JPS61197546A - Production of 3,3'-dinitrodiphenyl ether - Google Patents

Production of 3,3'-dinitrodiphenyl ether

Info

Publication number
JPS61197546A
JPS61197546A JP60036535A JP3653585A JPS61197546A JP S61197546 A JPS61197546 A JP S61197546A JP 60036535 A JP60036535 A JP 60036535A JP 3653585 A JP3653585 A JP 3653585A JP S61197546 A JPS61197546 A JP S61197546A
Authority
JP
Japan
Prior art keywords
meta
self
reaction
condensation reaction
base
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
JP60036535A
Other languages
Japanese (ja)
Inventor
Keisaburo Yamaguchi
桂三郎 山口
Yukihiro Yoshikawa
幸宏 吉川
Masaji Tamai
正司 玉井
Kenichi Sugimoto
賢一 杉本
Yoshimitsu Tanabe
良満 田辺
Teruhiro Yamaguchi
彰宏 山口
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 JP60036535A priority Critical patent/JPS61197546A/en
Priority to AU53787/86A priority patent/AU568789B2/en
Priority to KR1019860001229A priority patent/KR880000203B1/en
Priority to EP86301234A priority patent/EP0193358B1/en
Priority to DE8686301234T priority patent/DE3665302D1/en
Publication of JPS61197546A publication Critical patent/JPS61197546A/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 obtain the titled compound useful as a raw material for agricultural chemicals and drugs easily in high purity and in high yield, by subjecting inexpensive meta-dinitrobenzene to self-condensation reaction in the presence of a base and a catalytic amount of meta-nitrophenol in an aprotic polar solvent. CONSTITUTION:Meta-nitrobenzene is subjected to self-condensation reaction in the presence of a base (e.g., potassium carbonate, potassium hydroxide, NaOH, etc.) and a catalytic amount of meta-nitrophenol in an aprotic polar solvent (e.g., 1,3-dimethyl-2-imidazolidinone, hexamethylphosphoramide, etc.) to give 3,3'-dinitrodiphenyl ether. Since this method has high conversion ratio to the aimed substance and high selectivity, it is economical. This process has further easy purification, and is industrially preferable.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、3.;’−ジニトロジフェニルエーテルの新
規な製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention comprises 3. ;'-Relating to a novel method for producing dinitrodiphenyl ether.

さらに詳しくは、メタジニトロベンゼンを塩基と触媒量
のメタニトロフェノールの存在下、非プロトン性極性溶
剤中で自己縮合反応させることを特徴とする3、5′−
ジニトロジフェニルエーテルの製造方法に関する。
More specifically, the 3,5'-
The present invention relates to a method for producing dinitrodiphenyl ether.

3.3′−ジニトロジフェニルエーテルは農医薬原料と
なるほか、ボリアεド、ポリアミドイミド、ポリイミド
の原料である3、3′−ジアミノジフェニルエーテルの
中間体である。
3.3'-Dinitrodiphenyl ether is an intermediate for 3,3'-diaminodiphenyl ether, which is a raw material for agrochemicals and medicines, and is also a raw material for boria ε-do, polyamideimide, and polyimide.

(従来の技術) 3、 s’ −ジニトロジフェニルニーテルハ、従来、
メタニトロフェノールとメタブロモニトロベンゼンのU
l1mann反応により製造する方法が知られている(
富田ら、薬学雑誌、、 751080(1955) 、
弁用ら、薬学雑誌、、  79273(1959) 、
 J、P、Cr1t−chleyら、T、Polyme
r、Sci 、、 part A−1101795(1
797) )。
(Prior art) 3. s'-dinitrodiphenylniterha, conventionally,
U of metanitrophenol and metabromonitrobenzene
A method of producing by l1mann reaction is known (
Tomita et al., Pharmaceutical Journal, 751080 (1955),
Benyo et al., Pharmaceutical Journal, 79273 (1959),
J, P, Crlt-chley et al., T, Polyme
r, Sci,, part A-1101795 (1
797) ).

(発明が解決しようとする問題点) しかしながら、これらの方法は収率が低かったシ、爆発
の危険性を供なう等の難点があり、さらに、工業的に実
施するうえで原料が高価で、入手が容易でないというこ
とが最大の欠点である。
(Problems to be solved by the invention) However, these methods have drawbacks such as low yields and the risk of explosion, and furthermore, the raw materials are too expensive to carry out industrially. The biggest drawback is that it is not easy to obtain.

(問題を解決するだめの手段) 本発明者らは、3.3’−ジニトロジフェニルエーテル
の安価なしかも工業的に製造し得る方法について鋭意検
討した。先にメタジニトロベンゼンとメタニトロフェノ
ールの化学量論量による方法およびメタジニトロベンゼ
ンを亜硝酸塩の存在下で自己縮合反応させる方法を見出
し、さらに、メタジニトロベンゼンの反応について鋭意
検討を重ねた結果、メタジニトロベンゼンを塩基と触媒
量のメタニトロフェノールの存在下で自己縮合反応全進
行させ得るということを見出し、本発明を完成させた。
(Another Means to Solve the Problem) The present inventors have intensively studied methods for producing 3,3'-dinitrodiphenyl ether at low cost and industrially. First, we discovered a method using stoichiometric amounts of metadinitrobenzene and metanitrophenol, and a method of self-condensing methadinitrobenzene in the presence of nitrite.Furthermore, as a result of intensive studies on the reaction of metadinitrobenzene, we discovered that metadinitrobenzene was The present invention was completed based on the discovery that the entire self-condensation reaction can proceed in the presence of a base and a catalytic amount of meta-nitrophenol.

すなわち、本発明はメタジニトロベンゼンを塩基と触媒
量のメタニトロフェノールの存在下、非プロトン性極性
溶剤中で自己縮合反応させることを特徴とする5、3′
−ジニトロジフェニルエーテルの製造方法である。
That is, the present invention is characterized in that methadinitrobenzene is subjected to a self-condensation reaction in an aprotic polar solvent in the presence of a base and a catalytic amount of metanitrophenol.
- A method for producing dinitrodiphenyl ether.

本発明の方法は、まず、触媒量のメタニトロフェノール
アルカリ金属がメタジニトロベンゼンと縮合し、次に、
生成した亜硝酸塩が順次メタジニトロベンゼンを自己縮
合反応に導くという方法である。したがって、メタジニ
トロベンゼンの自己縮合による以外に、任意の触媒量の
メタニトロフェノールからも目的物が導かれる。
The method of the present invention involves first condensing a catalytic amount of metanitrophenol alkali metal with metadinitrobenzene;
In this method, the generated nitrite sequentially leads metadinitrobenzene to a self-condensation reaction. Therefore, in addition to self-condensation of metadinitrobenzene, the desired product can also be derived from any catalytic amount of metanitrophenol.

ニトロ化合物の自己縮合反応でエーテル類を製造する例
としては、4−ニトロ−N−メチルフタルイミドから4
.4′−オキシビス(N−メチルフタルイミド)を製造
する方法(R,J、Markezichら。
An example of producing ethers by the self-condensation reaction of nitro compounds is 4-nitro-N-methylphthalimide.
.. Method for producing 4'-oxybis(N-methylphthalimide) (R,J, Markezich et al.

J、○rg、Chem、、 423431〜3434(
1977)  )、4−二トロヘンゾニトリルから4.
4′−ジシアノジフェニルエーテルを製造する方法(E
、He1nz  ら。
J, ○rg, Chem,, 423431-3434 (
1977) ), 4-nitrohenzonitrile to 4.
Method for producing 4'-dicyanodiphenyl ether (E
, Helnz et al.

Ger of fen 、、 2.037.781 )
等がある。
Ger of fen,, 2.037.781)
etc.

しかしながら、これらはいずれもP位に電子吸引性基を
持つ活性なニトロ基の反応であり、m位に電子吸引性基
を持つ不活性なニトロ基の反応は知られていない。
However, all of these reactions involve an active nitro group having an electron-withdrawing group at the P-position, and reactions involving an inert nitro group having an electron-withdrawing group at the m-position are unknown.

また、同−核にニトロ基を複数布する化合物の自己縮合
反応の例も知られていない。
Further, there is no known example of a self-condensation reaction of a compound having multiple nitro groups on the same nucleus.

本発明のニトロフェノールを触媒として、副生ずる亜硝
酸塩でメタジニトロベンゼンを自己縮合反応させる方法
は新規な反応である。
The method of the present invention in which metadinitrobenzene is subjected to a self-condensation reaction with nitrite as a by-product using nitrophenol as a catalyst is a novel reaction.

本発明の方法で使用する塩基としては、アルカリ金属の
炭酸塩、炭酸水素塩、水酸化物またはアルコキシドであ
り、具体的には炭酸カリウム、炭酸ナトリウム、炭酸水
素カリウム、水酸化カリウム、水酸化ナトリウム、ナト
リウムメトキシド、カリウムインプロポキシド等が挙げ
られる。
The base used in the method of the invention is an alkali metal carbonate, hydrogen carbonate, hydroxide or alkoxide, specifically potassium carbonate, sodium carbonate, potassium hydrogen carbonate, potassium hydroxide, sodium hydroxide. , sodium methoxide, potassium impropoxide, and the like.

これら塩基の使用量/は、触媒として使用されるJ: メタニトロフェノールに対して当量以上あればよく、具
体的には1〜10当量あれば良い。
The amount of these bases to be used may be at least equivalent to J:metanitrophenol used as a catalyst, and specifically, it may be from 1 to 10 equivalents.

本発明の方法で使用する溶剤としては、1.3−ジメチ
ル−2−イミダゾリジノン、ヘキサメチルホスホルアミ
ドが好ましく用いられ、N、N−ジメチルホルムアミド
、N、N−ジメチルアセトアミド、N−メチルピロリド
ン、ジメチルスルホキシド、スルホラン等も使用できる
As the solvent used in the method of the present invention, 1,3-dimethyl-2-imidazolidinone, hexamethylphosphoramide are preferably used, N,N-dimethylformamide, N,N-dimethylacetamide, N-methyl Pyrrolidone, dimethyl sulfoxide, sulfolane, etc. can also be used.

これらの溶剤の使用量は、特に限定されないが、通常、
原料に対して1〜15重量倍、好ましくは3〜10重量
倍である。
The amount of these solvents used is not particularly limited, but usually
The amount is 1 to 15 times, preferably 3 to 10 times the weight of the raw material.

また、本発明の方法では、反応を促進するための触媒と
して、銅粉または銅系化合物、あるいはクラウンエーテ
ル、ポリエチレングリコール、四級アンモニウム塩、四
級ホスホニウム塩のような相間移動触媒を使用しても何
ら差しつかえない。
Further, in the method of the present invention, a phase transfer catalyst such as copper powder or a copper-based compound, or a crown ether, polyethylene glycol, quaternary ammonium salt, or quaternary phosphonium salt is used as a catalyst to promote the reaction. There is nothing wrong with that either.

反応温度は、通常、100〜240℃の範囲であるが、
好ましくは140〜200℃の範囲がよい。
The reaction temperature is usually in the range of 100 to 240°C,
Preferably, the temperature is in the range of 140 to 200°C.

本発明の一般的な実施態様としては、所定量のメタニト
ロフェノール、塩基、および溶剤を装入し、メタニトロ
フェノールをアルカリ金属塩としたのち、メタジニトロ
ベンゼンを添加して反応させるか、あるいは、あらかじ
めメタジニトロベンゼンを含む全原料を同時に加え、そ
のまま昇温して反応させるかのいずれであっても良い。
In a general embodiment of the present invention, a predetermined amount of metanitrophenol, a base, and a solvent are charged, metanitrophenol is converted into an alkali metal salt, and then methadinitrobenzene is added and reacted, or, It is also possible to add all the raw materials containing metadinitrobenzene at the same time in advance, and then to raise the temperature and allow the reaction to occur.

勿論、これらに限定されるものでなくその他の態様によ
り適宜実施できる。
Of course, the present invention is not limited to these examples, and may be implemented in other ways as appropriate.

反応系内に水が生成する場合の除去方法として、窒素ガ
ス等を通気させることによって、反応中、徐々に系外に
排出させる方法があるが、一般的にはベンゼン、トルエ
ン、キシレン、クロルベンゼン等を少量使用して共沸に
よシ系外へと取り除く方法が多用される。
When water is generated in the reaction system, there is a method to remove it by passing nitrogen gas etc. to gradually discharge it out of the system during the reaction, but in general, benzene, toluene, xylene, and chlorobenzene are removed. A method is often used in which a small amount of acetate is used to remove it from the system by azeotropy.

反応の終点は、薄層クロマトグラフィー、高速液体クロ
マトグラフィー捷たはガスクロマトグラフィーにより原
料の減少を見ながら決定することができる。
The end point of the reaction can be determined by thin layer chromatography, high performance liquid chromatography, or gas chromatography while observing the decrease in raw materials.

反応終了後、濃縮したのち、あるいはそのまま水等に排
出して粗3,3′−ジニトロジフェニルエーテルを得る
。このものは溶剤で容易に再結晶精製することができる
After the reaction is completed, the residue is concentrated or directly discharged into water to obtain crude 3,3'-dinitrodiphenyl ether. This product can be easily purified by recrystallization using a solvent.

(作用および効果) 本発明の方法によれば、極めて安価なメタンニトロベン
ゼンを原料とし、触媒量のメタニトロフ” / −ルヲ
用イ”T: 3+ ”−ジニトロジフェニルエーテルが
製造できる。
(Functions and Effects) According to the method of the present invention, a catalytic amount of methane nitrobenzene can be produced using extremely inexpensive methane nitrobenzene as a raw material.

さらに、この方法は目的物への転化率および選択率が高
いので、より経済的であるばかりでなく、精製も容易で
あり高純度のものが収率よく製造できる等工業的な製造
方法として好適である。
Furthermore, since this method has a high conversion rate and selectivity to the target product, it is not only more economical, but also easy to purify and is suitable as an industrial manufacturing method because it can produce high-purity products with good yield. It is.

(実施例) 以下、本発明の方法を実施例により更に詳細に説明する
(Example) Hereinafter, the method of the present invention will be explained in more detail with reference to Examples.

実施例1゜ 攪拌装置、温度計、還流冷却器および水分離器を備えた
反応器にメタニトロフェノール702(0,05モル)
、96俸水酸化カリウム2.921i’ (0,05モ
ル)、ベンゼン”、Omlおよび1.ろ−ジメチル−2
−イミダゾリジノンsoomgを装入し、撹拌しながら
ベンゼンの還流状態で共沸してくる水を系外に除去した
。完全に共沸脱水を行なったのち、温度を60℃に下げ
てメタジニトロベンゼン84り(05モ″ル)を加えた
。次に、窒素ガスを通気させながら昇温しで温度を17
0〜180℃に保ち18時間反応させた。
Example 1 Metanitrophenol 702 (0.05 mol) was added to a reactor equipped with a stirrer, a thermometer, a reflux condenser and a water separator.
, 96 kalium potassium hydroxide 2.921i' (0.05 mol), benzene", Oml and 1.ro-dimethyl-2
-imidazolidinone somg was charged, and water that azeotroped under the reflux state of benzene was removed from the system while stirring. After complete azeotropic dehydration, the temperature was lowered to 60°C and 84 ml (0.5 mol) of metadinitrobenzene was added.Next, the temperature was raised to 17°C while bubbling nitrogen gas.
The temperature was kept at 0 to 180°C and the reaction was carried out for 18 hours.

反応終了後、減圧濃縮して溶剤を回収したのち、残有の
タール状物を水500m1に排出した。
After the reaction was completed, the solvent was recovered by concentration under reduced pressure, and the remaining tar-like substance was discharged into 500 ml of water.

撹拌をつづけると褐色小塊状の結晶となった。When stirring was continued, small brown crystals formed.

これを濾過、乾燥したのちベンゼンで再P品−j−ルこ
とにより39.2 ? (収率548%)の6.3′−
ジニトロジフェニルエーテルヲ得り。
After filtering and drying this, it was reconstituted with benzene. (yield 548%) of 6.3'-
Obtain dinitrodiphenyl ether.

このものを酢酸エチルで再結晶して微褐色プリズム晶の
純品を得た。
This product was recrystallized with ethyl acetate to obtain a pure product of slightly brown prismatic crystals.

融点は127〜128℃で元素分析の結果は次のとおり
である。
The melting point was 127-128°C, and the results of elemental analysis were as follows.

HN 計算値(%)   55,39  3.10  10.
77測定値(%)   55,12  3.31  1
0.71実施例2゜ 攪拌装置、温度計を備えた反応器にメタニトロフェノー
ル20.99 (0,15モル)、メタジニトロベンゼ
ン84y(0,5モル)、無水炭酸カリウム138グ(
0,1モル)、銅粉03L?およびヘキサメチルホスホ
ルアミド350m1を装入し、攪拌しながら、窒素ガス
を通気させて昇温した。温度180〜190℃で8時間
保って反応を終了した。
HN Calculated value (%) 55,39 3.10 10.
77 Measured value (%) 55,12 3.31 1
0.71 Example 2 Into a reactor equipped with a stirrer and a thermometer, 20.99 (0.15 mol) of metanitrophenol, 84 y (0.5 mol) of metadinitrobenzene, and 138 g (138 g) of anhydrous potassium carbonate were added.
0.1 mol), copper powder 03L? and 350 ml of hexamethylphosphoramide were charged, and the temperature was raised by bubbling nitrogen gas while stirring. The reaction was completed by maintaining the temperature at 180-190°C for 8 hours.

反応終了後の後処理は実施例1と同様に行なって57.
61(収率63.3 % )のろ、3′−ジニトロジフ
ェニルエーテルを得た。
Post-treatment after the completion of the reaction was carried out in the same manner as in Example 1.
61 (yield 63.3%), 3'-dinitrodiphenyl ether was obtained.

実施例3゜ 塩基をナトリウムメトキシド2.79 (0,05モル
)に替え、ベンゼンとともにメタノールを留去させた以
外は実施例1と同様に行なって39.79 (収率55
5%) +7) 3.3’−ジニトロジフェニルエーテ
ルを得た。
Example 3 The procedure of Example 1 was repeated except that the base was replaced with 2.79 (0.05 mol) of sodium methoxide and methanol was distilled off together with benzene.
5%) +7) 3.3'-dinitro diphenyl ether was obtained.

実施例4゜ 塩基を炭酸ナトリウム11M?(0,1モル)に替えた
以外は実施例2と同様に行なって50.39 (収$5
9.5%)ノ3.3’−シニトロンフェニルエーテルを
得た。
Example 4゜The base was 11M sodium carbonate? (0.1 mol) was carried out in the same manner as in Example 2, yielding 50.39 (yield $5
9.5%) of 3,3'-sinitron phenyl ether was obtained.

実施例5゜ 実施例1と同じ装置にメタニトロフェノール20.9 
P (0,15モル)、水酸化ナトリウム6グ(0,1
5モル)、ベンゼン50m1およびN、N−ジメチルホ
ルムアミド500m1’z装入し、撹拌しながらベンゼ
ンの還流状態で共沸してくる水を系外に除去した。完全
に共沸脱水を行なったのち、温度を60℃に下げてメタ
ジニトロベンゼン847(05モル)を加えた。以後の
操作は実施例1と同様に行なってS4B? (収率41
2%)の69口′−ジニトロジフェニルエーテルヲ得り
Example 5゜ Metanitrophenol 20.9 was added to the same apparatus as Example 1.
P (0.15 mol), 6 g of sodium hydroxide (0.1
5 moles), 50 ml of benzene, and 500 ml of N,N-dimethylformamide were charged, and water that azeotroped under the reflux state of benzene was removed from the system while stirring. After complete azeotropic dehydration, the temperature was lowered to 60° C. and metadinitrobenzene 847 (0.5 mol) was added. The subsequent operations are performed in the same manner as in Example 1, and S4B? (Yield 41
2%) of 69'-dinitrodiphenyl ether was obtained.

Claims (1)

【特許請求の範囲】[Claims] 1)メタジニトロベンゼンを塩基と触媒量のメタニトロ
フェノールの存在下、非プロトン性極性溶剤中で自己縮
合反応させることを特徴とする3,3′−ジニトロジフ
ェニルエーテルの製造方法。
1) A method for producing 3,3'-dinitrodiphenyl ether, which comprises subjecting metadinitrobenzene to a self-condensation reaction in an aprotic polar solvent in the presence of a base and a catalytic amount of metanitrophenol.
JP60036535A 1985-02-22 1985-02-27 Production of 3,3'-dinitrodiphenyl ether Pending JPS61197546A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP60036535A JPS61197546A (en) 1985-02-27 1985-02-27 Production of 3,3'-dinitrodiphenyl ether
AU53787/86A AU568789B2 (en) 1985-02-22 1986-02-20 3,3'-dinitrodiphenylether from m-dinitrobenzene
KR1019860001229A KR880000203B1 (en) 1985-02-22 1986-02-21 Process for the preparation of 3.3'-dinitrodi-phenyleter
EP86301234A EP0193358B1 (en) 1985-02-22 1986-02-21 Method of preparing 3,3'-dinitrodiphenyl ether
DE8686301234T DE3665302D1 (en) 1985-02-22 1986-02-21 Method of preparing 3,3'-dinitrodiphenyl ether

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60036535A JPS61197546A (en) 1985-02-27 1985-02-27 Production of 3,3'-dinitrodiphenyl ether

Publications (1)

Publication Number Publication Date
JPS61197546A true JPS61197546A (en) 1986-09-01

Family

ID=12472473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60036535A Pending JPS61197546A (en) 1985-02-22 1985-02-27 Production of 3,3'-dinitrodiphenyl ether

Country Status (1)

Country Link
JP (1) JPS61197546A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6212748A (en) * 1985-07-10 1987-01-21 Teijin Ltd Production of nitro-substituted diphenyl ether

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6212748A (en) * 1985-07-10 1987-01-21 Teijin Ltd Production of nitro-substituted diphenyl ether
JPH0415773B2 (en) * 1985-07-10 1992-03-19 Teijin Ltd

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