JPH01265051A - Production of diaryloxyalkane - Google Patents

Production of diaryloxyalkane

Info

Publication number
JPH01265051A
JPH01265051A JP63092055A JP9205588A JPH01265051A JP H01265051 A JPH01265051 A JP H01265051A JP 63092055 A JP63092055 A JP 63092055A JP 9205588 A JP9205588 A JP 9205588A JP H01265051 A JPH01265051 A JP H01265051A
Authority
JP
Japan
Prior art keywords
chloride
mol
water
aromatic alcohol
phenol
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
JP63092055A
Other languages
Japanese (ja)
Inventor
Masato Satomura
里村 正人
Ken Iwakura
岩倉 謙
Masanobu Takashima
正伸 高島
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP63092055A priority Critical patent/JPH01265051A/en
Publication of JPH01265051A publication Critical patent/JPH01265051A/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

Landscapes

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

Abstract

PURPOSE:To obtain a low-cost diaryloxyalkane to be readily purified, useful as a thermoplastic substance for recording materials in high yield, by reacting an aryloxyalkyl halide with an aromatic alcohol in the presence of a phase transfer catalyst. CONSTITUTION:An aryloxyalkyl halide such as 2-phenoxyethyl chloride shown by formula I [Ar is (substituted) phenyl or naphthyl; X is halogen, preferably Cl or Br; n is 2-10] is reacted with an aromatic alcohol such as phenol in water or a mixture of water and an organic solvent in the presence of a phase transfer catalyst such as quaternary ammonium shown by formula II [R1-R4 are alkyl or aryl; X is inorganic acid residue or organic acid residue such as Cl, Br, I or OSO2R (R is OH or aryl)], e.g., tetra-n-butylammonium bromide, preferably in the coexistence of a base such as caustic soda at 40-120 deg.C to give the aimed compound such as 1,2-diphenoxyethane.

Description

【発明の詳細な説明】 (発明の分野) 本発明は記録オ料用の熱可融性物質として有用なジアリ
ールオキシアルカンの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention This invention relates to a method for producing diaryloxyalkanes useful as thermofusible materials for recording materials.

(従来技術) ジアリールオキシアルカンの製造方法としては従来より
、1)アリールオキシアルコールの活性エステルとフェ
ノールを反応させる方法、2)アルキレンジオールのジ
活性エステルとフェノールを反応させる方法、3)アリ
ールオキシアルキルハライドとフェノールを塩基存在下
に反応させる方法、4)ウィリアムソン法等がしられて
おり。
(Prior Art) Conventional methods for producing diaryloxyalkanes include 1) a method of reacting an active ester of an aryloxyalcohol with phenol, 2) a method of reacting a diactive ester of an alkylene diol with phenol, and 3) a method of reacting an aryloxyalkyl A method of reacting a halide and phenol in the presence of a base, 4) Williamson method, etc. are known.

特開昭62−281836号、特公昭51−33542
号等に開示されている。しかしながらこれらの方法では
、収率が低かったり、ハンドリングの点、コストの点、
安全性の点などで問題があった。
JP 62-281836, JP 51-33542
Disclosed in the issue etc. However, these methods have low yields, handling issues, cost issues,
There were problems with safety and other issues.

(発明の目的) 本発明の目的は高収率で、しかも精製が容易でかつ低コ
ストなジアリールオキシアルカンの製造方法を提供する
ことである。
(Objective of the Invention) An object of the present invention is to provide a method for producing diaryloxyalkanes with high yield, easy purification, and low cost.

(発明の構成) 本発明の目的は、アリールオキシアルキルハライドと芳
香族アルコールを相間移動触媒の存在下で反応させるこ
とを特徴とするジアリールオキシアルカンの製造方法を
開発することにより達成された。
(Structure of the Invention) The object of the present invention was achieved by developing a method for producing diaryloxyalkanes, which is characterized by reacting an aryloxyalkyl halide and an aromatic alcohol in the presence of a phase transfer catalyst.

本発明に係わるアリールオキシアルキルハライドは下記
一般式(1)で表されるものを言う。
The aryloxyalkyl halide according to the present invention is represented by the following general formula (1).

Ar0CI、H2,IX     (I)上式中、Ar
は置換基を有していても良いフェニル基又はナフチル基
を、Xはハロゲン原子、好ましくは塩素原子又は臭素原
子を、nは2〜10の整数を表す。
Ar0CI, H2, IX (I) In the above formula, Ar
represents a phenyl group or a naphthyl group which may have a substituent, X represents a halogen atom, preferably a chlorine atom or a bromine atom, and n represents an integer of 2 to 10.

Arの置換基の例としてはアルキル基、アルコキシ基、
ハロゲン原子、ニトロ基、シアノ基、アシル基、フェニ
ル基1等があげられる。
Examples of substituents for Ar include alkyl groups, alkoxy groups,
Examples include a halogen atom, a nitro group, a cyano group, an acyl group, and a phenyl group.

具体的な例としては、2−フェノキシエチルクロリド、
3−フェノキシプロビルクロリド、4−フェノキシブチ
ルクロリド、6−フェノキシエチルクロリド、10−フ
ェノキシデシルクロリド。
Specific examples include 2-phenoxyethyl chloride,
3-phenoxypropyl chloride, 4-phenoxybutyl chloride, 6-phenoxyethyl chloride, 10-phenoxydecyl chloride.

2−P−メチルフェノキシエチルクロリド、2−P−エ
チルフェノキシエチルクロリド、2−P−メトキシフェ
ノキシエチルクロリド、2−P−エトキシフェノキシエ
チルクロリド、2−p−クロロフェノキシエチルクロリ
ド、2−m−メチルフェノキシエチルクロリド、2−0
−メチルフェノキシエチルクロリド、2−β−ナフチル
オキンエチルクロリド、2−β−ナフチルオキシプロピ
ルクロリド、3−β−ナフチルオキシプロピル−2−ク
ロリド1等が挙げられる。これらのなかでも特に、β−
アリールオキシエチルクロリドとくに。
2-P-methylphenoxyethyl chloride, 2-P-ethylphenoxyethyl chloride, 2-P-methoxyphenoxyethyl chloride, 2-P-ethoxyphenoxyethyl chloride, 2-p-chlorophenoxyethyl chloride, 2-m-methyl Phenoxyethyl chloride, 2-0
-methylphenoxyethyl chloride, 2-β-naphthyloxyneethyl chloride, 2-β-naphthyloxypropyl chloride, 3-β-naphthyloxypropyl-2-chloride 1, and the like. Among these, β-
Especially aryloxyethyl chloride.

原料の人手のしやすさから、2−フェノキシエチルクロ
リドが好ましい。
2-phenoxyethyl chloride is preferred from the viewpoint of easy handling of raw materials.

本発明に係わる製造方法では、Xが反応性の低い塩素原
子の場合でも反応が円滑に進行するという利点がある。
The production method according to the present invention has the advantage that the reaction proceeds smoothly even when X is a chlorine atom with low reactivity.

本発明に係わる芳香族アルコールは、低級アルキル基、
低級アルコキシ基、ハロゲン原子などの置換基を有して
いてもよい、フェノール又はナフトール誘導体を言い、
具体的にはフェノール、p。
The aromatic alcohol according to the present invention includes a lower alkyl group,
Refers to a phenol or naphthol derivative that may have a substituent such as a lower alkoxy group or a halogen atom,
Specifically, phenol, p.

m、又は0−クレゾール、p、m、又は0−エチルフェ
ノール、p、m又は 0−プロピルフェノール、p、m
、又は0−メトキシフェノール、p。
m, or 0-cresol, p, m, or 0-ethylphenol, p, m, or 0-propylphenol, p, m
, or 0-methoxyphenol, p.

m、又はQ−エトキシフェノール、p、m、又は0−ク
ロロフェノール、α−ナフトール、β−ナフトールなど
があげられる。
Examples include m- or Q-ethoxyphenol, p-, m- or 0-chlorophenol, α-naphthol, β-naphthol, and the like.

本発明に係わる相間移動触媒としては、4級アンモニウ
ム塩、ポリアルキレングリコール、クラウンエーテルな
どがあげられるが、この中で特に。
Examples of the phase transfer catalyst according to the present invention include quaternary ammonium salts, polyalkylene glycols, crown ethers, etc. Among these, in particular.

下記一般式(II)で表される4級アンモニウム塩が好
ましい。
A quaternary ammonium salt represented by the following general formula (II) is preferred.

上式中、R1〜R1はアルキル基又はアリール基を、X
は無機酸又は有機酸の残基9例えばCI。
In the above formula, R1 to R1 represent an alkyl group or an aryl group,
is a residue of an inorganic or organic acid 9 such as CI.

Br、r、03Oz R,(Rは○H,アリール基。Br, r, 03Oz R, (R is ○H, aryl group.

0NRI  R2Ri R−を表す、)などの酸基を表
す。
0NRI R2Ri R- represents an acid group such as ).

4級アンモニウム塩の具体的な例としては、臭化テトラ
メチルアンモニウム、臭化テトラエチルアンモニウム、
臭化テトラ−n−ブチルアンモニウム、臭化テトラ−n
−オクチルアンモニウム。
Specific examples of quaternary ammonium salts include tetramethylammonium bromide, tetraethylammonium bromide,
Tetra-n-butylammonium bromide, Tetra-n bromide
-Octylammonium.

塩化テトラ−n−ブチルアンモニウム、塩化テトラエチ
ルアンモニウム、塩化トリエチルベンジルアンモニウム
、臭化トリエチルベンジルアンモニウム、塩化トリオク
チルベンジルアンモニウム。
Tetra-n-butylammonium chloride, tetraethylammonium chloride, triethylbenzylammonium chloride, triethylbenzylammonium bromide, trioctylbenzylammonium chloride.

臭化トリオクチルベンジルアンモニウム、塩化トリブチ
ルベンジルアンモニウム、臭化トリフチルベンジルアン
モニウム、塩化N−ラウリルピリジニウム、水酸化テト
ラエチルアンモニウム、水酸化トリエチルベンジルアン
モニウム、臭化トリメチルフェニルアンモニウム、テト
ラ−n−ブチルアンモニウムハイドロジエンサルフェー
ト、N−ペンジルピコリウムクロライド、ヨウ化テトラ
エチルアンモニウム、ヨウ化テトラ−n−ブチルアンモ
ニウム、N−ラウリル−4−ピコリニウムクロリド等が
あげられる。
trioctylbenzylammonium bromide, tributylbenzylammonium chloride, triphthylbenzylammonium bromide, N-laurylpyridinium chloride, tetraethylammonium hydroxide, triethylbenzylammonium hydroxide, trimethylphenylammonium bromide, tetra-n-butylammonium hydrodiene Sulfate, N-pendylpicolium chloride, tetraethylammonium iodide, tetra-n-butylammonium iodide, N-lauryl-4-picolinium chloride, and the like.

4級アンモニウム塩の使用量はアリ−レオキンアルキル
ハライド1モルに対して0.01〜3モルが好ましく、
特に0.1〜1モルが好ましい。
The amount of quaternary ammonium salt used is preferably 0.01 to 3 mol per 1 mol of aryleoquine alkyl halide,
Particularly preferred is 0.1 to 1 mol.

アリールオキシアルキルハライドと芳香族アルコールの
使用量は、アリールオキシアルキル7%ライド1モルに
対して、芳香族アルコール0.5〜2モルが好ましく、
特に0.9〜1.2モ′ルが好ましい。
The amount of aryloxyalkyl halide and aromatic alcohol used is preferably 0.5 to 2 mol of aromatic alcohol per 1 mol of aryloxyalkyl 7% ride.
Particularly preferred is 0.9 to 1.2 mol.

本発明の製造方法を実施する際の反応温度は40〜12
0°Cが好ましく、特に60〜100゜Cが好ましい、
130°C以上だと副反応が生じやすく、高純度の生成
物を得にくい。
The reaction temperature when carrying out the production method of the present invention is 40 to 12
0°C is preferred, particularly 60 to 100°C.
If the temperature is 130°C or higher, side reactions are likely to occur, making it difficult to obtain a highly pure product.

本発明の製造方法を実施する際には、水、水と有機溶媒
の混合物または有機溶媒中で行うことができるが、特に
4級アンモニウム塩の溶鯉性及びコストの点から水、又
は水と有機溶媒の混合物中で行うことがこのましい。
When carrying out the production method of the present invention, it can be carried out in water, a mixture of water and an organic solvent, or an organic solvent. Preferably, the reaction is carried out in a mixture of organic solvents.

本発明の製造方法を実施する際には、塩基を併用するこ
とが好ましく、塩基としてはナトリウム化合物、または
カリウム化合物が好ましい。
When carrying out the production method of the present invention, it is preferable to use a base in combination, and the base is preferably a sodium compound or a potassium compound.

塩基の具体例としては、苛性ソーダ、苛性カリ。Specific examples of bases include caustic soda and caustic potash.

炭酸ソーダ、炭酸カリ等があげられる。この中で特に苛
性ソーダ、苛性カリが好ましい。
Examples include carbonated soda and carbonated potassium. Among these, caustic soda and caustic potash are particularly preferred.

使用する塩基の中は芳香族アルコール1モルに対して1
〜3モルが好ましく、特に1〜2モルが好ましい。
The base used is 1 mole of aromatic alcohol.
-3 mol is preferable, and 1-2 mol is especially preferable.

不発明の製造方法を実施する際には、ハンドリングの点
から仕込み時の固形分濃度が50%以下であることが好
ましい。
When implementing the uninvented manufacturing method, it is preferable that the solid content concentration at the time of preparation is 50% or less from the viewpoint of handling.

また不活性ガスの=囲気下に反応を行うことも。The reaction can also be carried out under an atmosphere of inert gas.

生成物の着色防止の点から好ましい。This is preferable from the viewpoint of preventing coloring of the product.

本発明に係わる製造方法は収率が極めて良好な上、生成
物の着色が少なく、かつハンドリングが容易であること
などすぐれた点が多い。
The production method according to the present invention has many advantages such as a very good yield, less coloring of the product, and ease of handling.

(発明の実施例) 以下実施例により本発明を具体的に説明するが。(Example of the invention) The present invention will be specifically explained below with reference to Examples.

本発明は実施例に限定されるものではない。The invention is not limited to the examples.

実施例1 1.2−ジフェノキシエタン かきまぜ機のついた三つロフラスコに、2−フェノキン
エチルクロリド1.0モル、フェノール1.0モル、苛
性ソーダ2.0モル、臭化fト5− n −ブチルアン
モニウム0.3モルlkloOmlを秤りとる。かきま
ぜなから80’Cで3時間反応させた9反応混合物を水
にあけ、析出した結晶をろ取し、さらに水およびメタノ
ール水で洗浄し目的物を得た。収率98%、融点98°
C比較例1 かきまぜ機のついた三つロフラスコに、2−フェノキシ
エチルクロリド1.0モル、フェノール1、Q%ル、前
件ソーダ2.Q%ル、水100m1を秤りとり、かきま
ぜなから80’Cで3時間反応させた。実施例1と同様
に後処理して目的物を得た。収$=30%、融点96〜
98°C比較例2 かきまぜ機のついた三つロフラスコに、2−フェノキシ
エチルトシレート1.0モル、フェノール1.0モル、
苛性ソーダ2.0モル、水100m1を秤りとり、かき
まぜながら80°Cで3時間反応させた。実施例1と同
様に後処理して目的物を得た。収率90%、融点98°
C 実施例2 ■−フェノキンー2−p−エチルフェノキシエタン かきまぜ機のついた三つロフラスコに、2−フェノキン
エチルクロリド1.0モル、p−エチルフェノール1.
0モル、苛性ソータ2 、  [1モル。
Example 1 1.2-Diphenoxyethane In a three-neck flask equipped with a stirrer, 1.0 mol of 2-phenoquinethyl chloride, 1.0 mol of phenol, 2.0 mol of caustic soda, and 5-n bromide were added. - Weigh out 0.3 mol lkloOml of butylammonium. 9. The reaction mixture was reacted at 80'C for 3 hours without stirring and poured into water, and the precipitated crystals were collected by filtration and further washed with water and methanol to obtain the desired product. Yield 98%, melting point 98°
C Comparative Example 1 In a three-necked flask equipped with a stirrer, 1.0 mol of 2-phenoxyethyl chloride, 1 mol of phenol, 1.0 mol of phenol, 2. 100 ml of water was weighed out and reacted at 80'C for 3 hours without stirring. The desired product was obtained by post-treatment in the same manner as in Example 1. Yield: $30%, melting point: 96~
98°C Comparative Example 2 In a three-neck flask equipped with a stirrer, 1.0 mol of 2-phenoxyethyl tosylate, 1.0 mol of phenol,
2.0 mol of caustic soda and 100 ml of water were weighed out and reacted at 80°C for 3 hours while stirring. The desired product was obtained by post-treatment in the same manner as in Example 1. Yield 90%, melting point 98°
C Example 2 ■-Fenoquine-2-p-ethylphenoxyethane In a three-necked flask equipped with a stirrer, 1.0 mol of 2-phenoquine ethyl chloride and 1.0 mol of p-ethylphenol were added.
0 mol, caustic sorter 2, [1 mol.

A化テトラ−n−ブチルアンモニウム0.3モル。Tetra-n-butylammonium A 0.3 mol.

水100m1を秤りとり、かきまぜながら80’Cで3
時間反応させた、実施例1と同様に後処理して目的物を
得た。収率96%、融点106°C実施例3 ■、2−ジーm−メチルフェノキ/エタンかきまぜ機の
ついた三つロフラスコに、2−m−メチルフェノキシエ
チルクロリド1.0モル。
Weigh out 100ml of water and heat it to 80'C while stirring.
The desired product was obtained by post-treatment in the same manner as in Example 1, in which the reaction was carried out for a period of time. Yield 96%, melting point 106 DEG C. Example 3 (1) 1.0 mol of 2-m-methylphenoxyethyl chloride was placed in a three-necked flask equipped with a 2-di-m-methylphenoxy/ethane stirrer.

m−メチルフェノール1.0モル、苛性ソーダ2゜0モ
ル、臭化テトラ−n−ブチルアンモニウム0゜3モル、
水100m1を秤りとり、かきまぜながら90°Cで3
時間反応させた。実施例1と同様に後処理して目的物を
得た。収率95%、融点98°C 実施例4〜9 実施例1と同様にして以下の芳香族アルコールを反応さ
せた。
1.0 mol of m-methylphenol, 2.0 mol of caustic soda, 0.3 mol of tetra-n-butylammonium bromide,
Weigh out 100ml of water and heat it to 90°C while stirring.
Allowed time to react. The desired product was obtained by post-treatment in the same manner as in Example 1. Yield 95%, melting point 98°C Examples 4 to 9 The following aromatic alcohols were reacted in the same manner as in Example 1.

実施例4 4−クレゾール X絶倒5  4−イソプロピルフェノール実M例6  
3.4−ジメチルフェノール実施例7 4−フロロフェ
ノール 実施例8 4−クロロフェノール 実施例9 4−メトキンフェノール 実施例1と同様に後処理して 1i例4 1−フェノキン−2−p−メチルフェノキン
エタン(融点100°C)、実施例51−フェノキシ−
2−p−イソプロピルフェノキシエタン(融点 95°
C)、実施例61−フニノキン−2(3,4−ジメチル
フェノキシ)エタン(融点100°C)、 実施例71
−フェノキシ−2−p−フロロフェノキシエタン(融点
 90°C)、実施例81−フェノキン−2−p−クロ
ロフェノキシエタン(融点101°C)、実施例91−
フェノキシ−2−p−メトキシフェノキンエタン(融点
102°C)を得た。いずれも収率は90%以上だった
Example 4 4-Cresol
3. 4-Dimethylphenol Example 7 4-Fluorophenol Example 8 4-Chlorophenol Example 9 4-Methoquinphenol After treatment in the same manner as Example 1, 1i Example 4 1-phenoquine-2-p-methyl Phenoquinethane (melting point 100°C), Example 51-phenoxy-
2-p-isopropylphenoxyethane (melting point 95°
C), Example 61-funinoquine-2(3,4-dimethylphenoxy)ethane (melting point 100°C), Example 71
-Phenoxy-2-p-chlorophenoxyethane (melting point 90°C), Example 81-phenoquine-2-p-chlorophenoxyethane (melting point 101°C), Example 91-
Phenoxy-2-p-methoxyphenoquinethane (melting point 102°C) was obtained. In all cases, the yield was over 90%.

Claims (1)

【特許請求の範囲】[Claims] アリールオキシアルキルハライドと芳香族アルコールを
相間移動触媒の存在下で反応させることを特徴とするジ
アリールオキシアルカンの製造方法
A method for producing a diaryloxyalkane, which comprises reacting an aryloxyalkyl halide and an aromatic alcohol in the presence of a phase transfer catalyst.
JP63092055A 1988-04-14 1988-04-14 Production of diaryloxyalkane Pending JPH01265051A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63092055A JPH01265051A (en) 1988-04-14 1988-04-14 Production of diaryloxyalkane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63092055A JPH01265051A (en) 1988-04-14 1988-04-14 Production of diaryloxyalkane

Publications (1)

Publication Number Publication Date
JPH01265051A true JPH01265051A (en) 1989-10-23

Family

ID=14043817

Family Applications (1)

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JP63092055A Pending JPH01265051A (en) 1988-04-14 1988-04-14 Production of diaryloxyalkane

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002090351A1 (en) * 1999-11-24 2002-11-14 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivative
EP1311485A1 (en) * 2000-08-14 2003-05-21 Teva Pharmaceutical Industries Ltd. Processes for preparing cilostazol
US6630590B1 (en) 1999-11-24 2003-10-07 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives
WO2004024716A1 (en) * 2002-09-10 2004-03-25 Otsuka Pharmaceutical Co., Ltd. Process for producing cilostazol
US7399864B2 (en) 2001-05-02 2008-07-15 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives
US7825251B2 (en) 2001-05-02 2010-11-02 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002090351A1 (en) * 1999-11-24 2002-11-14 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivative
US6630590B1 (en) 1999-11-24 2003-10-07 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives
EP1311485A1 (en) * 2000-08-14 2003-05-21 Teva Pharmaceutical Industries Ltd. Processes for preparing cilostazol
EP1311485A4 (en) * 2000-08-14 2004-05-12 Teva Pharma Processes for preparing cilostazol
US7399864B2 (en) 2001-05-02 2008-07-15 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives
US7825251B2 (en) 2001-05-02 2010-11-02 Otsuka Pharmaceutical Co., Ltd. Process for producing carbostyril derivatives
WO2004024716A1 (en) * 2002-09-10 2004-03-25 Otsuka Pharmaceutical Co., Ltd. Process for producing cilostazol
US7026486B2 (en) 2002-09-10 2006-04-11 Otsuka Pharmaceutical Co., Ltd. Process for production cilostazol

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