JPH06256251A - Production of 4'-acetylbiphenyl-4-carboxylic acid - Google Patents

Production of 4'-acetylbiphenyl-4-carboxylic acid

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Publication number
JPH06256251A
JPH06256251A JP5067361A JP6736193A JPH06256251A JP H06256251 A JPH06256251 A JP H06256251A JP 5067361 A JP5067361 A JP 5067361A JP 6736193 A JP6736193 A JP 6736193A JP H06256251 A JPH06256251 A JP H06256251A
Authority
JP
Japan
Prior art keywords
carboxylic acid
acetylbiphenyl
acid
mmol
acetyl
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
JP5067361A
Other languages
Japanese (ja)
Inventor
Yasuhito Ogawa
泰仁 小川
Teruaki Yamada
輝明 山田
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.)
Eneos Corp
Original Assignee
Japan Energy Corp
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 Japan Energy Corp filed Critical Japan Energy Corp
Priority to JP5067361A priority Critical patent/JPH06256251A/en
Publication of JPH06256251A publication Critical patent/JPH06256251A/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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  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To provide a method for profitably producing 4'-acetylbiphenyl-4- carboxylic acid. CONSTITUTION:This is a method for producing 4'-acetylbiphenyl-4-carboxylic acid comprises oxidizing 4'-acetyl-4-methylbiphenyl with molecular oxygen in the presence of cobalt in a solution containing at least 50wt.% of a lover aliphatic monocarboxylic acid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、4'-アセチル-4-メチ
ルビフェニルから4'-アセチルビフェニル-4-カルボン
酸を製造する方法に関する。4'-アセチルビフェニル-
4-カルボン酸は、液晶化合物中間体や高機能性ポリマ
ーの合成原料として有用な4'-ヒドロキシビフェニル-
4-カルボン酸の原料として有用なものである。
FIELD OF THE INVENTION The present invention relates to a method for producing 4'-acetylbiphenyl-4-carboxylic acid from 4'-acetyl-4-methylbiphenyl. 4'-acetylbiphenyl-
4-Carboxylic acid is a useful 4'-hydroxybiphenyl- as a raw material for the synthesis of liquid crystal compound intermediates and highly functional polymers.
It is useful as a raw material for 4-carboxylic acid.

【0002】[0002]

【従来の技術】この4'-ヒドロキシビフェニル-4-カル
ボン酸は、4'-アセチルビフェニル-4-カルボン酸を酸
化剤で酸化することにより極めて容易に得ることかでき
る。
2. Description of the Related Art This 4'-hydroxybiphenyl-4-carboxylic acid can be obtained very easily by oxidizing 4'-acetylbiphenyl-4-carboxylic acid with an oxidizing agent.

【0003】この4'-アセチルビフェニル-4-カルボン
酸は、4'-アセチル-4-シアノビフェニルを水又はアル
コール中で加溶媒分解して製造する方法が提案されてい
る(特開昭64-75415号公報)。しかしこの方法の
出発原料である4'-アセチル-4-シアノビフェニルはビ
フェニルから誘導されるが、この合成操作が煩雑であ
り、あまり好ましい方法ではない。
A method for producing this 4'-acetylbiphenyl-4-carboxylic acid by solvolysis of 4'-acetyl-4-cyanobiphenyl in water or alcohol has been proposed (JP-A-64- 75415). However, 4'-acetyl-4-cyanobiphenyl, which is the starting material of this method, is derived from biphenyl, but this synthetic operation is complicated and is not a very preferable method.

【0004】一方、4'-ヒドロキシビフェニル-4-カル
ボン酸については、例えば、p-フェニルフェノールをカ
ルバミン酸クロライドでカルバメート化した後、塩化ア
ルミニウムの存在下にカルバミン酸クロライドでアミド
化し、これを加水分解する方法(特開昭63-11944
0号公報)、ジ臭素化又はジヨウ素化ビフェニルを一酸
化炭素でモノカルボニル化し、次いで残りの臭素又はヨ
ウ素を加水分解して水酸基と置換する方法(特開昭63-
99036号公報)等が知られている。しかし、ビフェ
ニルからこれらの方法を経て4'-ヒドロキシビフェニル
-4-カルボン酸を製造すると反応工程が複雑となり、工
業的に有利な方法ではない。
On the other hand, with respect to 4'-hydroxybiphenyl-4-carboxylic acid, for example, p-phenylphenol is carbamate-ized with carbamic acid chloride, amidated with carbamic acid chloride in the presence of aluminum chloride, and then hydrolyzed. Method of disassembling (Japanese Patent Laid-Open No. 63-11944)
No. 0), a dibrominated or diiodinated biphenyl is monocarbonylated with carbon monoxide, and then the remaining bromine or iodine is hydrolyzed to substitute with a hydroxyl group (JP-A-63-
No. 99036) is known. However, 4'-hydroxybiphenyl was obtained from biphenyl through these methods.
The production of -4-carboxylic acid complicates the reaction process and is not an industrially advantageous method.

【0005】[0005]

【発明が解決しようとする課題】本発明は上記現状を鑑
みなされたもので、本発明の目的は工業的に有利な4'-
アセチルビフェニル-4-カルボン酸の製造方法を提供す
ることにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above situation, and an object of the present invention is industrially advantageous 4'-
It is to provide a method for producing acetylbiphenyl-4-carboxylic acid.

【0006】[0006]

【課題を解決しようとする手段】本発明の4'-アセチル
ビフェニル-4-カルボン酸の製造方法は、4'-アセチル
-4-メチルビフェニルを低級脂肪族モノカルボン酸をの
少なくとも50重量%含む溶液中で、コバルトの存在
下、分子状酸素により酸化することからなるものであ
る。
The method for producing 4'-acetylbiphenyl-4-carboxylic acid according to the present invention is 4'-acetyl.
It consists of oxidizing 4-methylbiphenyl with molecular oxygen in the presence of cobalt in a solution containing at least 50% by weight of a lower aliphatic monocarboxylic acid.

【0007】本発明で用いる4'-アセチル-4-メチルビ
フェニルは、ビフェニルを塩化アルミニウム等のアルキ
ル化触媒の存在下にメチル化し、得られた4-メチルビ
フェニルを塩化アルミニウム等のアシル化触媒の存在
下、無水酢酸、塩化アセチル等のアセチル化剤によって
アセチル化することによって収率良く、しかも経済的に
得られる。
The 4'-acetyl-4-methylbiphenyl used in the present invention is obtained by methylating biphenyl in the presence of an alkylation catalyst such as aluminum chloride, and converting the obtained 4-methylbiphenyl into an acylation catalyst such as aluminum chloride. Acetylation in the presence of an acetylating agent such as acetic anhydride or acetyl chloride provides a good yield and is economical.

【0008】本発明は、この4'-アセチル-4-メチルビ
フェニルのメチル基を選択的に酸化するものであるが、
この酸化は低級脂肪族モノカルボン酸を少なくとも50
重量%含む溶液中で行う。この場合の低級脂肪族モノカ
ルボン酸は、炭素数が1〜5のモノカルボン酸で、蟻
酸、酢酸、プロピオン酸等を用いることが好ましい。ま
たこれらの臭化物であるブロモ酢酸等を用いることもで
きるが、実用上は酢酸が最も好ましい。また、低級脂肪
族モノカルボン酸は他の溶媒、例えば、モノクロロベン
ゼン、ジクロロベンゼン等のベンゼン系溶媒と混合して
用いても良いが、この場合前記カルボン酸は50重量%
以上含有させないと酸化反応が十分に進行しない。
The present invention selectively oxidizes the methyl group of 4'-acetyl-4-methylbiphenyl.
This oxidation produces at least 50 lower aliphatic monocarboxylic acids.
Performed in a solution containing wt%. In this case, the lower aliphatic monocarboxylic acid is a monocarboxylic acid having 1 to 5 carbon atoms, and formic acid, acetic acid, propionic acid or the like is preferably used. Although bromoacetic acid, which is a bromide of these, can be used, acetic acid is most preferable in practical use. The lower aliphatic monocarboxylic acid may be used as a mixture with another solvent, for example, a benzene solvent such as monochlorobenzene or dichlorobenzene. In this case, the carboxylic acid is 50% by weight.
If the above content is not contained, the oxidation reaction will not proceed sufficiently.

【0009】この工程で用いる金属触媒種としてはコバ
ルトを用いるが、コバルト以外にマンガン、セリウム、
ニッケル、鉄、銅、亜鉛等の他の金属が存在していて
も、何ら支障をきたすものではない。この金属触媒は、
金属単体の形態で用いることもできるが、酸化物、水酸
化物、炭酸塩、ハロゲン化物等の無機塩や、蟻酸、酢
酸、プロピオン酸等の脂肪酸の有機酸塩などの化合物の
形態のものが溶媒に対する溶解性が高いので好ましい。
特には、溶媒に用いる低級脂肪族モノカルボン酸の有機
酸塩が好ましい。また金属触媒は、分子状臭素、臭化水
素、臭化ナトリウム、臭化カリウム、臭化アンモニウム
等の臭素を助触媒として併せて用いると金属の触媒活性
が向上するので好ましい。
Cobalt is used as the metal catalyst species used in this step. In addition to cobalt, manganese, cerium,
The presence of other metals such as nickel, iron, copper and zinc does not cause any problems. This metal catalyst is
Although they can be used in the form of a simple metal, those in the form of compounds such as inorganic salts such as oxides, hydroxides, carbonates and halides, and organic acid salts of fatty acids such as formic acid, acetic acid and propionic acid can be used. It is preferable because it has high solubility in a solvent.
Particularly, an organic acid salt of a lower aliphatic monocarboxylic acid used as a solvent is preferable. Further, the metal catalyst is preferably used together with bromine such as molecular bromine, hydrogen bromide, sodium bromide, potassium bromide and ammonium bromide as a cocatalyst because the catalytic activity of the metal is improved.

【0010】酸化剤として用いる分子状酸素は、純酸素
や工業用排ガスなども使用できるが、工業的には空気を
用いることが最適である。
As the molecular oxygen used as an oxidant, pure oxygen or industrial exhaust gas can be used, but it is most preferable to use air industrially.

【0011】酸化工程で使用される溶媒、金属触媒及び
原料の4'-アセチル-4-メチルビフェニルの量及びそれ
らの比は特に規制されるものではないが、実用的には金
属触媒は溶媒1リットルに対し金属種それぞれが0.0
1〜0.5モル、助触媒としての臭素を併せて用いる場
合には、臭素は金属触媒の金属量の合計に対し元素比で
0.01〜5の範囲で用いることが好ましい。
The solvent used in the oxidation step, the amount of 4'-acetyl-4-methylbiphenyl as the metal catalyst and the raw material and the ratio thereof are not particularly limited, but the metal catalyst is practically used as the solvent 1 Each metal type is 0.0 per liter
When 1 to 0.5 mol and bromine as a co-catalyst are used together, it is preferable to use bromine in an element ratio of 0.01 to 5 with respect to the total amount of metals in the metal catalyst.

【0012】この反応の反応温度は40〜220℃の範
囲で行うのが好ましい。反応方式は、回分式、連続式及
び半回分式のいずれでもよい。この反応における生成物
は、4'-アセチルビフェニル-4-カルボン酸、4,4'-
ビフェニルジカルボン酸、未反応の4'-アセチル-4-メ
チルビフェニルの混合物として得られる。この混合物か
ら酸析や再結晶等の公知の方法により4'-アセチルビフ
ェニル-4-カルボン酸を単離することができる。
The reaction temperature of this reaction is preferably 40 to 220 ° C. The reaction system may be a batch system, a continuous system or a semi-batch system. The product of this reaction is 4'-acetylbiphenyl-4-carboxylic acid, 4,4'-
Obtained as a mixture of biphenyldicarboxylic acid and unreacted 4'-acetyl-4-methylbiphenyl. From this mixture, 4'-acetylbiphenyl-4-carboxylic acid can be isolated by a known method such as acid precipitation or recrystallization.

【0013】[0013]

【実施例】この実施例中の4'-アセチルビフェニル-4-
カルボン酸の収量はガスクロマトグラフィー、高速液体
クロマトグラフィー及びガスクロマトグラフ質量分析に
よって、同定し、定量した。
EXAMPLE 4'-Acetylbiphenyl-4- in this example
The yield of carboxylic acid was identified and quantified by gas chromatography, high performance liquid chromatography and gas chromatograph mass spectrometry.

【0014】(実施例1)4'-アセチル-4-メチルビフ
ェニル2.33g(11.1mmol)に対し酢酸コバルト(II)
4水和物1.37g(5.50mmol)、臭化ナトリウム0.0
54g(0.52mmol)及び酢酸50mlを反応容器に入れ、
撹拌下、酸素ガスを1分間に300mlの割合で溶液中に
吹き込みながら常圧条件下で90℃に加熱した。2時間
反応を行ったところ、4'-アセチルビフェニル-4-カル
ボン酸2.34g(収率87.8mol%)を含む白色の生成物
2.61gを得た。
Example 1 2.33 g (11.1 mmol) of 4'-acetyl-4-methylbiphenyl was added to cobalt (II) acetate.
Tetrahydrate 1.37 g (5.50 mmol), sodium bromide 0.0
54 g (0.52 mmol) and 50 ml acetic acid were placed in a reaction vessel,
While stirring, oxygen gas was blown into the solution at a rate of 300 ml per minute, and the solution was heated to 90 ° C. under normal pressure. When the reaction was carried out for 2 hours, 2.61 g of a white product containing 2.34 g (yield 87.8 mol%) of 4'-acetylbiphenyl-4-carboxylic acid was obtained.

【0015】これに1.3%濃度の水酸化ナトリウム水
溶液100mlを加え、30分間撹拌した後、不溶物をろ
過回収した。この不溶物に2%濃度の硫酸水溶液50ml
を加え、20分間撹拌し、固形物をろ過して乾燥させた
結果、純度98%以上の4'-アセチルビフェニル-4-カ
ルボン酸2.21g(収率83.0mol%)が得られた。
To this, 100 ml of a 1.3% aqueous sodium hydroxide solution was added, and after stirring for 30 minutes, the insoluble matter was collected by filtration. 50 ml of 2% sulfuric acid solution in this insoluble matter
Was added, the mixture was stirred for 20 minutes, and the solid matter was filtered and dried. As a result, 2.21 g (yield 83.0 mol%) of 4'-acetylbiphenyl-4-carboxylic acid having a purity of 98% or more was obtained.

【0016】(実施例2)酢酸コバルト(II)4水和物を
0.686g(2.75mmol)使用し、他は実施例1と同様
の方法で2時間反応を行ったところ、4'-アセチルビフ
ェニル-4-カルボン酸2.06g(収率77.2mol%)を含
む白色の生成物2.51gを得た。
Example 2 0.686 g (2.75 mmol) of cobalt (II) acetate tetrahydrate was used, and the reaction was carried out for 2 hours in the same manner as in Example 1 except that 4'- 2.51 g of a white product containing 2.06 g of acetylbiphenyl-4-carboxylic acid (yield 77.2 mol%) was obtained.

【0017】(実施例3)反応温度を70℃とし、他は
実施例1と同様の方法で6時間反応を行ったところ、
4'-アセチルビフェニル-4-カルボン酸2.50g(収率
93.6mol%)を含む白色の生成物2.59gを得た。
(Example 3) When the reaction temperature was 70 ° C and the reaction was carried out for 6 hours in the same manner as in Example 1, except that
2.59 g of a white product containing 2.50 g of 4'-acetylbiphenyl-4-carboxylic acid (yield 93.6 mol%) was obtained.

【0018】(実施例4)反応温度を60℃とし、他は
実施例1と同様の方法で6時間反応を行ったところ、
4'-アセチルビフェニル-4-カルボン酸2.44g(収率
91.4mol%)を含む白色の生成物2.56gを得た。
Example 4 The reaction temperature was set to 60 ° C., and the reaction was carried out for 6 hours in the same manner as in Example 1, except that
2.56 g of a white product containing 2.44 g (yield 91.4 mol%) of 4'-acetylbiphenyl-4-carboxylic acid was obtained.

【0019】(実施例5)酢酸コバルト(II)4水和物を
1.09g(4.40mmol)使用して更に酢酸マンガン(II)
4水和物0.270g(1.10mmol)を加えて、実施例1
と同様の方法で2時間反応を行ったところ、4'-アセチ
ルビフェニル-4-カルボン酸2.14g(収率80.3mol
%)を含む黄白色の生成物2.55gを得た。
Example 5 1.09 g (4.40 mmol) of cobalt (II) acetate tetrahydrate was used and manganese (II) acetate was further added.
Example 1 was added with 0.270 g (1.10 mmol) of tetrahydrate.
When the reaction was carried out for 2 hours in the same manner as described above, 2.14 g of 4'-acetylbiphenyl-4-carboxylic acid (yield 80.3 mol
%) Was obtained, giving 2.55 g of a yellowish white product.

【0020】(実施例6)酢酸コバルト(II)4水和物を
0.686g(2.75mmol)、酢酸マンガン(II)4水和物
を0.673g(2.75mmol)とした以外は実施例5と同
様の方法で2時間反応を行ったところ、4'-アセチルビ
フェニル-4-カルボン酸1.15g(収率43.0mol%)を
含む黄白色の生成物2.53gを得た。
Example 6 Example 6 was carried out except that 0.686 g (2.75 mmol) of cobalt acetate (II) tetrahydrate and 0.673 g (2.75 mmol) of manganese (II) acetate tetrahydrate were used. When the reaction was carried out for 2 hours in the same manner as in Example 5, 2.53 g of a yellowish white product containing 1.15 g (yield 43.0 mol%) of 4'-acetylbiphenyl-4-carboxylic acid was obtained.

【0021】(実施例7)酢酸コバルト(II)4水和物を
1.09g(4.40mmol)使用して更に酢酸セリウム(III)
1水和物0.369g(1.10mmol)を加えてた以外は実
施例1と同様の方法で2時間反応を行ったところ、4'-
アセチルビフェニル-4-カルボン酸2.11g(収率79.
1mol%)を含む黄白色の生成物2.56gを得た。
EXAMPLE 7 1.09 g (4.40 mmol) of cobalt (II) acetate tetrahydrate was used and further cerium (III) acetate was used.
When the reaction was performed for 2 hours in the same manner as in Example 1 except that 0.369 g (1.10 mmol) of monohydrate was added, 4'-
Acetylbiphenyl-4-carboxylic acid 2.11 g (yield 79.
2.56 g of a pale yellow product containing 1 mol%) are obtained.

【0022】(実施例8)4'-アセチル-4-メチルビフ
ェニル13.88g(66.0mmol)に対し酢酸コバルト(I
I)4水和物1.37g(5.50mmol)、酢酸マンガン(II)
4水和物0.270g(1.10mmol)、臭化カリウム1.3
6g(13.2mmol)、酢酸200ml及びクロロベンゼン1
00mlを0.5リットルのチタン製オートクレーブに入
れ、30kgf/cm2の加圧下で撹拌し、空気を毎時160
リットルの割合で溶液中に吹き込みながら120℃にて
30分間反応を行ったところ、4'-アセチルビフェニル
-4-カルボン酸13.35g(収率83.5mol%)を含む黄
白色の生成物15.25gを得た。
(Example 8) Cobalt acetate (I) was added to 13.88 g (66.0 mmol) of 4'-acetyl-4-methylbiphenyl.
I) tetrahydrate 1.37 g (5.50 mmol), manganese (II) acetate
0.270 g (1.10 mmol) tetrahydrate, potassium bromide 1.3
6 g (13.2 mmol), acetic acid 200 ml and chlorobenzene 1
00 ml was placed in a 0.5 liter titanium autoclave, stirred under a pressure of 30 kgf / cm2, and air was supplied at 160 per hour.
When the reaction was carried out at 120 ° C for 30 minutes while blowing it into the solution at a rate of 4 liters, 4'-acetylbiphenyl
15.25 g of a yellowish white product containing 13.35 g of 4-carboxylic acid (yield 83.5 mol%) was obtained.

【0023】(実施例9)4'-アセチル-4-メチルビフェ
ニル20.13g(95.7mmol)に対し酢酸コバルト(II)
4水和物2.74g(11.0mmol)、酢酸ニッケル(II)4
水和物0.547(2.20mmol)、臭化カリウム1.36g
(13.2mmol)及び酢酸300mlを0.5リットルのチタ
ン製オートクレーブに入れ、25kgf/cm2の加圧下で撹
拌し、空気を毎時160リットルの割合で溶液中に吹き
込みながら150℃にて30分間反応を行ったところ、
4'-アセチルビフェニル-4-カルボン酸14.33g(収
率62.3mol%)を含む黄白色の生成物22.64gを得
た。
(Example 9) Cobalt (II) acetate was added to 20.13 g (95.7 mmol) of 4'-acetyl-4-methylbiphenyl.
2.74 g (11.0 mmol) tetrahydrate, nickel (II) acetate 4
Hydrate 0.547 (2.20 mmol), potassium bromide 1.36 g
(13.2 mmol) and 300 ml of acetic acid were placed in a titanium autoclave of 0.5 liter, stirred under a pressure of 25 kgf / cm2, and reacted at 150 ° C. for 30 minutes while blowing air into the solution at a rate of 160 liters per hour. I went to
22.64 g of a yellowish white product containing 14.33 g of 4'-acetylbiphenyl-4-carboxylic acid (yield 62.3 mol%) was obtained.

【0024】[0024]

【発明の効果】本発明は、工業的に有利に、4'-アセチ
ル-4-メチルビフェニルから4'-アセチルビフェニル-
4-カルボン酸を製造できるという格別の効果を奏す
る。
INDUSTRIAL APPLICABILITY The present invention is industrially advantageous in that 4'-acetyl-4-methylbiphenyl to 4'-acetylbiphenyl-
It has a special effect that 4-carboxylic acid can be produced.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 4'-アセチル-4-メチルビフェニルを、
低級脂肪族モノカルボン酸を少なくとも50重量%含む
溶液中で、コバルトの存在下、分子状酸素により酸化す
ることを特徴とする4'-アセチルビフェニル-4-カルボ
ン酸の製造方法。
1. A 4'-acetyl-4-methylbiphenyl,
A method for producing 4'-acetylbiphenyl-4-carboxylic acid, which comprises oxidizing with a molecular oxygen in the presence of cobalt in a solution containing at least 50% by weight of a lower aliphatic monocarboxylic acid.
JP5067361A 1993-03-04 1993-03-04 Production of 4'-acetylbiphenyl-4-carboxylic acid Pending JPH06256251A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5067361A JPH06256251A (en) 1993-03-04 1993-03-04 Production of 4'-acetylbiphenyl-4-carboxylic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5067361A JPH06256251A (en) 1993-03-04 1993-03-04 Production of 4'-acetylbiphenyl-4-carboxylic acid

Publications (1)

Publication Number Publication Date
JPH06256251A true JPH06256251A (en) 1994-09-13

Family

ID=13342806

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5067361A Pending JPH06256251A (en) 1993-03-04 1993-03-04 Production of 4'-acetylbiphenyl-4-carboxylic acid

Country Status (1)

Country Link
JP (1) JPH06256251A (en)

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