JPH0641435B2 - Method for producing diphenyl ether dicarboxylic acid - Google Patents

Method for producing diphenyl ether dicarboxylic acid

Info

Publication number
JPH0641435B2
JPH0641435B2 JP60279907A JP27990785A JPH0641435B2 JP H0641435 B2 JPH0641435 B2 JP H0641435B2 JP 60279907 A JP60279907 A JP 60279907A JP 27990785 A JP27990785 A JP 27990785A JP H0641435 B2 JPH0641435 B2 JP H0641435B2
Authority
JP
Japan
Prior art keywords
formula
diphenyl ether
acid
dicarboxylic acid
cooh
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
JP60279907A
Other languages
Japanese (ja)
Other versions
JPS62138449A (en
Inventor
寛 平井
正一 馬場
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals 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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP60279907A priority Critical patent/JPH0641435B2/en
Publication of JPS62138449A publication Critical patent/JPS62138449A/en
Publication of JPH0641435B2 publication Critical patent/JPH0641435B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

Description

【発明の詳細な説明】 産業上の利用分野 本発明はジフエニルエーテル−3,3′−または3,
4′−ジカルボン酸の製造方法に関する。
The present invention relates to diphenyl ether-3,3'- or 3,
It relates to a method for producing 4'-dicarboxylic acid.

これらのジフエニルエーテルジカルジボン酸類は、いず
れも耐熱性の高分子原料などとして有用な化合物であ
り、経済的な工業的製造法の出現が望まれていた。
All of these diphenyl ether dicardibonic acids are useful compounds as heat-resistant polymer raw materials, and the advent of an economical industrial production method has been desired.

従来の技術 これらの化合物の製造法としては従来、クレゾールのア
ルカリ金属塩とハロゲン化トルエンとを銅触媒の存在下
に縮合させてジメチルジフエニルエーテルを得、次にこ
れを過マンガン酸塩や重クロム酸塩などの化学薬品によ
り酸化するか、あるいは触媒存在下に分子状酸素によっ
て酸化してジフエニルエーテルジカルボン酸とする方法
が知られている。
Conventionally, the conventional method for producing these compounds is to condense an alkali metal salt of cresol and a halogenated toluene in the presence of a copper catalyst to obtain dimethyldiphenyl ether, which is then added to permanganate or a heavy salt. There is known a method of oxidizing with a chemical agent such as chromate, or with molecular oxygen in the presence of a catalyst to give a diphenyl ether dicarboxylic acid.

しかし、化学薬品による酸化の場合は、過マンガン酸塩
や重クロム酸塩などを大量に必要とするのみならず、反
応後の廃物の大量の処理が必要になり、工業的に有利な
方法とは言いがたい。また酸素酸化による方法も触媒の
回収使用の繁雑さ、設備の複雑さ、原料中の不純物によ
る酸化の妨害、爆発の危険性などの問題があり、これも
工業化に適した方法とは称しがたい。
However, in the case of oxidation by chemicals, not only a large amount of permanganate or dichromate is required, but also a large amount of waste materials after the reaction are required, which is an industrially advantageous method. Is hard to say. In addition, the method using oxygen oxidation has problems such as complexity of catalyst recovery and use, complexity of equipment, interference of oxidation by impurities in raw materials, and risk of explosion, and it is difficult to call this method suitable for industrialization. .

これらの観点に立てば、このような芳香族カルボン酸誘
導体同志を縮合させて一挙に目的物のジフエニルエーテ
ルジカルボン酸を合成する方法が最も好ましい方法であ
ることは容易に理解できるが、現在までこの一段階方法
は全く知られていない。
From these viewpoints, it is easy to understand that the method of condensing such aromatic carboxylic acid derivatives and synthesizing the desired diphenyl ether dicarboxylic acid at once is the most preferable method. No one-step method is known.

特開昭48−61443号公報には、具体例としてm−
オキシ安息香酸ナトリウムやm−オキシ安息香酸メチル
エステルと、ブロムベンゼンとを銅粉触媒及び炭酸カリ
の存在下、加熱反応させてm−フエノキシ安息香酸やm
−フエノキシ安息香酸メチルエステルを得る方法が記載
されているが、目的生成物の収率は夫々45%、75%
と低い。
In Japanese Patent Laid-Open No. 48-61443, m-
Sodium oxybenzoate or m-oxybenzoic acid methyl ester and brombenzene are reacted by heating in the presence of a copper powder catalyst and potassium carbonate to give m-phenoxybenzoic acid or m.
-A method for obtaining phenoxybenzoic acid methyl ester is described, but the yields of the desired product are 45% and 75%, respectively.
And low.

すなわち該方法では、モノカルボン酸がエステル化され
たm−オキシ安息香酸メチルを用いた場合はまだしも、
安息香酸ナトリウム塩を用いた場合、高価なブロムベン
ゼンを過剰量使用して反応させているにもかかわらず、
得られる目的生成物は工業的製法としては満足できる収
率ではない。
That is, in the method, when using methyl m-oxybenzoate in which monocarboxylic acid is esterified,
When using benzoic acid sodium salt, despite using expensive brombenzene in excess,
The desired product obtained is not in a satisfactory yield as an industrial process.

これらのことより、本発明方法に用いる原料のように、
両者にカルボン酸基を有する化合物同志の縮合は、さら
に収率低下が予想され、そのため一段法の提案はなされ
ていないものと推定できる。
From these, like the raw materials used in the method of the present invention,
Condensation of compounds having a carboxylic acid group on both sides is expected to further reduce the yield, so it can be presumed that the one-step method has not been proposed.

問題を解決するための手段 本発明者らは、ジフエニルエーテル−3,3′−および
3,4′−ジカルボン酸の工業的製造法を鋭意検討し本
発明に達した。
Means for Solving the Problems The present inventors have earnestly studied the industrial production method of diphenyl ether-3,3′- and 3,4′-dicarboxylic acid and arrived at the present invention.

すなわち本発明は式(I) 〔式中、−COOHは水酸基に対し3または4位。〕で示さ
れるm−またはp−ヒドロシキ安息香酸と、式(II) 〔式中、XはBrまたはClを表わし、−COOHはXに対し3
または4位。〕 で示されるm−またはp−ハロゲン化安息香酸とを、8
−キノリノール銅錯体触媒の存在下、アルカリ金属炭酸
塩またはアルカリ金属水酸化物を、式(I)と式(II)化合
物の水酸基及びカルボン酸基に対し0.3〜2.0当量用い、
非プロトン極性溶媒及びその際好ましくは式(IV)で示さ
れるアルキレングルコール 式中、R、R′は水素原子、メチルまたはエチル基であ
り、nは0〜10の整数〕 を併用して加熱反応させることを特徴とする式 〔式中、−COOHは3,3′または3,4′位。〕 で示される、ジフエニルエーテル−3,3′ジカルボン
酸またはジフエニルエーテル−3,4′ジカルボン酸の
製造方法である。
That is, the present invention has the formula (I) [In formula, -COOH is a 3 or 4 position with respect to a hydroxyl group. And m- or p-hydroxybenzoic acid represented by the formula (II) [In the formula, X represents Br or Cl, and -COOH is 3 with respect to X.
Or 4th place. ] The m- or p-halogenated benzoic acid shown by these is 8
-In the presence of a quinolinol copper complex catalyst, an alkali metal carbonate or an alkali metal hydroxide is used in an amount of 0.3 to 2.0 equivalents with respect to the hydroxyl group and carboxylic acid group of the compound of formula (I) and formula (II),
Aprotic polar solvent and alkylene glycol of the formula (IV). In the formula, R and R ′ are a hydrogen atom, a methyl or ethyl group, and n is an integer of 0 to 10], and the reaction is carried out by heating. [In the formula, -COOH is in the 3,3 'or 3,4' position. ] It is a manufacturing method of diphenyl ether-3,3 'dicarboxylic acid or diphenyl ether-3,4' dicarboxylic acid shown by these.

本発明法においては原料ハロゲン化安息香酸として高価
なブロム安息香酸を必ずしも用いなくともクロル安息香
酸を用いても収率上何ら問題はない。またこれらの安息
香酸類は、エスエル化して用いる必要もなく、ヒドロキ
シ安息香酸、ハロゲン化安息香酸ともに農薬等の中間体
として容易に安価に入手しうるものである。
In the method of the present invention, there is no problem in yield even if chlorobenzoic acid is used as the starting halogenated benzoic acid without necessarily using expensive bromobenzoic acid. Further, these benzoic acids do not need to be used after conversion into ester, and both hydroxybenzoic acid and halogenated benzoic acid can be easily and inexpensively obtained as intermediates for pesticides and the like.

本発明法においてヒドロキシ安息香酸のハロゲン化安息
香酸に対する使用割合は0.5〜2モル比が適当であり、
特に等モル比が望ましい。
In the method of the present invention, the ratio of hydroxybenzoic acid to halogenated benzoic acid is preferably 0.5 to 2 molar ratio,
An equimolar ratio is particularly desirable.

本発明においては、これらの化合物の水酸基及びカルボ
ン酸基は反応に先だち、アルカリ金属によりフエノラー
ト及びカルボン酸塩を形成した後縮合反応は進められ
る。アルカリ金属としてはカリウムまたはナトリウムが
水酸化物、炭酸塩、あるいは重炭酸塩として用いられる
が、その使用量は原料中に存在するすべてのヒドロキシ
基およびカルボン酸基の両方に対して0.3〜2.0当量、好
ましくは0.5〜1.5当量になるように添加する。特に1.0
モル比付近が好ましく、0.3当量未満、また2.0当量を越
えると収率が低下するので望ましくない。
In the present invention, the hydroxyl group and carboxylic acid group of these compounds are subjected to the condensation reaction prior to the reaction, after forming the phenolate and the carboxylate with an alkali metal. As the alkali metal, potassium or sodium is used as a hydroxide, carbonate, or bicarbonate, but the amount used is 0.3 to 2.0 equivalents for all hydroxy groups and carboxylic acid groups present in the raw material. , Preferably 0.5 to 1.5 equivalents. Especially 1.0
Around the molar ratio is preferable, and if it is less than 0.3 equivalent or exceeds 2.0 equivalents, the yield is lowered, which is not desirable.

ヒドロキシ安息香酸、ハロゲン化安息香酸のアルカリ金
属塩は、これらの安息香酸類と苛性アルカリ、炭酸アル
カリなどとをトルエンなどの共沸剤の存在または不在下
に加熱して水を留去させてつくるのが一般的な方法であ
り、本発明においても常法に従い容易に得ることができ
るが、この際生成塩類が固化して、かたまりを生じやす
い。
Alkali metal salts of hydroxybenzoic acid and halogenated benzoic acid are prepared by heating these benzoic acids and caustic alkali, alkali carbonate, etc. in the presence or absence of an azeotropic agent such as toluene to distill off water. Is a general method and can be easily obtained according to a conventional method also in the present invention, but at this time, the produced salt is solidified and easily agglomerates.

したがって本発明の好ましい態様としては、反応器に必
要量のアルカリ金属の炭酸塩、重炭酸塩またはアルカリ
金属水酸化物を後述の縮合反応に用いる非プロトン極性
溶媒やアルキレングリコールとともに仕込み、これを攪
拌しつつ、原料のヒドロキシ安息香酸及びハロゲン化安
息香酸を加えて、加熱下に脱水を行い、引続き所望の縮
合反応温度まで昇温して縮合反応を実施するのが望まし
い。
Therefore, in a preferred embodiment of the present invention, a reactor is charged with a necessary amount of an alkali metal carbonate, bicarbonate or alkali metal hydroxide together with an aprotic polar solvent or alkylene glycol used in the condensation reaction described below, and the mixture is stirred. On the other hand, it is desirable to add hydroxybenzoic acid and halogenated benzoic acid as raw materials, dehydrate under heating, and then raise the temperature to a desired condensation reaction temperature to carry out the condensation reaction.

本発明においては使用する銅系触媒は、8−キノリノー
ルの銅錯体として用いる必要があり、通常のジフエニル
エーテル製造に用いられている銅粉などでは反応は進行
しない。8−キノリノール銅錯体は、予め調整してから
反応に添加してもよいが、ハロゲン化銅及び8−キノリ
ノールを反応系中に添加するだけで容易に銅錯体は形成
されるので、反応系中にハロゲン化銅及び8−キノリノ
ールを夫々添加してもよい。ハロゲン化銅としては特に
塩化第一銅、臭化第一銅が適当である。その添加量は原
料ヒドロキシ安息香酸に対して0.001〜0.2モル比で
よい。また8−キノリノールの添加量はハロゲン化銅に
対して0.2〜2.5モル比の範囲が適当である。
In the present invention, the copper-based catalyst used needs to be used as a copper complex of 8-quinolinol, and the reaction does not proceed with copper powder or the like used in the usual production of diphenyl ether. The 8-quinolinol copper complex may be added to the reaction after being adjusted in advance, but since the copper complex is easily formed by adding copper halide and 8-quinolinol to the reaction system, Copper halide and 8-quinolinol may be added to the above. Particularly suitable cuprous halides are cuprous chloride and cuprous bromide. The addition amount may be 0.001 to 0.2 molar ratio with respect to the raw material hydroxybenzoic acid. Further, the amount of 8-quinolinol added is appropriately in the range of 0.2 to 2.5 molar ratio with respect to the copper halide.

本発明に使用される溶媒としては、非プロトン極性溶媒
を用いる必要があり、通常知られている有機の溶媒、特
にスルホラン、1,3−ジメチル−2−イミダゾリジノ
ン、N−メチルピロリドン、ジメチルアセトアミドなど
が好適である。またその際収率をさらに高めるため、下
記のアルキレングリコールを併用してもよい。
As the solvent used in the present invention, it is necessary to use an aprotic polar solvent, and commonly known organic solvents, particularly sulfolane, 1,3-dimethyl-2-imidazolidinone, N-methylpyrrolidone and dimethyl. Acetamide and the like are preferable. In addition, in this case, in order to further increase the yield, the following alkylene glycol may be used in combination.

アルキレングリコール類としては、一般式 (式中R,R′は水素原子、メチル基またはエチル基、
nは0〜10の整数を示す。ただしn=1のときはRは
水素原子、R′−はメチル基またはエチル基を示す。)
で表わされるもの、特にジエチレングリコール、セロソ
ルブ、ジエチレングリコールジメチルエーテル、トリエ
チレングリコールなどが有利に用いられる。
As the alkylene glycol, a general formula (In the formula, R and R'are hydrogen atom, methyl group or ethyl group,
n shows the integer of 0-10. However, when n = 1, R represents a hydrogen atom and R'- represents a methyl group or an ethyl group. )
Those represented by, particularly diethylene glycol, cellosolve, diethylene glycol dimethyl ether, triethylene glycol and the like are advantageously used.

これらの溶媒は単独で用いてもよいが、2種またはそれ
以上混合してもよく、その混合比率に特に制限はない。
非プロトン極性溶媒とアルキレングリコール溶媒を併用
する場合は、同量程度の混合比率がよい。
These solvents may be used alone, or two or more kinds may be mixed, and the mixing ratio thereof is not particularly limited.
When the aprotic polar solvent and the alkylene glycol solvent are used in combination, the mixing ratio is preferably about the same.

これらの溶媒の使用量は原料ヒドロキシ安息香酸の2〜
20重量倍が適当であり、特に5〜15重量倍が好まし
い。
The amount of these solvents used is 2 to 2 of the raw material hydroxybenzoic acid.
20 times by weight is suitable, and 5 to 15 times by weight is particularly preferable.

反応は通常120〜250℃の温度で行なわれるが、特
に150〜200℃が適当である。反応時間は反応温
度、溶媒種類、触媒量などによっても変えられるが、通
常5〜30時間である。
The reaction is usually carried out at a temperature of 120 to 250 ° C, but 150 to 200 ° C is particularly suitable. The reaction time varies depending on the reaction temperature, solvent type, amount of catalyst, etc., but is usually 5 to 30 hours.

反応後の生成物はジカルボン酸塩となっており、水に溶
解させるか、または蒸留によって溶媒を回収したのち水
に溶解して、その溶液を塩酸、硫酸などの酸で酸性にす
ればジフエニルエーテルジカルボン酸が析出する。これ
を過、水洗後乾燥すれば粗製品が得られるが、より高
純度のものを必要とする場合にはこの粗製品をメタノー
ルと加熱して不純物を溶解させて除く方法、アルカリ水
溶液に溶解して酸で析出させる方法、ジメチルホルムア
ミド等の溶媒で再結晶する方法などによって精製するこ
とができる。
The product after the reaction is a dicarboxylic acid salt, and if it is dissolved in water or the solvent is recovered by distillation and then dissolved in water and the solution is acidified with an acid such as hydrochloric acid or sulfuric acid, diphenyl Ether dicarboxylic acid precipitates. A crude product can be obtained by over-washing it with water, and then drying it.However, if a higher-purity product is required, the crude product can be heated with methanol to dissolve and remove impurities. Can be purified by an acid precipitation method, a recrystallization method with a solvent such as dimethylformamide, or the like.

以下実施例を挙げて説明する。Examples will be described below.

実施例1 攪拌装置、水分離器、温度計をつけた300m1四ツ口フ
ラスコに、m−ヒドロキシ安息香酸13.8g(0.1モ
ル)、m−クロル安息香酸15.6g(0.1モル)、炭酸
カリ(純度99.5%)20.8g(0.15モル)、1,3
−ジメチル−2−イミダゾリジノン100m1、塩化第一
銅0.4g(0.04モル)、8−キノリノール0.6g(0.
04モル)およびトルエン500m1を装入し、攪拌しな
がら加熱、沸騰下に生成水を、トルエンで共沸留去させ
ながら分離し、m−ヒドロキシ安息香酸のフエノラート
安息香酸塩及びm−クロル安息香酸塩を生成させた。次
いでトルエンを留去後、さらに加熱し170℃で20時
間保温攪拌し反応を終了した。
Example 1 In a 300 ml four-necked flask equipped with a stirrer, a water separator, and a thermometer, 13.8 g (0.1 mol) of m-hydroxybenzoic acid and 15.6 g (0.1 mol of m-chlorobenzoic acid) were added. ), Potassium carbonate (purity 99.5%) 20.8 g (0.15 mol), 1,3
-Dimethyl-2-imidazolidinone 100 m1, cuprous chloride 0.4 g (0.04 mol), 8-quinolinol 0.6 g (0.0.
(04 mol) and 500 ml of toluene, and the mixture is heated with stirring, and the produced water is separated by azeotropic distillation with toluene under boiling. A salt was formed. Then, after the toluene was distilled off, it was further heated and agitated while maintaining the temperature at 170 ° C. for 20 hours to complete the reaction.

反応液から1,3−ジメチル−2−イミダゾリジノンを
減圧下に留去し、残分を水に溶解して不溶物を別し、
得られた水溶液を濃塩酸で酸性とし、析出する結晶を
過、水洗、乾燥し、ジフエニルエーテル−3,3′−ジ
カルボン酸を収量18.1g(収率70.2%)で得た。m
p247〜251℃。
1,3-dimethyl-2-imidazolidinone was distilled off from the reaction solution under reduced pressure, the residue was dissolved in water to separate insoluble matter,
The obtained aqueous solution was acidified with concentrated hydrochloric acid, and the precipitated crystals were filtered, washed with water and dried to obtain 18.1 g (yield 70.2%) of diphenyl ether-3,3'-dicarboxylic acid. m
p247-251 ° C.

実施例2〜5 実施例1と同様にして、溶媒にスルホラン、N−メチル
−2−ピロリドン、ジエチレングリコール、およびスル
ホランとジエチレングリコールの混合溶媒(混合物1:
1)を夫々用いた場合の結果を表−1に示す。
Examples 2 to 5 As in Example 1, sulfolane, N-methyl-2-pyrrolidone, diethylene glycol, and a mixed solvent of sulfolane and diethylene glycol (mixture 1:
Table 1 shows the results when each of 1) was used.

実施例6 実施例1と同様の反応装置にm−ヒドロキシ安息香酸1
3.8g(0.1モル)、p−クロル安息香酸15.6g(0.
1モル)、炭酸カリ(99.5%)20.8g(0.15モ
ル)、スルホラン100m1、塩化第一銅0.4g(0.04
モル)、8−キノリノール0.6g(0.04モル)および
トルエン50m1を装入し、以下実施例1と同様に操作し
てジフエニルエーテル3,4′−ジカルボン酸を収量2
3.2g(収率90%)で得た。mp283〜286℃。
Example 6 m-Hydroxybenzoic acid 1 was added to the same reactor as in Example 1.
3.8 g (0.1 mol), p-chlorobenzoic acid 15.6 g (0.1 mol).
1 mol), potassium carbonate (99.5%) 20.8 g (0.15 mol), sulfolane 100 m1, cuprous chloride 0.4 g (0.04)
Mol), 0.6 g (0.04 mol) of 8-quinolinol and 50 ml of toluene, and the same procedure as in Example 1 was followed to obtain diphenyl ether 3,4'-dicarboxylic acid in a yield of 2
Obtained in 3.2 g (yield 90%). mp 283-286 ° C.

実施例7 実施例1と同様の反応装置にp−オキシ安息香酸13.8
g(0.1モル)、m−クロル安息香酸15.6g(0.1モ
ル)、炭酸カリ(99.5%)20.8g(0.15モル)、
スルホラン100m1、塩化第一銅0.4g(0.04モ
ル)、8−キノリノール0.6g(0.04、モル)および
トルエン50m1を装入し、反応温度を190℃、反応時
間を30時間とした以外は実施例1と同様に操作してジ
フエニルエーテル3,4′−ジカルボン酸粗製品を収量
12.9g(収率50%)を得た。
Example 7 A reactor similar to that in Example 1 was charged with 13.8 p-oxybenzoic acid.
g (0.1 mol), m-chlorobenzoic acid 15.6 g (0.1 mol), potassium carbonate (99.5%) 20.8 g (0.15 mol),
100 ml of sulfolane, 0.4 g (0.04 mol) of cuprous chloride, 0.6 g (0.04, mol) of 8-quinolinol and 50 ml of toluene were charged, the reaction temperature was 190 ° C., and the reaction time was 30 hours. The same procedure as in Example 1 was carried out except that the yield was 12.9 g (yield 50%) of a crude product of diphenyl ether 3,4'-dicarboxylic acid.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】式(I) 〔式中、−COOHは水酸基に対し3または4位〕で示され
るm−またはp−ヒドロキシ安息香酸と、式(II) 〔式中、XはBr、またはClを表わし、−COOHはXに対し
3または4位。〕 で示されるm−またはp−ハロゲン化安息香酸とを、8
−キノリノール銅錯体触媒の存在下、アルカリ金属炭酸
塩またはアルカリ金属水酸化物を、式(I)と式(II)化合
物の水酸基及びカルボン酸基に対し0.3〜2.0当量用
い、非プロトン極性溶媒中で加熱反応させることを特徴
とする式(III) 〔式中、−COOHは3,3′または3,4′位。〕で示さ
れる、ジフエニルエーテル−3,3′ジカルボン酸また
はジフエニルエーテル−3,4′ジカルボン酸の製造方
法。
1. A formula (I) [In the formula, -COOH is at the 3 or 4 position relative to the hydroxyl group] and m- or p-hydroxybenzoic acid represented by the formula (II) [In the formula, X represents Br or Cl, and -COOH is at the 3 or 4 position with respect to X. ] The m- or p-halogenated benzoic acid shown by these is 8
-In the presence of a quinolinol copper complex catalyst, an alkali metal carbonate or an alkali metal hydroxide is used in an amount of 0.3 to 2.0 equivalents based on the hydroxyl group and carboxylic acid group of the compounds of formula (I) and formula (II). Formula (III) characterized by heating reaction in a polar polar solvent [In the formula, -COOH is in the 3,3 'or 3,4' position. ] The manufacturing method of diphenyl ether-3,3 'dicarboxylic acid or diphenyl ether-3,4' dicarboxylic acid shown by these.
【請求項2】式(I) 〔式中、−COOHは水酸基に対し3または4位〕で示され
るm−またはp−ヒドロキシ安息香酸と、式(II) 〔式中、XはBr、またはClを表わし、−COOHはXに対し
3または4位。〕 で示されるm−またはp−ハロゲン化安息香酸とを、8
−キノリノール銅錯体触媒の存在下、アルカリ金属炭酸
塩またはアルカリ金属水酸化物を、式(I)と式(II)化合
物の水酸基及びカルボン酸基に対し0.3〜2.0当量用
い、非プロトン極性溶媒及び式(IV)で示されるアルキレ
ングリコール 〔式中、R、R′は水素原子、メチルまたはエチル基で
あり、nは0〜10の整数〕 溶媒中で加熱反応させることを特徴とする式 (III) 〔式中、−COOHは3,3′または3,4′位。)で示さ
れる、ジフエニルエーテル−3,3′ジカルボン酸また
はジフエニルエーテル−3,4′−ジカルボン酸の製造
方法。
2. Formula (I) [In the formula, -COOH is at the 3 or 4 position relative to the hydroxyl group] and m- or p-hydroxybenzoic acid represented by the formula (II) [In the formula, X represents Br or Cl, and -COOH is at the 3 or 4 position with respect to X. ] The m- or p-halogenated benzoic acid shown by these is 8
-In the presence of a quinolinol copper complex catalyst, an alkali metal carbonate or an alkali metal hydroxide is used in an amount of 0.3 to 2.0 equivalents based on the hydroxyl group and carboxylic acid group of the compounds of formula (I) and formula (II). Proton polar solvent and alkylene glycol represented by formula (IV) [Wherein, R and R'are hydrogen atoms, methyl or ethyl groups, and n is an integer of 0 to 10] Formula (III) characterized by reacting by heating in a solvent [In the formula, -COOH is in the 3,3 'or 3,4' position. The manufacturing method of diphenyl ether-3,3 'dicarboxylic acid or diphenyl ether-3,4'-dicarboxylic acid shown by these.
JP60279907A 1985-12-12 1985-12-12 Method for producing diphenyl ether dicarboxylic acid Expired - Lifetime JPH0641435B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
JP60279907A JPH0641435B2 (en) 1985-12-12 1985-12-12 Method for producing diphenyl ether dicarboxylic acid

Publications (2)

Publication Number Publication Date
JPS62138449A JPS62138449A (en) 1987-06-22
JPH0641435B2 true JPH0641435B2 (en) 1994-06-01

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ID=17617578

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