JPH03188044A - Production of acyloxyaliphatic hydrocarbon - Google Patents

Production of acyloxyaliphatic hydrocarbon

Info

Publication number
JPH03188044A
JPH03188044A JP1328053A JP32805389A JPH03188044A JP H03188044 A JPH03188044 A JP H03188044A JP 1328053 A JP1328053 A JP 1328053A JP 32805389 A JP32805389 A JP 32805389A JP H03188044 A JPH03188044 A JP H03188044A
Authority
JP
Japan
Prior art keywords
hydrocarbon
alkali metal
reaction
formula
general formula
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.)
Pending
Application number
JP1328053A
Other languages
Japanese (ja)
Inventor
Shinichi Matsuura
松浦 眞一
Osamu Miyano
宮野 修
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.)
TOUSOO YUKI KAGAKU KK
Original Assignee
TOUSOO YUKI KAGAKU KK
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 TOUSOO YUKI KAGAKU KK filed Critical TOUSOO YUKI KAGAKU KK
Priority to JP1328053A priority Critical patent/JPH03188044A/en
Publication of JPH03188044A publication Critical patent/JPH03188044A/en
Pending legal-status Critical Current

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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

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

Abstract

PURPOSE:To easily obtain the title compound as e.g. an intermediate for medicines or pesticides without after-treatment problems by reaction between a dihalogenated hydrocarbon and an alkali metal salt of aliphatic carboxylic acid in the presence of each specific phase-transfer catalyst and solvent. CONSTITUTION:In the presence of a phase-transfer catalyst of formula I (R is hydrocarbon residue; X is halogen), a reaction is made, at 20-300 deg.C, (esp. 30-100) deg.C in an acetic alkyl ester solvent, between (A) a dihalogenated hydrocarbon of formula II (X1 and X2 are each halogen differing from each other; A is alkylene) and (B) and alkali metal salt of aliphatic carboxylic acid of formula III (R is alkyl; M is alkali metal) using pref. 1.0-1.5mols per mol of the compounds A of the compound B, thus obtaining the objective compound of formula IV (X3 is halogen). The phase-transfer catalyst is e.g. tetramethylammonium chloride; and the solvent is e.g. n-butyl acetate.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、医薬、農薬等の中間体、あるいは各種化学商
品の原料として有用なアシルオキシ脂肪族炭化水素の製
造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing acyloxyaliphatic hydrocarbons useful as intermediates for pharmaceuticals, agricultural chemicals, etc., or raw materials for various chemical products.

〔従来の技術および発明が解決しようとする課題〕従来
、アシルオキシ脂肪族炭化水素を製造する方法として、
次のような方法が用いられている。
[Prior art and problems to be solved by the invention] Conventionally, as a method for producing acyloxyaliphatic hydrocarbons,
The following methods are used:

すなわち、相異なるハロゲン原子を有するジハロゲン化
炭化水素であるI−ブロモ−3−クロロプロパンと脂肪
族カルボン酸のアルカリ金属塩である酢酸カリウムを酢
酸溶媒中で反応させる方法である(Journal o
j the Americxn Che+ni(!l 
5ociety 70. 56(19540゜しかしな
がら、この方法は目的とする1−アセトキシ−3−クロ
ロプロパンの選択率が68%しかなく、これ以外に1−
アセトレキ−3−ブロモプロパンおよび1.3−ジアセ
トキシプロパン等が副生じ、原料であるハロゲン化炭化
水素の一方のハロゲン原子のみを選択的にアシルオキシ
基に置換するには難しいものがあった。
That is, it is a method in which I-bromo-3-chloropropane, which is a dihalogenated hydrocarbon having different halogen atoms, and potassium acetate, which is an alkali metal salt of an aliphatic carboxylic acid, are reacted in an acetic acid solvent (Journal o
j the Americanxn Che+ni(!l
5ociety 70. 56 (19540°) However, this method has a selectivity of only 68% for the target 1-acetoxy-3-chloropropane;
Acetleky-3-bromopropane, 1,3-diacetoxypropane, etc. are produced as by-products, and it is difficult to selectively substitute only one halogen atom of the halogenated hydrocarbon raw material with an acyloxy group.

又、特開昭63−152341では、同反応を溶媒とし
てアルコール類、エーテル類および脂肪族ニトリル類等
、水溶性のものを用いて実施しており、好収率で目的物
が得られている。しかしながら、処理として大量の固体
をろ過しなければならず、工業的にはあまり好ましいも
のとは言い難い。
Furthermore, in JP-A-63-152341, the same reaction was carried out using water-soluble solvents such as alcohols, ethers, and aliphatic nitriles, and the desired product was obtained in good yield. . However, as a treatment, a large amount of solid must be filtered, and this is not very desirable from an industrial perspective.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは、上記の従来の欠点を解決すべく鋭意研究
を重ねた結果、相間移動触媒を用いることにより、相異
なるハロゲン原子を有するジハロゲン化炭化水素の一方
のハロゲン原子のみを選択的にアシルオキシ基に置換で
きることを見いだし、さらに水に難溶性の溶媒を反応溶
媒として用いることにより、後処理において水を加える
だけで生成した塩を極めて容易に分離できることを見い
出し本発明を完成するに至った。
As a result of extensive research to solve the above-mentioned conventional drawbacks, the present inventors have found that by using a phase transfer catalyst, only one halogen atom of a dihalogenated hydrocarbon having different halogen atoms can be selectively transferred. They discovered that the acyloxy group can be substituted with an acyloxy group, and further discovered that by using a poorly water-soluble solvent as the reaction solvent, the resulting salt could be separated extremely easily by simply adding water in post-treatment, leading to the completion of the present invention. .

すなわち、本発明の要旨とすると所は、一般式(1) %式%(1) (ただし、XlおよびX2は相異なるハロゲン原子であ
り、Aはアルキレン基である)で示されるジハロゲン化
炭化水素と、一般式(IT) RCOOM           (II)(ただし、
Rはアルキル基であり、Mはアルカリ金属である。) で示される脂肪族カルボン酸のアルカリ金属塩を、一般
式(m) R’4N+X           (m)(ただし、
R′は炭化水素残基であり、Xはハロゲン原子である。
That is, the gist of the present invention is that dihalogenated hydrocarbons represented by the general formula (1) % formula % (1) (wherein, Xl and X2 are different halogen atoms, and A is an alkylene group) and the general formula (IT) RCOOM (II) (however,
R is an alkyl group and M is an alkali metal. ) An alkali metal salt of an aliphatic carboxylic acid represented by the general formula (m) R'4N+X (m) (however,
R' is a hydrocarbon residue and X is a halogen atom.

) で示される相間移動触媒の存在下、酢酸アルキルエステ
ル溶媒中で反応させることを特徴とする、一般式(mV
) RCOO−A−X3   (rV) (ただし、X3はハロゲン原子であり、Aはアルキレン
基であり、Rはアルキル基である。)で示されるアシル
オキシ脂肪族炭化水素の製造方法に関する。
) in the presence of a phase transfer catalyst represented by the general formula (mV
) RCOO-A-X3 (rV) (wherein, X3 is a halogen atom, A is an alkylene group, and R is an alkyl group).

本発明によれば相異なる2種のハロゲン原子を有するジ
ハロゲン化水素の一方のハロゲン原子のみを選択的にア
シルオキシ基に置換することができる。しかも、反応溶
媒として水に難溶性の溶媒を用いるため、反応換水を加
えて生成した塩を溶解させることができる。
According to the present invention, only one halogen atom of a dihydrogen halide having two different types of halogen atoms can be selectively substituted with an acyloxy group. Furthermore, since a solvent that is poorly soluble in water is used as the reaction solvent, the salt produced can be dissolved by adding reaction water.

その結果、従来法に比べて高い選択性、しかも高収率で
高品質の1−アセトキシ−3−クロロプロパン等を得る
ことができることから、工業的に極めて優れた方法と言
うことができる。
As a result, it is possible to obtain high-quality 1-acetoxy-3-chloropropane and the like with higher selectivity and higher yield than conventional methods, so it can be said to be an extremely excellent method industrially.

〔作 用〕[For production]

本発明の一般式(I)で示される原料であるジハロゲン
化炭化水素において、XlおよびX2で示されるハロゲ
ン原子は、フッ素、塩素、臭素、ヨウ素の各原子がある
がXlとX2のいずれか一方が塩素原子であり、他方が
臭素原子またはヨウ素原子である場合は、臭素原子また
はヨウ素原子がアシルオキシ基に高い選択率で置換され
、目的とするアシルオキシ脂肪族炭化水素の収率が大き
くなるため、本発明において好ましい態様である。
In the dihalogenated hydrocarbon that is the raw material represented by the general formula (I) of the present invention, the halogen atoms represented by Xl and X2 include fluorine, chlorine, bromine, and iodine atoms, but either Xl or X2 When is a chlorine atom and the other is a bromine atom or an iodine atom, the bromine atom or iodine atom is substituted with the acyloxy group with high selectivity, and the yield of the target acyloxy aliphatic hydrocarbon increases. This is a preferred embodiment of the present invention.

又、一般式(T)中、Aで示されるアルキレン基として
は、メチレン、エチレン、プロピレン、ブチレン、ペン
チレン、ヘキシレン等が挙げられる。
Further, in the general formula (T), examples of the alkylene group represented by A include methylene, ethylene, propylene, butylene, pentylene, hexylene, and the like.

本発明において用いられる一般式(1)で表わされるジ
ハロゲン化炭化水素としては、ブロモクロロメタン、1
−ブロモ−2−クロロエタン、1−ブロモ−3−クロロ
プロパン、1−ブロモ−4−クロロブタン、1−ブロモ
−5−クロロペンタン、1−ブロモー6−ヘキサン、1
−ヨード−2−クロロエタン、1−ヨード−3−クロロ
プロパン、1−ヨード−2=ブロモエタンが挙げられる
The dihalogenated hydrocarbon represented by the general formula (1) used in the present invention includes bromochloromethane, 1
-Bromo-2-chloroethane, 1-bromo-3-chloropropane, 1-bromo-4-chlorobutane, 1-bromo-5-chloropentane, 1-bromo-6-hexane, 1
-iodo-2-chloroethane, 1-iodo-3-chloropropane, and 1-iodo-2=bromoethane.

次に、もう一方の原料である一般式(II)で表わされ
る脂肪族カルボン酸のアルカリ金属塩は、アルキル基の
炭素数が1〜6で、アルカリ金属としては、リチウム、
ナトリウム、カリウム、ルビジウムが挙げられるが、収
率の面でカリウムが好ましい。
Next, the other raw material, an alkali metal salt of an aliphatic carboxylic acid represented by the general formula (II), has an alkyl group having 1 to 6 carbon atoms, and the alkali metal includes lithium,
Examples include sodium, potassium, and rubidium, with potassium being preferred in terms of yield.

本発明において用いられる一般式1)の相間移動触媒と
してはテトラメチルアンモニウムクロライド、ベンジル
トリメチルアンモニウムクロライド、ベンジルトリエチ
ルアンモニウムクロライド、ベンジルトリブチルアンモ
ニウムクロライド、テトラブチルアンモニウムクロライ
ド、テトラブチルアンモニウムブロマイド等が挙げられ
る。
Examples of the phase transfer catalyst of general formula 1) used in the present invention include tetramethylammonium chloride, benzyltrimethylammonium chloride, benzyltriethylammonium chloride, benzyltributylammonium chloride, tetrabutylammonium chloride, tetrabutylammonium bromide, and the like.

また、これらの使用量は一般式(I)で示されるハロゲ
ン化炭化水素1モルに対して0.001〜0.005モ
ルの範囲で使用するのが好ましい。
Moreover, it is preferable that these are used in an amount of 0.001 to 0.005 mol per 1 mol of the halogenated hydrocarbon represented by the general formula (I).

溶媒としては、水に難溶のエステル類である酢酸アルキ
ルエステルが好ましい。たとえば、酢酸エチルエステル
、酢酸n−ブチルエステル、酢酸イソブチルエステル、
等が挙げられる。
As the solvent, acetic acid alkyl esters, which are esters that are sparingly soluble in water, are preferred. For example, ethyl acetate, n-butyl acetate, isobutyl acetate,
etc.

これらの溶媒の使用量は特に制限されないが、通常はハ
ロゲン化炭化水素に対して3〜10倍モルの範囲で用い
ることが好ましい。
The amount of these solvents to be used is not particularly limited, but it is usually preferable to use them in a molar range of 3 to 10 times the amount of the halogenated hydrocarbon.

本発明における反応は、反応温度が20〜200℃で、
好ましくは30〜100℃の範囲で進行する。
The reaction in the present invention has a reaction temperature of 20 to 200°C,
Preferably, the process proceeds in the range of 30 to 100°C.

本発明の置換反応において一般式(1)で示されるハロ
ゲン化炭化水素と脂肪族カルボン酸のアルカリ金属塩は
理論量で反応させてもよいが、ハロゲン化炭化水素1モ
ルに対して脂肪族カルボン酸のアルカリ金属塩を1.0
−1.5モルの範囲で過剰に使用するのが好ましい。
In the substitution reaction of the present invention, the halogenated hydrocarbon represented by the general formula (1) and the alkali metal salt of the aliphatic carboxylic acid may be reacted in stoichiometric amounts; 1.0 alkali metal salt of acid
It is preferable to use an excess in the range of -1.5 mol.

反応終了後、反応混合物に水を加えると生成した塩が溶
解できることから、ろ過等の手段をとることなく簡単な
分岐操作で後処理することができる。抽出液は減圧下蒸
留することにより目的物であるアシルオキシ脂肪族炭化
水素を容易に分離することができ同時に回収した溶媒は
そのまま再使用が可能である。
After the reaction is completed, the salt produced can be dissolved by adding water to the reaction mixture, so it can be post-treated by a simple branching operation without using any means such as filtration. By distilling the extract under reduced pressure, the target acyloxyaliphatic hydrocarbon can be easily separated, and at the same time, the recovered solvent can be reused as is.

〔実施例〕〔Example〕

本発明を以下の実施例にて更に詳細に説明するが、これ
らに限定されるものではない。
The present invention will be explained in more detail in the following examples, but is not limited thereto.

実施例1 還流冷却器、温度計及び攪拌機を取り付けた300 m
lの三つロフラスコに溶媒として酢酸イソブチル130
 mlを入れ、これに1−ブロム−3−クロルプロパン
(78,7g、 0.5mol) 、酢酸カリウム(5
3,9g、 0.55aol) 、テトラブチルアンモ
ニウムブロマイド(0,5g、 0.0016+aol
)を加えて50℃で20時間反応した。
Example 1 300 m equipped with reflux condenser, thermometer and stirrer
Isobutyl acetate as a solvent in a three-necked flask with 130
1-bromo-3-chloropropane (78.7 g, 0.5 mol) and potassium acetate (5 mol).
3.9g, 0.55aol), tetrabutylammonium bromide (0.5g, 0.0016+aol)
) was added and reacted at 50°C for 20 hours.

反応液に水を200 mlを加えて振とう後、分液し有
機層を取り出し、さらに飽和食塩水100 mlを加え
て振とう後、分液して有機層を取り出した。
After adding 200 ml of water to the reaction solution and shaking, the mixture was separated and the organic layer was taken out. 100 ml of saturated brine was added and shaken, then the layers were separated and the organic layer was taken out.

ころ、収率が91%で生成していることを確認した。(
転化率97.7%、選択率93.6%)さらに、酢酸イ
ソブチルを回収後、減圧蒸留で1−アセトキシ−3−ク
ロロプロパン58.0gを得た。沸点97℃/70m+
nHg(蒸留収率85%)実施例2 実施例1の反応温度を25℃に換えて実施例1と同様の
操作で1−アセトキシ−3−クロロプロパンを得た。そ
の結果を表1に示した。
It was confirmed that the product was produced at a yield of 91%. (
After recovering isobutyl acetate (conversion rate: 97.7%, selectivity: 93.6%), 58.0 g of 1-acetoxy-3-chloropropane was obtained by distillation under reduced pressure. Boiling point 97℃/70m+
nHg (distillation yield 85%) Example 2 1-acetoxy-3-chloropropane was obtained in the same manner as in Example 1 except that the reaction temperature in Example 1 was changed to 25°C. The results are shown in Table 1.

実施例3 実施例1のテトラブチルアンモニウムブロマイドの使用
量を換え、実施例1と同様の操作により1−アセトキシ
−3−クロロプロパンを得た。
Example 3 1-acetoxy-3-chloropropane was obtained in the same manner as in Example 1 except that the amount of tetrabutylammonium bromide used was changed.

その結果を表1に示した。The results are shown in Table 1.

(反応スケールは実施例1と同様である。)ここでガス
クロマトグラフィーで定量したと〔発明の効果〕 本発明によれば、相異なる2種のハロゲン原子を有する
ハロゲン化炭化水素の一方のハロゲン原子のみを選択的
にアシルオキシ基に置換することができる。従って、特
定のハロゲン原子のみがアシルオキシ基に置換されたア
シルオキシ脂肪族炭化水素の選択性90%以上と非常に
高く、収率も91%と良好である。
(The reaction scale is the same as in Example 1.) Here, as determined by gas chromatography, [Effects of the Invention] According to the present invention, one of the halogenated hydrocarbons having two different types of halogen atoms Only atoms can be selectively substituted with acyloxy groups. Therefore, the selectivity for acyloxyaliphatic hydrocarbons in which only specific halogen atoms are substituted with acyloxy groups is very high at 90% or more, and the yield is also as good as 91%.

また、反応後、水を加えて塩を溶解させるという手法に
より極めて容易に後処理をすることができる。
Further, after the reaction, post-treatment can be carried out extremely easily by adding water to dissolve the salt.

従って、本発明は副反応による生成物が少なく、しかも
分離、精製が極めて容易に実施できることから、工業的
に極めて優れた方法と言うことが出来る。
Therefore, the present invention can be said to be an extremely excellent method industrially because it produces fewer products due to side reactions and can be separated and purified very easily.

Claims (1)

【特許請求の範囲】 一般式( I ) X1−A−X2( I ) (ただし、X1およびX2は相異なるハロゲン原子であ
り、Aはアルキレン基である) で示されるジハロゲン化炭化水素と、 一般式(II) RCOOM(II) (ただし、Rはアルキル基であり、Mはアルカリ金属で
ある。) で示される脂肪族カルボン酸のアルカリ金属塩を、 一般式(III) R′_4N^+X^−(III) (ただし、R′は炭化水素残基であり、Xはハロゲン原
子である。) で示される相間移動触媒の存在下、酢酸アルキルエステ
ル溶媒中で反応させることを特徴とする 一般式(IV) RCOO−A−X3(IV) (ただし、X3はハロゲン原子であり、Aはアルキレン
基であり、Rはアルキル基である。)で示されるアシル
オキシ脂肪族炭化水素の製造方法。
[Claims] A dihalogenated hydrocarbon represented by the general formula (I) Formula (II) RCOOM (II) (However, R is an alkyl group, M is an alkali metal.) An alkali metal salt of an aliphatic carboxylic acid represented by the general formula (III) R'_4N^+X^ -(III) (However, R' is a hydrocarbon residue and X is a halogen atom.) A general formula characterized in that the reaction is carried out in an acetic acid alkyl ester solvent in the presence of a phase transfer catalyst represented by (IV) A method for producing an acyloxyaliphatic hydrocarbon represented by RCOO-A-X3(IV) (wherein, X3 is a halogen atom, A is an alkylene group, and R is an alkyl group).
JP1328053A 1989-12-18 1989-12-18 Production of acyloxyaliphatic hydrocarbon Pending JPH03188044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1328053A JPH03188044A (en) 1989-12-18 1989-12-18 Production of acyloxyaliphatic hydrocarbon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1328053A JPH03188044A (en) 1989-12-18 1989-12-18 Production of acyloxyaliphatic hydrocarbon

Publications (1)

Publication Number Publication Date
JPH03188044A true JPH03188044A (en) 1991-08-16

Family

ID=18205984

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1328053A Pending JPH03188044A (en) 1989-12-18 1989-12-18 Production of acyloxyaliphatic hydrocarbon

Country Status (1)

Country Link
JP (1) JPH03188044A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993008152A1 (en) * 1991-10-18 1993-04-29 Ihara Chemical Industry Co., Ltd. Process for producing halomethyl ester of aliphatic carboxylic acid
WO1998014421A1 (en) * 1996-10-02 1998-04-09 Daiichi Pharmaceutical Co., Ltd. Method for esterifying carboxylic compounds
JP2010531852A (en) * 2007-07-02 2010-09-30 シンケム A new synthesis of fenofibrate
JP2016014003A (en) * 2014-07-01 2016-01-28 サミ ラブズ リミテッド Synthesis of calebin-a and its biologically active analogs

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993008152A1 (en) * 1991-10-18 1993-04-29 Ihara Chemical Industry Co., Ltd. Process for producing halomethyl ester of aliphatic carboxylic acid
US5319132A (en) * 1991-10-18 1994-06-07 Ihara Chemical Industry Co., Ltd. Process for producing halomethyl ester of aliphatic carboxylic acid
WO1998014421A1 (en) * 1996-10-02 1998-04-09 Daiichi Pharmaceutical Co., Ltd. Method for esterifying carboxylic compounds
JP2010531852A (en) * 2007-07-02 2010-09-30 シンケム A new synthesis of fenofibrate
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