JPS6042781B2 - Method for producing symmetrical diphenyl ethers - Google Patents
Method for producing symmetrical diphenyl ethersInfo
- Publication number
- JPS6042781B2 JPS6042781B2 JP51160567A JP16056776A JPS6042781B2 JP S6042781 B2 JPS6042781 B2 JP S6042781B2 JP 51160567 A JP51160567 A JP 51160567A JP 16056776 A JP16056776 A JP 16056776A JP S6042781 B2 JPS6042781 B2 JP S6042781B2
- Authority
- JP
- Japan
- Prior art keywords
- group
- formula
- nuclear
- phase transfer
- transfer catalyst
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は一般式
@一@
Z5−nZ5−n
で表わされる対称型ジフェニルエーテル類の製造に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the production of symmetrical diphenyl ethers represented by the general formula @1@Z5-nZ5-n.
(式中Yはニトロ基を示し少くともその1個はエーテル
結合に対しオルト位またはパラ位を占めるものとする。(In the formula, Y represents a nitro group, at least one of which occupies the ortho or para position with respect to the ether bond.
Zは水素、アルコキシ基、もしくはアルキル基を示し、
nは1または2を示す。)本発明によつて得ら゛れる化
合物は、医薬、農薬、合成樹脂などの製造において有用
である。一般に本系列の化合物は核置換ハロゲン化ベン
ゼンと核置換フェノールのアルカリ金属塩とを反応させ
る、いわゆるウイリアムソン反応によつて製造されてい
る。この場合、原料として核置換ハロゲン化ベンゼンと
それに対応するフェノールのアルカリ金属塩の2種が必
要であり、しかも原料としてフェノールのナトリウム塩
を使用すると反応がほとんど進行せず一般に高価なりリ
ウム塩を必要とする。特公昭44−1433楢びにドイ
ツ特許1290147に於いては核置換ハロゲン化ベン
ゼンのみを原料とする対称型ジフェニルエーテル類の製
造方法が開示されているが、いずれの場合も反応溶媒と
して極性非プロトン溶媒の使用が必要でありしかも高価
な炭酸カリウム又は水酸化カリウムが必要である。Z represents hydrogen, an alkoxy group, or an alkyl group,
n represents 1 or 2. ) The compounds obtained according to the present invention are useful in the production of medicines, agricultural chemicals, synthetic resins, etc. Generally, this series of compounds is produced by the so-called Williamson reaction, in which a nuclear-substituted halogenated benzene is reacted with an alkali metal salt of a nuclear-substituted phenol. In this case, two types of raw materials are required: a nuclear-substituted halogenated benzene and the corresponding alkali metal salt of phenol.Moreover, if the sodium salt of phenol is used as a raw material, the reaction will hardly proceed and an expensive lithium salt is generally required. shall be. Japanese Patent Publication No. 44-1433 and German Patent No. 1290147 disclose a method for producing symmetrical diphenyl ethers using only nuclear-substituted halogenated benzene as a raw material, but in both cases, a polar aprotic solvent is used as the reaction solvent. Potassium carbonate or hydroxide is required and is expensive.
本発明者らは、核置換ハロゲン化ベンゼンのみをまたは
核置換ニトロベンゼンのみを原料として対称型ジフェニ
ルエーテルを製造するに際し、相間移動触媒を用いるこ
とにより、水酸化カリウムと同様に水酸化ナトリウムが
使用可能であり、反応溶媒としてベンゼン等の非極性溶
媒が使用可能であり且つ有機溶媒がなくても反応を進め
得ることを見い出し本発明の方法に到つた。The present inventors have discovered that by using a phase transfer catalyst, sodium hydroxide can be used in the same way as potassium hydroxide when producing symmetrical diphenyl ether using only nuclear-substituted halogenated benzene or only nuclear-substituted nitrobenzene as a raw material. The present inventors have discovered that a nonpolar solvent such as benzene can be used as a reaction solvent and that the reaction can proceed without an organic solvent, leading to the method of the present invention.
すなわち、本発明は一般式
(式中Y,Z,およびnは前記に同じ、Xはニトロ基、
塩素、臭素、沃素、またはフッ素原子を示す。That is, the present invention is based on the general formula (where Y, Z, and n are the same as above, X is a nitro group,
Indicates a chlorine, bromine, iodine, or fluorine atom.
)で表わされる核置換ニトロベンゼン、又は核置換ハロ
ゲン化ベンゼンを原料とし、相間移動触媒の存在下アル
カリ金属水酸化物と反応させる一般式(式中Y,Z,お
よびnは前記のとうり。) or a nuclear-substituted halogenated benzene is used as a raw material and reacted with an alkali metal hydroxide in the presence of a phase transfer catalyst (where Y, Z, and n are as described above).
)で表わ−される対称型ジフェニルエーテル類の製造方
法である。本発明の方法に適用される核置換ニトロベン
ゼン又は核置換ハロゲン化ベンゼンとしては、オルソジ
ニトロベンゼン、バラニトロベンゼン、2●3ージニト
ロトルエン、2●5ージニトロトルエン、3●4ージニ
トロトルエン、2◆3−ニトロバラキシレン、2●5ー
ジニトロメタキシレン、オルソクロロニトロベンゼン、
バラクロロニトロベンゼン、4−クロロ3−ニトロトル
エン、2−・クロロ5−ニトロトルエン、4−ブロモ3
−ニトロアニソール、2−フルオロ5−ニトロアニソー
ル、2・4ージニトロフルオロベンゼン等が挙げられる
。) is a method for producing symmetrical diphenyl ethers represented by Examples of the nuclear-substituted nitrobenzene or the nuclear-substituted halogenated benzene that can be applied to the method of the present invention include ortho-dinitrobenzene, varanitrobenzene, 2●3-dinitrotoluene, 2●5-dinitrotoluene, 3●4-dinitrotoluene, 2◆3 -Nitrovaraxylene, 2●5-dinitromethaxylene, orthochloronitrobenzene,
Parachloronitrobenzene, 4-chloro3-nitrotoluene, 2-chloro5-nitrotoluene, 4-bromo3
-nitroanisole, 2-fluoro5-nitroanisole, 2,4-dinitrofluorobenzene, and the like.
本発明で用いられる相間移動触媒としては、例えばテト
ラn−ブチルアンモニウムクロリド、ベンジルトリエチ
ルアンモニウムプロミド、テトラn−ブチルホスホニウ
ムクロリド、セチルトリn−ブチルホスホニウムクロリ
ド等のアルキル基あるいはアリル基をもつ4級アンモニ
ウム塩類または4級ホスホニウム塩類、あるいはトリn
−ブチルアミンオキシド等のアミンオキシド類、あるい
は18−クラウンー6等のクラウンエーテル類等がl挙
げられる。Examples of the phase transfer catalyst used in the present invention include quaternary ammoniums having an alkyl group or an allyl group, such as tetra n-butylammonium chloride, benzyltriethylammonium bromide, tetra n-butylphosphonium chloride, and cetyltri n-butylphosphonium chloride. salts or quaternary phosphonium salts, or
Examples include amine oxides such as -butylamine oxide, and crown ethers such as 18-crown-6.
触媒の添加量には特に制限はないが、通常は、原料の核
置換ニトロベンゼン、又は核置換ハロゲン化ベンゼン1
モルに対して、0.0005モルから0.05モルの範
囲である。There is no particular limit to the amount of catalyst added, but usually the raw material nuclear-substituted nitrobenzene or nuclear-substituted halogenated benzene 1
The range is from 0.0005 mol to 0.05 mol.
本発明の方法で用いるアルカリ金属水酸化物としては水
酸化ナトリウム、水酸化カリウム、水酸化リチウムを挙
げることができる。The alkali metal hydroxides used in the method of the invention include sodium hydroxide, potassium hydroxide, and lithium hydroxide.
更に、水溶液とした時、加水分解によりアルカリ金属水
酸化物を生ずるような弱酸のアルカリ金属塩類、例えば
”炭酸ナトリウム、フェノールのナトリウム塩等もその
概念に含まれる。アルカリ金属水酸化物は固体のまま添
加することもできるが、通常は水溶液として添加される
。Furthermore, the concept also includes alkali metal salts of weak acids that produce alkali metal hydroxides by hydrolysis when made into aqueous solutions, such as sodium carbonate and sodium salts of phenol.Alkali metal hydroxides are solids. Although it can be added as is, it is usually added as an aqueous solution.
アルカリ金属水酸化物の添加量は原料の核置換ニトロベ
ンゼン又は核置換ハロゲン化ベンゼン1モルに対し1モ
ル以上であれば特に制限はないが、通常は1モルから5
0モルの範囲である。アルカリ金属水酸化物を水溶液と
して添加する場合、その濃度が稀薄であると触媒の効果
が発現しないので通常は、1呼量%以上の濃度で用いら
れる。本発明の方法に依ると、核置換ニトロベンゼン又
は核置換ハロゲン化ベンゼンとアルカリ金属水酸化物の
水溶液とを相間移動触媒の存在下で攪拌混合しながら加
熱するだけで目的とする対称型ジフェニルエーテル類を
製造することが可能であるが、水と二層系を形成する非
極性溶媒を添加することにより対称型ジフェニルエーテ
ル類の収率を増すことができるので、通常はベンゼン、
トルエン、シメン等の芳香族炭化水素類、ジクロルメタ
ン、臭化エチル、トリクロルエチレン、クロルベンゼン
等のハロゲン化炭化水素類、またはエチルエーテル、イ
ソプロピルエーテル、フェニルエチルエーテル等のエー
テル類等を添加して反応が行われる。The amount of alkali metal hydroxide added is not particularly limited as long as it is 1 mol or more per 1 mol of nuclear-substituted nitrobenzene or nuclear-substituted halogenated benzene as the raw material, but it is usually between 1 mol and 5 mol.
It is in the range of 0 mol. When an alkali metal hydroxide is added as an aqueous solution, the catalytic effect will not be exhibited if the concentration is too dilute, so it is usually used at a concentration of 1% by volume or more. According to the method of the present invention, the desired symmetrical diphenyl ethers can be produced by simply heating a nuclear-substituted nitrobenzene or a nuclear-substituted halogenated benzene and an aqueous solution of an alkali metal hydroxide while stirring and mixing them in the presence of a phase transfer catalyst. However, the yield of symmetric diphenyl ethers can be increased by adding a nonpolar solvent that forms a two-layer system with water, so benzene,
React by adding aromatic hydrocarbons such as toluene and cymene, halogenated hydrocarbons such as dichloromethane, ethyl bromide, trichloroethylene, and chlorobenzene, or ethers such as ethyl ether, isopropyl ether, and phenylethyl ether. will be held.
この場合反応液は有機層と水層の2液相を形成するので
、相間の接触を良くし反応速度を高めるために、反応は
強い攪拌の下に行われる。In this case, since the reaction solution forms two liquid phases, an organic layer and an aqueous layer, the reaction is carried out under strong stirring in order to improve the contact between the phases and increase the reaction rate.
反応温度は通常50℃から300℃の範囲で選ばれ、反
応時間は、反応温度、攪拌強度等により大きく変り通常
数十分から数日の範囲である。次に実施例により本発明
の方法を更に説明する。The reaction temperature is usually selected in the range of 50°C to 300°C, and the reaction time varies greatly depending on the reaction temperature, stirring intensity, etc., and is usually in the range of several tens of minutes to several days. The method of the present invention will now be further illustrated by examples.
実施例1
オルソジニトロベンゼン6.0g(0.0357モル)
、40m1のベンゼン、50Wt%の苛性ソーダ水溶液
60y1および相間移動触媒であるテトラn−ブチルア
ンモニウムクロリド0.2yを内容積300m1のオー
トクレーブに仕込み、オートクレーブ内の空気を窒素で
置換した後、100℃で6時間、1200r.p.mの
攪拌下で反応を行う。Example 1 Orthodinitrobenzene 6.0g (0.0357mol)
, 40 ml of benzene, 60 ml of a 50 wt% aqueous solution of caustic soda, and 0.2 y of tetra n-butylammonium chloride as a phase transfer catalyst were charged into an autoclave with an internal volume of 300 ml, and after replacing the air in the autoclave with nitrogen, the mixture was heated at 100°C for 60 ml. Time, 1200r. p. The reaction is carried out under stirring for m.
冷却後オートクレーブの内容物を取り出し、ベンゼンで
抽出する。ベンゼン抽出液を減圧蒸留して溶剤を留去す
る。次いで水蒸気蒸留により未反応の原料0.1yを回
収した,後、残留物をアルコールより再結晶してビス(
2−ニトロフェニル)エーテル3.7yを得た。(収率
81.1%)M.pll4〜115yC0実施例2
ベンゼンを添加しなかつた点以外は実施例1と;同様の
操作を行つて原料1.2fを回収し、ビス(2−ニトロ
フェニル)エーテル0.5yを得た。After cooling, the contents of the autoclave are removed and extracted with benzene. The benzene extract is distilled under reduced pressure to remove the solvent. Next, 0.1y of unreacted raw material was recovered by steam distillation, and the residue was recrystallized from alcohol to obtain bis(
3.7y of 2-nitrophenyl)ether was obtained. (Yield 81.1%)M. pll4-115yC0 Example 2 The same procedure as in Example 1 was performed except that benzene was not added; 1.2f of the raw material was recovered to obtain 0.5y of bis(2-nitrophenyl) ether.
実施例3−5相間移動触媒として実施例3ではテトラn
−ブチルアンモニウムプロミドを0.2y1実施例4で
5はトリn−ブチルアミンオキシドを0.2y1および
実施例5では18−クラウンー6を0.2y用いた点を
除いて実施例1と同様の操作を行つて表1の結果を得た
。Example 3-5 In Example 3, tetra n was used as a phase transfer catalyst.
- The same procedure as in Example 1 except that in Example 4, 0.2y1 of butylammonium bromide and 0.2y1 of tri-n-butylamine oxide were used in Example 5, and 0.2y1 of 18-crown-6 was used in Example 5. The results shown in Table 1 were obtained.
C実施例
6,7原料として、実施例6ではバラクロルニトロベン
ゼンを6.0f1実施例7では4−クロル3−ニトロト
ルエンを6.0yを夫々オルソジニトロベンゼンの代り
に用いた点と反応を150℃で行つた点とを除き実施例
1と同様の操作を行つて表2の結果を得た。C Examples 6 and 7 In Example 6, 6.0f of valachlornitrobenzene and 6.0y of 4-chloro3-nitrotoluene were used in place of orthodinitrobenzene in Example 7, and the reaction was carried out at 150°C. The same operations as in Example 1 were performed except for the points mentioned above, and the results shown in Table 2 were obtained.
実施例8
バラクロルニトロベンゼン15.0y(0.0955モ
ル)、炭酸ナトリウム27.8q(0.262モル)、
水90yおよび相間移動触媒であるテトラーn−ブチル
ホスホニウムプロミド0.6yを内容積300m1のオ
ートクレーブに仕込み、オートクレーブ内の空気を窒素
で置換した後、170゜Cで6時間、1200rpmの
攪拌下で反応を行つた。Example 8 Valachlornitrobenzene 15.0y (0.0955 mol), sodium carbonate 27.8q (0.262 mol),
90 y of water and 0.6 y of tetra n-butylphosphonium bromide as a phase transfer catalyst were charged into an autoclave with an internal volume of 300 m1, and after replacing the air in the autoclave with nitrogen, the mixture was heated at 170°C for 6 hours with stirring at 1200 rpm. The reaction was carried out.
Claims (1)
原子を示す。 Yはニトロ基を示し、少くともその1つはXに対しオル
ト位またはパラ位を占めるものとする。Zは水素、アル
コキシ基、アルキル基を示す。nは1または2を示す。
)で表わされる核置換ニトロベンゼン、または核置換ハ
ロゲン化ベンゼンを相間移動触媒の存在下アルカリ金属
水酸化物と反応させることを特徴とする一般式▲数式、
化学式、表等があります▼ (式中、Y、Z、およびnは前記のとおり。 )で表わされる対称型ジフェニルエーテル類の製造方法
。2 アルキル基あるいはアリル基をもつ4級アンモニ
ウム塩類または4級ホスホニウム塩類、アミンオキシド
類、およびクラウンエーテル類よりなる化合物群の中か
ら選ばれた1つもしくはそれらの混合物を相間移動触媒
として使用する特許請求の範囲1の方法。 3 反応に際して水と二層系を形成する非極性溶媒を存
在させる特許請求の範囲1または2の方法。[Claims] 1 General formula ▲ Numerical formula, chemical formula, table, etc. ▼ (In the formula, X represents a nitro group, chlorine, bromine, iodine, or fluorine atom. Y represents a nitro group, and at least one Z shall occupy the ortho or para position with respect to X. Z represents hydrogen, an alkoxy group, or an alkyl group. n represents 1 or 2.
) or a nuclear-substituted halogenated benzene is reacted with an alkali metal hydroxide in the presence of a phase transfer catalyst.
There are chemical formulas, tables, etc. ▼ Method for producing symmetrical diphenyl ethers represented by (in the formula, Y, Z, and n are as described above). 2. A patent for using as a phase transfer catalyst one selected from the group of compounds consisting of quaternary ammonium salts or quaternary phosphonium salts, amine oxides, and crown ethers having an alkyl group or allyl group, or a mixture thereof. The method of claim 1. 3. The method according to claim 1 or 2, wherein a nonpolar solvent that forms a two-layer system with water is present during the reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51160567A JPS6042781B2 (en) | 1976-12-29 | 1976-12-29 | Method for producing symmetrical diphenyl ethers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51160567A JPS6042781B2 (en) | 1976-12-29 | 1976-12-29 | Method for producing symmetrical diphenyl ethers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5384926A JPS5384926A (en) | 1978-07-26 |
| JPS6042781B2 true JPS6042781B2 (en) | 1985-09-25 |
Family
ID=15717757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51160567A Expired JPS6042781B2 (en) | 1976-12-29 | 1976-12-29 | Method for producing symmetrical diphenyl ethers |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6042781B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4783285A (en) * | 1983-04-11 | 1988-11-08 | E. I. Dupont De Nemours And Company | Process for the nucleophilic substitution of unactivated aromatic and heteroaromatic substrates |
-
1976
- 1976-12-29 JP JP51160567A patent/JPS6042781B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5384926A (en) | 1978-07-26 |
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