モル以上
の酢酸の使用は反応速度が低下し又、ハルツの副
生が顕著となる。 かかる反応によつて中間体としてマンデル酸ベ
ンジル誘導体
Mandelic acid is a chemical substance useful as an intermediate for agricultural chemicals or medicines. However, as a method for producing the acid, a method has long been known in which mandelic acid nitrile, which is obtained by reacting benzaldehyde with hydrocyanic acid, is hydrolyzed with an acid. However, the necessity of handling hydrocyanic acid, a highly toxic compound, requires great care in terms of work hygiene and wastewater treatment, and is therefore not desirable as an industrial method. Therefore, the present applicant first proposed a method for industrially advantageous production of mandelic acid without using such harmful raw materials, in which sulfuric acid is present in the presence of 0.1 mole or more and less than 1 mole and acetic acid 0.5 to 10 mole per mole of glyoxylic acid. proposed a method for reacting glyoxylic acid and benzene. In this method, the yield of mandelic acid is about 60% based on glyoxylic acid. However, the present applicant has now discovered a method for producing mandelic acid with even higher yield and has completed the present invention. That is, the present invention involves reacting glyoxylic acid and benzene in the presence of a cation exchange resin in a substantially anhydrous state to obtain a benzyl mandelic acid derivative, and then hydrolyzing the derivative to produce mandelic acid. The yield of mandelic acid is up to 90% of that of glyoxylic acid, and mandelic acid can be obtained extremely efficiently. The chemical formula of the method of the present invention is as follows. First, when carrying out the present invention, a cation exchange resin is used as a catalyst. As the resin, a sulfonic acid type strongly acidic cation exchange resin is most advantageously used, but it is also possible to use a weakly acidic cation exchange resin such as a carboxylic acid type or a phosphoric acid type. Specific examples of strongly acidic cation exchange resins include Amberlyst 15 and Amberlyst.
XN-1004, Amberlite IR-120B, Amberlite IR-122, Amberlite IR-124, Amberlite IRC-84 (all manufactured by Rohm and Haas), Dowlite C20, Dowlite
C10, Dowex CC3 (all manufactured by Chemical Process Co., Ltd.), Dowex 50WX8, Dowex
MSC-1, Dowex CCR-2 (all manufactured by Dow Chemical Company), Revacit (manufactured by Bayer), Narcite (manufactured by National American Company), Palmtit (manufactured by Palmtit), Wolfachit (manufactured by Falbenindo), Examples include Diamondion (manufactured by Mitsubishi Kasei Corporation). The above-mentioned cation exchange resins having an average pore diameter of about 50 to 1000 Å are particularly advantageously used. These are used in an amount of about 50 to 300% by weight based on glyoxylic acid. The reaction must be conducted in substantially anhydrous conditions. Glyoxylic acid is usually sold as a 40% aqueous solution, so it can be dehydrated and concentrated to form glyoxylic acid monohydrate and glyoxylic anhydride, and then mixed with excess benzene to carry out the reaction. . Benzene serves both as a raw material and as a reaction solvent.
In addition, when using the aqueous glyoxylic acid solution as it is, it is sufficient to mix the liquid with benzene and once azeotropically dehydrate the benzene and water before starting the reaction. In any case, in order for the reaction to proceed efficiently, the amount of water in the system must be reduced to 5% by weight or less. If more water than this amount is present during the reaction, the yield of mandelic acid will drop significantly. Benzene is used in an amount of about 3 to 20 times the molar amount of glyoxylic acid. Reaction temperature is 50-80
℃, and the reaction time is preferably 5 to 50 hours. Since water is produced as a by-product as the reaction progresses, the reaction is preferably carried out under dehydration. It is effective to use acetic acid as a cocatalyst during the reaction. The amount used is 10 mol or less, preferably 2 to 5 mol, per 1 mol of glyoxylic acid. In particular, the use of acetic anhydride is advantageous because it also acts as a co-stimulant for water in the system. If more than 10 moles of acetic acid are used, the reaction rate will decrease and Harz by-products will become noticeable. Such a reaction produces a benzyl mandelate derivative as an intermediate.

【式】が生成 する。 次いで該誘導体を加水分解してマンデル酸とす
る。前記反応においてはマンデル酸ベンジル誘導
体以外に
[Formula] is generated. The derivative is then hydrolyzed to mandelic acid. In the above reaction, in addition to the benzyl mandelate derivative,

【式】あるいは酢 酸共存在下では[Formula] or vinegar In the presence of acid

【式】ある いは 等が生成するがいずれも加水分解によつてマンデ
ル酸に転換され得る。加水分解は次の様に実施さ
れる。 加水分解はアルカリでも酸(特に陽イオン交換
樹脂)でも可能である。 アルカリによる加水分解はまず前記反応で得ら
れたマンデル酸ベンジル誘導体含有反応生成液か
ら陽イオン交換樹脂を別する。液に水を加え
次いで水酸化アルカリを水層のPHが11程度になる
まで添加し、約1時間程度加熱撹拌するとマンデ
ル酸(アルカリ塩)が生成する。該塩は水層中に
含有されているので該層をベンゼン層と分離し、
水層に塩酸、硫酸等の酸を添加してPHを5〜6程
度にコントロールするとマンデル酸の結晶が析出
する。析出したマンデル酸は過、遠心分離等常
法に従つて系から分離され少量の冷水で洗浄、乾
燥して最終製品を得る。必要があれば適宜再結晶
等の精製操作が実施される。 一方、酸による加水分解としては硫酸、塩酸等
の鉱酸を用いても出来るが、ベンゼンとグリオキ
シル酸との反応触媒がそのまま加水分解の触媒と
して使用出来る点、触媒の回収が容易である等の
点で陽イオン交換樹脂の使用が有利である。陽イ
オン交換樹脂を用いて加水分解を行なうにはマン
デル酸誘導体含有反応生成液からベンゼンを留去
した後系に水を加えて加熱すれば良い。ベンゼン
留去の際、陽イオン交換樹脂の劣化等の恐れがあ
る時は反応生成液から一旦、触媒を別したあと
でベンゼンを留去し次いで水及び陽イオン交換樹
脂を添加して加水分解しても良い。 加水分解終了後は陽イオン交換樹脂を別し
液を冷却すればマンデル酸が析出するので常法に
従つて単離する。 かくして得られたマンデル酸は医薬、農薬の中
間体として有用である。 次に実例を挙げて本発明の方法を更に具体的に
説明する。 実例 1 撹拌器、温度計、デカンター、冷却管を付設し
た500mlの4つ口フラスコにグリオキシル酸1水
和物0.1モル、ベンゼン2モル、酢酸1モル及び
レバチツトSPC118BG(バイエル社製、陽イオン
交換樹脂)100gを仕込み撹拌しながら80℃で24
時間、脱水下に反応を行ないマンデル酸ベンゼン
誘導体 反応生成液を得た。 陽イオン交換樹脂を別しベンゼンでよく洗浄
した後、洗浄液と液を混合した。 該混合液に水500mlを加え、撹拌下に40%水酸
化ナトリウム水溶液を水層のPHが11になるまで添
加した。その後、室温で約30分間加水分解反応を
行つた。 水層とベンゼン層を分離し水層に塩酸をPHが1
以下となるまで添加しマンデル酸の結晶を析出さ
せた。グリオキシル酸に対するマンデル酸の収率
は80%であつた。 尚、得られたマンデル酸は再結晶後、融点及び
IRスペクトルを標品と比較し両者が一致したこ
とにより確認した。 実例 2 グリオキシル酸無水物0.4モル及びベンゼン2
モル、無水酢酸0.2モル及びレバチツト
SPC118BG50gを実例1と同一のフラスコに仕込
み、75℃で24時間反応を行つた。 その後は実例1と同一の方法で加水分解を行な
い80%の収率でマンデル酸を得た。 実例 3 実例1と同一のフラスコにグリオキシル酸1モ
ル、酢酸3.5モル、ベンゼン10モル及びレバチツ
トSPC118G150gを仕込み、24時間共沸脱水反応
を行つた。 反応終了液から陽イオン交換樹脂を別し、
液を減圧蒸留して酢酸及びベンゼンを留去した。 得られた濃縮液120gに水100gを添加、更にダ
イヤイオンSK−IBH(三菱化成社製、陽イオン交
換樹脂)100gを混合し、80℃で8時間加水分解
反応を行つた。反応終了後、陽イオン交換樹脂を
別し液を15℃まで冷却した。 析出したジフエニル酢酸を分離した液を濃縮
後、再度15℃まで冷却するとマンデル酸の結晶が
析出した。収率は90%であつた。
[Formula] or etc., which can all be converted to mandelic acid by hydrolysis. Hydrolysis is carried out as follows. Hydrolysis is possible with either alkaline or acidic (especially cation exchange resins). In hydrolysis with an alkali, the cation exchange resin is first separated from the reaction product solution containing the benzyl mandelate derivative obtained in the above reaction. Water is added to the liquid, and then alkali hydroxide is added until the pH of the aqueous layer reaches about 11. Mandelic acid (alkali salt) is produced by heating and stirring for about 1 hour. Since the salt is contained in the aqueous layer, this layer is separated from the benzene layer,
When an acid such as hydrochloric acid or sulfuric acid is added to the aqueous layer to control the pH to about 5 to 6, mandelic acid crystals are precipitated. The precipitated mandelic acid is separated from the system by conventional methods such as filtration and centrifugation, washed with a small amount of cold water, and dried to obtain the final product. If necessary, purification operations such as recrystallization are carried out as appropriate. On the other hand, acid hydrolysis can also be carried out using mineral acids such as sulfuric acid and hydrochloric acid, but there are some advantages such as the fact that the reaction catalyst of benzene and glyoxylic acid can be used as it is as a hydrolysis catalyst, and the catalyst can be easily recovered. In this respect, the use of cation exchange resins is advantageous. To carry out hydrolysis using a cation exchange resin, benzene may be distilled off from the reaction product solution containing a mandelic acid derivative, and then water may be added to the system and heated. When removing benzene, if there is a risk of deterioration of the cation exchange resin, first remove the catalyst from the reaction product liquid, distill off the benzene, and then add water and the cation exchange resin to hydrolyze it. It's okay. After the hydrolysis is completed, the cation exchange resin is separated and the liquid is cooled to precipitate mandelic acid, which is then isolated using a conventional method. The mandelic acid thus obtained is useful as an intermediate for pharmaceuticals and agricultural chemicals. Next, the method of the present invention will be explained in more detail by giving examples. Example 1 In a 500 ml four-necked flask equipped with a stirrer, a thermometer, a decanter, and a cooling tube, 0.1 mol of glyoxylic acid monohydrate, 2 mol of benzene, 1 mol of acetic acid, and Levacit SPC118BG (manufactured by Bayer, cation exchange resin) were added. ) 100g and stirred at 80℃ for 24 hours.
Mandelic acid benzene derivatives are obtained by performing the reaction under dehydration for a long time. A reaction product liquid was obtained. After the cation exchange resin was separated and thoroughly washed with benzene, the washing liquid and the liquid were mixed. 500 ml of water was added to the mixture, and a 40% aqueous sodium hydroxide solution was added while stirring until the pH of the aqueous layer reached 11. Thereafter, a hydrolysis reaction was carried out at room temperature for about 30 minutes. Separate the aqueous layer and benzene layer and add hydrochloric acid to the aqueous layer until the pH is 1.
The amount of mandelic acid was added to precipitate crystals of mandelic acid. The yield of mandelic acid based on glyoxylic acid was 80%. In addition, the obtained mandelic acid has a melting point and a
This was confirmed by comparing the IR spectrum with the standard product and finding a match between the two. Example 2 0.4 mol of glyoxylic anhydride and 2 benzene
mol, acetic anhydride 0.2 mol and rebatit
50 g of SPC118BG was placed in the same flask as in Example 1, and the reaction was carried out at 75°C for 24 hours. Thereafter, hydrolysis was carried out in the same manner as in Example 1 to obtain mandelic acid with a yield of 80%. Example 3 Into the same flask as in Example 1, 1 mole of glyoxylic acid, 3.5 moles of acetic acid, 10 moles of benzene, and 150 g of Rebachito SPC118G were charged, and an azeotropic dehydration reaction was carried out for 24 hours. Separate the cation exchange resin from the reaction finished solution,
The liquid was distilled under reduced pressure to remove acetic acid and benzene. 100 g of water was added to 120 g of the obtained concentrate, and 100 g of Diaion SK-IBH (manufactured by Mitsubishi Kasei Corporation, cation exchange resin) was added thereto, followed by a hydrolysis reaction at 80° C. for 8 hours. After the reaction was completed, the cation exchange resin was removed and the liquid was cooled to 15°C. After concentrating the liquid from which the precipitated diphenyl acetic acid had been separated, it was cooled again to 15°C, and mandelic acid crystals were precipitated. The yield was 90%.

Claims (1)

【特許請求の範囲】[Claims] 1 実質的に無水状態で陽イオン交換樹脂の存在
下、グリオキシル酸とベンゼンを反応させてマン
デル酸ベンジル誘導体を得、次いで該誘導体を加
水分解することを特徴とするマンデル酸の製造方
法。
1. A method for producing mandelic acid, which comprises reacting glyoxylic acid and benzene in a substantially anhydrous state in the presence of a cation exchange resin to obtain a benzyl mandelic acid derivative, and then hydrolyzing the derivative.
JP57208255A 1982-11-26 1982-11-26 Mandelic acid production method Granted JPS5998033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57208255A JPS5998033A (en) 1982-11-26 1982-11-26 Mandelic acid production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57208255A JPS5998033A (en) 1982-11-26 1982-11-26 Mandelic acid production method

Publications (2)

Publication Number Publication Date
JPS5998033A JPS5998033A (en) 1984-06-06
JPH0224263B2 true JPH0224263B2 (en) 1990-05-29

Family

ID=16553210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57208255A Granted JPS5998033A (en) 1982-11-26 1982-11-26 Mandelic acid production method

Country Status (1)

Country Link
JP (1) JPS5998033A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010285420A (en) * 2009-05-11 2010-12-24 Mitsubishi Rayon Co Ltd Process for producing optically active aromatic hydroxycarboxylic acid condensate and optically active compound
FR3013351B1 (en) 2013-11-15 2016-01-01 Rhodia Operations PROCESS FOR THE PREPARATION OF MANDELIC AROMATIC COMPOUND AND AROMATIC ALDEHYDE COMPOUND

Also Published As

Publication number Publication date
JPS5998033A (en) 1984-06-06

Similar Documents

Publication Publication Date Title
JPS6338035B2 (en)
JPH0224263B2 (en)
JPS62201840A (en) Production of cinnamic acid compound
JP3339106B2 (en) Method for producing cis epoxy succinate
US4590295A (en) Process for the manufacture of p-hydroxyphenyl-acetic acid
KR100564072B1 (en) Method for non-pressurely preparing α, α-dimethylphenylacetic acid from α, α-dimethylbenzyl cyanide
JP3219256B2 (en) Method for producing bis (p-hydroxyphenyl) acetic acid
JPH03275644A (en) Production of alpha-hydroxyisobutyric acid
JP3257779B2 (en) Method for producing tartanyl acids
KR800001550B1 (en) Preparing process for 5-(4-hyroxy phenyl)hydantoins
JPS58120507A (en) Continuous manufacture of hydrazine
SU1313848A1 (en) Method for producing formic acid
JPH0581573B2 (en)
JP2901237B2 (en) 2-carbamoyl-3,4,5,6-tetrafluorobenzoic acid, a process for producing the same and derivatives thereof.
JPS6127979A (en) Preparation of hydroxyflavan compound
JPH07196610A (en) Method for producing 5-chloro-2-oxindole
KR930002277B1 (en) Method for preparing 5- (4-hydroxyphenyl) hydantoin
JPH09110784A (en) Production of phthalic acid derivative
JPS58953A (en) Preparation of butyric acid derivative
JPH0451550B2 (en)
JPH0335308B2 (en)
JPS61112043A (en) Mandelic acid production method
JP2001261642A (en) Method for producing 1-alkylindole-3-carboxylic acids
JPS60185752A (en) Production of alpha-acetamidocinnamic acid
JPS6261011B2 (en)