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JPS5943934B2 - Separation and purification method for monochlorinated side chains of naphthalene derivatives - Google Patents
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JPS5943934B2 - Separation and purification method for monochlorinated side chains of naphthalene derivatives - Google Patents

Separation and purification method for monochlorinated side chains of naphthalene derivatives

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Publication number
JPS5943934B2
JPS5943934B2 JP18399481A JP18399481A JPS5943934B2 JP S5943934 B2 JPS5943934 B2 JP S5943934B2 JP 18399481 A JP18399481 A JP 18399481A JP 18399481 A JP18399481 A JP 18399481A JP S5943934 B2 JPS5943934 B2 JP S5943934B2
Authority
JP
Japan
Prior art keywords
formula
general formula
side chain
derivative represented
naphthalene derivative
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
Application number
JP18399481A
Other languages
Japanese (ja)
Other versions
JPS57114528A (en
Inventor
征司 武内
和人 秋山
正道 清水
貞良 松井
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.)
Ihara Chemical Industry Co Ltd
Original Assignee
Ihara Chemical Industry 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 Ihara Chemical Industry Co Ltd filed Critical Ihara Chemical Industry Co Ltd
Priority to JP18399481A priority Critical patent/JPS5943934B2/en
Publication of JPS57114528A publication Critical patent/JPS57114528A/en
Publication of JPS5943934B2 publication Critical patent/JPS5943934B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、医薬、農薬等の製造中間体として有用なナフ
タレン誘導体側鎖モノ塩素化物の分離精製法に関し、さ
らに詳しくはナフタレン誘導体を側鎖塩素化して得られ
る粗ナフタレン誘導体側鎖塩素化物から高収率でしかも
高純度でナフタレン誘導体側鎖モノ塩素化物のみを分離
精製する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating and purifying side chain monochlorinated products of naphthalene derivatives useful as intermediates in the production of pharmaceuticals, agricultural chemicals, etc. More specifically, the present invention relates to a method for separating and purifying side chain monochlorinated products of naphthalene derivatives, which are useful as intermediates in the production of pharmaceuticals, agricultural chemicals, etc. The present invention relates to a method for separating and purifying only monochlorinated side chains of naphthalene derivatives from chlorinated side chains of derivatives with high yield and high purity.

ナフタレン誘遵伏@11鉛モノ塩素化物は対応するナフ
タ一U?νノ?リ,!年些?素化により製造されるが、
この際副生物としてナフタレン誘導体側鎖モノ塩素化物
と近似の沸点を有するナフタレン誘導体側鎖ジおよびト
リ塩素化物、および核塩素化物が生成する。
Naphthalene compliance @11 Lead monochloride is the corresponding naphthalene U? νノ? Ri,! How old is it? Although it is produced by chemical treatment,
At this time, as by-products, di- and trichlorinated products of the naphthalene derivative side chain and nuclear chlorinated products having boiling points similar to those of the monochlorinated product of the naphthalene derivative side chain are produced.

従来これらの副生物を含む粗ナフタレン誘導体側鎖塩素
化物からナフタレン誘導体側鎖モノ塩素化物の分離精製
は蒸留または精留による方法で行なつている。
Conventionally, separation and purification of monochlorinated side chains of naphthalene derivatives from crude chlorinated side chains of naphthalene derivatives containing these by-products has been carried out by distillation or rectification.

しかし、蒸留または精留による分離精製法ではナフタレ
ン誘導体側鎖モノ塩素化物と前記副生物との沸点差が小
さいために分離精製が極めて困難であり、これらの方法
では完全に分離精製を行なうことが容易でないため得ら
れるナフタレン誘導体側鎖モノ塩素化物は低純度、低収
率であつた。
However, separation and purification using distillation or rectification is extremely difficult due to the small boiling point difference between the side chain monochlorinated product of the naphthalene derivative and the above-mentioned by-product, and these methods cannot completely separate and purify the product. Since this is not easy, the side chain monochlorinated naphthalene derivatives obtained had low purity and low yield.

たとえば、2−メチルナフタレンの粗側鎖塩素化物では
2−クロロメチルナフタレン(側鎖モノ塩素化物、沸点
168〜169℃/20m7nHg)と副生する、1−
クロロ−2−メチルナフタレン(核塩素化物、沸点16
8℃/21mmHg)との沸点がほとんど等しいために
蒸留および精留によつて2−クロロメチルナフタレンを
分離精製することは不可能である。本発明者らは高純度
のナフタレン誘導体側鎖モノ塩素化物の製造を目的にナ
フタレン誘導体を側鎖塩素化して得られる粗ナフタレン
誘導体側鎖塩素化物から、高収率かつ高純度のナフタレ
ン誘導体側鎖モノ塩素化物を分離精製する方法について
種々研究を重ねた結果、粗ナフタレン誘導体側鎖塩素化
物に脂肪族第二級アミンを反応させればナフタレン誘導
体側鎖モノ塩素化物のみが反応して第三級アミン誘導体
を生成し、ナフタレン誘導体側鎖ジおよびトリ塩素化物
および被塩素化物等のナフタレン誘導体側鎖塩素化副生
物と分離でき、ついで分離したナフタレン誘導体側鎖モ
ノ塩素化物の第三級アミン誘導体に酸クロリドを反応さ
せることにより高収率でナフタレン誘導体側鎖モノ塩素
化物を得ることができるという事実を見出し本発明を完
成するに至つた。
For example, in the crude side chain chlorinated product of 2-methylnaphthalene, 2-chloromethylnaphthalene (side chain monochlorinated product, boiling point 168-169°C/20m7nHg) and 1-
Chloro-2-methylnaphthalene (nuclear chloride, boiling point 16
It is impossible to separate and purify 2-chloromethylnaphthalene by distillation and rectification because its boiling point is almost the same as that of 2-chloromethylnaphthalene (8° C./21 mmHg). The present inventors aimed to produce high-purity monochlorinated side chains of naphthalene derivatives by chlorinating the side chains of naphthalene derivatives. As a result of various studies on methods for separating and purifying monochlorinated products, we found that if a chlorinated side chain of a crude naphthalene derivative is reacted with an aliphatic secondary amine, only the monochlorinated product of the side chain of the naphthalene derivative reacts, resulting in a tertiary product. Amine derivatives can be generated and separated from naphthalene derivative side chain chlorinated by-products such as naphthalene derivative side chain di- and trichlorinated products and chlorinated products, and then separated into tertiary amine derivatives of naphthalene derivative side chain monochlorinated products. The present invention was completed based on the discovery that monochlorinated side chains of naphthalene derivatives can be obtained in high yield by reacting acid chlorides.

すなわち本発明は 一般式 A−CH3・・・・・・・・・(1) (式中Aは〔』〔〜=『を示し、Yは水素原子またはハ
ロゲン原子を示す。
That is, the present invention is based on the general formula A-CH3 (1) (wherein A represents [''[~='', and Y represents a hydrogen atom or a halogen atom].

)で表わされるナフタレン誘導体を側鎖塩素化して生成
する一般式(式中Aは前記と同一の意味を示す。
) is produced by chlorinating the side chain of a naphthalene derivative represented by the general formula (wherein A has the same meaning as above).

)で表わされるナフタレン誘導体側鎖モノ塩素化物を分
離精製する方法において1上記一般式(1)で表わされ
るナフタレン誘導体を側鎖塩素化して得られた粗ナフタ
レン誘導体側鎖塩素化物に一般式(式中Rおよびwは互
いに同一かまたは異なる低級アルキル基を示す。
) In a method for separating and purifying a side chain monochlorinated product of a naphthalene derivative represented by the general formula R and w are the same or different lower alkyl groups.

)で表わされる脂肪族第二級アミンを反応させ一般式(
式中R.R′およびAは前記と同一の意味を示す。
) is reacted with an aliphatic secondary amine represented by the general formula (
In the formula R. R' and A have the same meanings as above.

)で表わされる第三級アミン誘導体を生成させ単離する
第1程第1程で得られた上記一般式()で表わ される第三級アミン誘導体と一般式 (式中Bは低級アルコキシ基または ぞ −で表わされるフエニル基を示す。
) The tertiary amine derivative represented by the general formula () obtained in the first step is combined with the tertiary amine derivative represented by the general formula (where B is a lower alkoxy group or zo indicates a phenyl group represented by -.

zはハロゲン原子、低級アルキル基、低級アルコキシ基
、ニトロ基またはシアノ基を示し、nは011、2また
は3を示し、nは2または3である場合にはZは互いに
異なる基であつてもよい。
z represents a halogen atom, lower alkyl group, lower alkoxy group, nitro group or cyano group, n represents 011, 2 or 3, and when n is 2 or 3, even if Z is a different group from each other, good.

)で表わされる酸クロリドを反応させ、上記一般式()
で表わされるナフタレン誘導体側鎖モノ塩素化物を分離
する第2工程からなることを特徴とする粗ナフタレン誘
導体側鎖塩素化物から上記一般式()で表わされるナフ
タレン誘導体側鎖モノ塩素化物を分離精製する方法であ
る。
) is reacted with the acid chloride represented by the above general formula ().
Separating and purifying the naphthalene derivative side chain monochlorinated product represented by the above general formula () from the crude naphthalene derivative side chain chlorinated product, which is characterized by a second step of separating the naphthalene derivative side chain monochlorinated product represented by It's a method.

本発明を図に示すと次の通りである。The present invention is illustrated as follows.

本発明の第1工程は無溶媒中または有機溶媒中で粗ナフ
タリン誘導体側鎖塩素化物と一般式()で表わされる脂
肪族第二級アミンとを反応させ一般式()で表わされる
第三級アミン誘導体を得、ついで酸を加えて第三級アミ
ン誘導体の酸性塩を得、これを含有する水層とナフタレ
ン誘導体側鎖ジおよびトリ塩素化物および核塩素化物等
のナフタレン誘導体側鎖塩素化副生物を含有する有機層
とを分液し、得られた水層をアルカリ水溶液で中和した
後、水不溶の有機溶媒で抽出を行ない、ついで溶媒を留
去して一般式()で表わされる第三級アミン誘導体を単
離することからなる。
The first step of the present invention is to react a chlorinated side chain of a crude naphthalene derivative with an aliphatic secondary amine represented by the general formula () in a solvent-free or organic solvent to obtain a tertiary amine represented by the general formula (). An amine derivative is obtained, and then an acid is added to obtain an acid salt of a tertiary amine derivative, and an aqueous layer containing this and a chlorinated side chain of a naphthalene derivative such as di- and trichlorinated products and nuclear chlorinated products of the naphthalene derivative side chain are separated. After separating the organic layer containing living organisms and neutralizing the resulting aqueous layer with an alkaline aqueous solution, extraction is performed with a water-insoluble organic solvent, and then the solvent is distilled off to form a compound represented by the general formula (). It consists of isolating a tertiary amine derivative.

本発明の方法において用いる粗ナフタレン誘導体側鎖塩
素化物は一般式(1)で表わされるナフタレン誘導体、
例えば、ナフタレン、メチルナフタレン、クロロ−メチ
ルナフタレン、またはプロモーメチルナフタレン等を側
鎖塩素化したものであり、側鎖モノ塩素化物のほかに側
鎖ジおよびトトリ塩素化物および核塩素化物等の側鎖塩
素化副生物を含むものである。また、本発明の方法にお
いて用いる一般式()で表わされる脂肪族第二級アミン
は例えばジメチルアミン、ジエチルアミン、ジプロピル
アミン、ジブチルアミン、エチルメチルアミン、エチル
プロピルアミン、ブチルメチルアミン、ブチルエチルア
ミン、ブチルプロピルアミンおよびメチルプロピルアミ
ン等である。
The crude naphthalene derivative side chain chlorinated product used in the method of the present invention is a naphthalene derivative represented by general formula (1),
For example, side chain chlorination of naphthalene, methylnaphthalene, chloro-methylnaphthalene, or promomethylnaphthalene, etc. In addition to side chain monochlorinated products, side chain di- and totrichlorinated products and side chain chlorinated products such as nuclear chlorinated products are used. Contains chlorinated by-products. Further, aliphatic secondary amines represented by the general formula () used in the method of the present invention include, for example, dimethylamine, diethylamine, dipropylamine, dibutylamine, ethylmethylamine, ethylpropylamine, butylmethylamine, butylethylamine, These include butylpropylamine and methylpropylamine.

脂肪族第二級アミンの使用量は粗ナフタレン誘導体側鎖
塩素化物中に含まれるナフタレン誘導体側鎖モノ塩素化
物1モルに対し1モル以上使用すればいかなる量を使用
しても反応に支障はないが、好ましくは1.0〜1,1
モル使用するのが適当である。
The amount of aliphatic secondary amine to be used is 1 mol or more per 1 mol of the monochlorinated side chain of the naphthalene derivative contained in the chlorinated side chain of the crude naphthalene derivative, and no problem will occur in the reaction no matter what amount is used. but preferably 1.0 to 1.1
It is appropriate to use moles.

粗ナフタレン誘導体側鎖塩素化物と脂肪族第二級アミン
との反応は無溶媒中または有機溶媒中で、両者を混合し
加熱するかまたはせずに撹拌して行なう。
The reaction between the side chain chlorinated product of the crude naphthalene derivative and the aliphatic secondary amine is carried out by mixing the two and stirring with or without heating, in the absence of a solvent or in an organic solvent.

反応は無溶媒中でも十分進行するが、通常は水不溶の有
機溶媒中で行なうのが好ましい。水不溶の有機溶媒とし
てはベンゼン、トルエンキシレン等の芳香族炭化水素類
、クロロベンゼン、クロロトルエン等のハロゲン置換芳
香族炭化水素類、n−ヘキサン、シクロヘキサン等の脂
肪族炭化水素類およびクロロホルヘジクロロメタン、ジ
クロロエタン、ジクロロプロパン、トリクレン、四塩化
炭素等のハロゲン置換脂肪族炭化水素類、ジエチルエー
テル、ジイソプロピルエーテル等のエーテル類があげら
れる。反応温度は−20℃〜150℃好ましくはO℃〜
80℃が適当である。
Although the reaction proceeds satisfactorily even in the absence of a solvent, it is usually preferable to carry out the reaction in a water-insoluble organic solvent. Examples of water-insoluble organic solvents include aromatic hydrocarbons such as benzene and toluene-xylene, halogen-substituted aromatic hydrocarbons such as chlorobenzene and chlorotoluene, aliphatic hydrocarbons such as n-hexane and cyclohexane, and chloroforhedichloromethane. Examples include halogen-substituted aliphatic hydrocarbons such as dichloroethane, dichloropropane, tricrene, and carbon tetrachloride, and ethers such as diethyl ether and diisopropyl ether. The reaction temperature is -20°C to 150°C, preferably 0°C to
80°C is suitable.

また反応時間は1時間〜8時間好ましくは2時間〜5時
間が適当である。
The reaction time is suitably 1 hour to 8 hours, preferably 2 hours to 5 hours.

この粗ナフタレン誘導体側鎖塩素化物と脂肪族第二級ア
ミンとの反応では粗ナフタレン誘導体側鎖塩素化物中の
側鎖モノ塩素化物のみが脂肪族第二級アミンと反応して
一般式()で表わされる第三級アミン誘導体を生成し、
側鎖ジおよびトリ塩素化物、および核塩素化物等のナフ
タレン誘導体側鎖塩素化副生物は反応しない。
In this reaction between the chlorinated side chain of the crude naphthalene derivative and the aliphatic secondary amine, only the monochlorinated side chain of the chlorinated side chain of the crude naphthalene derivative reacts with the aliphatic secondary amine, resulting in the general formula (). producing a tertiary amine derivative represented by
Naphthalene derivative side chain chlorination by-products such as side chain di- and trichlorides and nuclear chlorides do not react.

反応終了後、生成した第三級アミン誘導体の分離は得ら
れた反応混合物に酸を加えて酸性にして分液する。
After the reaction is completed, the generated tertiary amine derivative is separated by adding an acid to the resulting reaction mixture to make it acidic and separate the mixture.

第三級アミン誘導体は酸性塩として水層に溶解し、ナフ
タレン誘導体側鎖ジおよびトリ塩素化物、および核塩素
化物等のナフタレン誘導体側鎖塩素化副生物は有機層に
溶解しているので、両層を分液することによつて第三級
アミン誘導体とナフタレン誘導体側鎖塩素化副生物とを
簡単に分離できる。ここで用いる酸としては塩酸、硫酸
、硝酸等の鉱酸類、ギ酸、酢酸、プロピオン酸等の有機
酸類があげられ、これらは水溶液として使用するのが好
ましい。
Tertiary amine derivatives are dissolved in the aqueous layer as acid salts, and side chain chlorinated by-products of naphthalene derivatives, such as di- and trichlorinated naphthalene derivatives and nuclear chlorides, are dissolved in the organic layer. By separating the layers, the tertiary amine derivative and the side chain chlorinated by-product of the naphthalene derivative can be easily separated. Examples of acids used here include mineral acids such as hydrochloric acid, sulfuric acid, and nitric acid, and organic acids such as formic acid, acetic acid, and propionic acid, and these are preferably used in the form of an aqueous solution.

酸の使用量は脂肪族第二級アミン1モルに対し1モル以
上好ましくは1.05〜1,15モルが適当である。分
液によつて得られた水層はアルカリ水溶液を加えて中和
した後、水不溶の有機溶媒を加えて溶媒抽出を行ない、
ついで得られた有機溶媒溶液から有機溶媒を留去するこ
とによつて一般式()で表わされる第三級アミン誘導体
を単離できる。
The amount of acid used is suitably 1 mol or more, preferably 1.05 to 1.15 mol, per 1 mol of aliphatic secondary amine. The aqueous layer obtained by separation is neutralized by adding an alkaline aqueous solution, and then a water-insoluble organic solvent is added to perform solvent extraction.
The tertiary amine derivative represented by the general formula () can then be isolated by distilling off the organic solvent from the obtained organic solvent solution.

ここで用いるアルカリ水溶液としては水酸化カリウム、
水酸化ナトリウム、水酸化カルシウム、炭酸カリおよび
炭酸ナトリウム等の水溶液があげられる。また、ここで
用いる水不溶の有機溶媒としてはベンゼン、トルエン、
キシレン等の芳香族炭化水素類、クロロベンゼン、クロ
ロトルエン等のハロゲン置換芳香族炭化水素類、n−ヘ
キサン、シクロヘキサン等の脂肪族炭化水素類およびク
ロロホルム、ジクロロメタン、ジクロロエタン、ジクロ
ロプロパン、トリクレン、四塩化炭素等のハロゲン置換
脂肪族炭化水素類、ジエチルエーテル、ジイソプロピル
エーテル等のエーテル類があげられる。
The alkaline aqueous solution used here is potassium hydroxide,
Examples include aqueous solutions of sodium hydroxide, calcium hydroxide, potassium carbonate, sodium carbonate, and the like. In addition, water-insoluble organic solvents used here include benzene, toluene,
Aromatic hydrocarbons such as xylene, halogen-substituted aromatic hydrocarbons such as chlorobenzene and chlorotoluene, aliphatic hydrocarbons such as n-hexane and cyclohexane, and chloroform, dichloromethane, dichloroethane, dichloropropane, trichlene, and carbon tetrachloride. and ethers such as diethyl ether and diisopropyl ether.

本発明の第2工程は無溶媒中または有機溶媒中で第1工
程において得られた一般式()で表わされる第三級アミ
ン誘導体と一般式(V)で表わされる酸クロリドを反応
させ生成した一般式()で表わされるナフタレン誘導体
側鎖モノ塩素化物を単離することからなる。
The second step of the present invention is produced by reacting the tertiary amine derivative represented by the general formula () obtained in the first step with the acid chloride represented by the general formula (V) in a solvent-free or organic solvent. The method consists of isolating a side chain monochlorinated naphthalene derivative represented by the general formula ().

本発明の方法において用いる一般式()で表わされる酸
クロリドとしては一般式基を示す。
The acid chloride represented by the general formula () used in the method of the present invention includes a general formula group.

)で表わされるクロルギ酸エステル、 または一般式 (式中ビは Dで表わされるフエニル 基を示し、Zおよびnは前記と同じ意味をもつ。) chloroformic acid ester, or general formula (In the formula, Bi is phenyl represented by D. Z and n have the same meanings as above.

)で表わされる芳香族酸クロリドである。ここで一般式
(V−)で表わされるクロルギ酸エステルとしてはR/
′がメチル基、エチル基プロピル基およびブチル基等の
低級アルキル基を有するものである。
) is an aromatic acid chloride represented by Here, as the chloroformic acid ester represented by the general formula (V-), R/
' has a lower alkyl group such as a methyl group, an ethyl group, a propyl group, or a butyl group.

また、一般式(V−)で表わされる芳香族酸クロリドと
してはZがフツ素、塩素、臭素、ヨウ素等のハロゲン原
子、メチル基、エチル基、プロピル基およびブチル基等
の低級アルキル基、メトキシ基、エトキシ基、プロポキ
シ基およびブトキシ基等の低級アルコキシ基、ニトロ基
またはシアノ基を有するものであり、nがO、1、2ま
たは3でありnが2または3である場合には互いに異な
る基であつてもよいものである。一般式(V)で表わさ
れる酸クロリドとして一般式(−T)で表わされるクロ
ルギ酸エステルを用いる場合は有機溶媒中で無触媒また
は触媒の存在下、一般式()で表わされる第三級アミン
誘導体とクロルギ酸エステルとを反応させ一般式()で
表わされるナフタレン誘導体側鎖モノ塩素化物と一般式
()で表わされるカルバミン酸エステル(B=B″0−
)を含む反応混合物を得、これに酸を加えてカルバミン
酸エステルを一般式()で表わされる脂肪族第二級アミ
ンとアルコールおよび炭酸ガスに加水分解した後、蒸留
等の常法の操作により目的とするナフタレン誘導体側鎖
モノ塩素化物を分離精製できる。第三級アミン誘導体と
クロルギ酸エステルと反応は有機溶媒中、無触媒または
酸触媒の存在下で両者を混合し、加熱するかまたはせず
に攪拌して行なう。
In addition, in the aromatic acid chloride represented by the general formula (V-), Z is a halogen atom such as fluorine, chlorine, bromine, or iodine, a lower alkyl group such as methyl group, ethyl group, propyl group, or butyl group, or methoxy groups, lower alkoxy groups such as ethoxy groups, propoxy groups and butoxy groups, nitro groups or cyano groups, and when n is O, 1, 2 or 3 and n is 2 or 3, they are different from each other. It may also be a group. When a chloroformic acid ester represented by the general formula (-T) is used as the acid chloride represented by the general formula (V), a tertiary amine represented by the general formula () is prepared in an organic solvent without a catalyst or in the presence of a catalyst. The derivative and chloroformic acid ester are reacted to form a naphthalene derivative side chain monochlorinated product represented by the general formula () and a carbamate ester represented by the general formula () (B=B″0-
) is obtained, an acid is added to this to hydrolyze the carbamate ester into an aliphatic secondary amine represented by the general formula (), alcohol and carbon dioxide gas, and then by conventional operations such as distillation. The desired naphthalene derivative side chain monochlorinated product can be separated and purified. The reaction between the tertiary amine derivative and the chloroformic acid ester is carried out by mixing the two in an organic solvent without a catalyst or in the presence of an acid catalyst, and stirring the mixture with or without heating.

クロルギ酸エステルの使用量は第三級アミン誘導体1モ
ルに対し1モル使用するのが好ましいが、1モル以上使
用しても反応に支障はない。有機溶媒としてはベンゼン
、トルエン、キシレン等の芳香族炭化水素類、クロロベ
ンゼン、クロロトルエン等のハロゲン置換芳香族炭化水
素類、nヘキサン、シクロヘキサン等の脂肪族炭化水素
類およびクロロホルム、ジクロロメタン、ジクロロエタ
ン、ジクロロプロパン、トリクレン、四塩化炭素等の・
・ロゲ7置換脂肪族炭化水素類、ジエチルエーテル、ジ
イソプロピルエーテル等のエーテル類があげられる。反
応温度は−3『C〜150℃、好ましくはO℃〜120
℃が適当である。
The amount of chloroformic acid ester to be used is preferably 1 mole per mole of the tertiary amine derivative, but even if it is used in excess of 1 mole, there will be no problem with the reaction. Examples of organic solvents include aromatic hydrocarbons such as benzene, toluene, and xylene, halogen-substituted aromatic hydrocarbons such as chlorobenzene and chlorotoluene, aliphatic hydrocarbons such as n-hexane and cyclohexane, and chloroform, dichloromethane, dichloroethane, and dichloromethane. Chloropropane, trichlene, carbon tetrachloride, etc.
-Rogge 7-substituted aliphatic hydrocarbons, ethers such as diethyl ether, diisopropyl ether, etc. The reaction temperature is -3°C to 150°C, preferably 0°C to 120°C.
°C is appropriate.

反応は無触媒でも十分進行するが、酸触媒または亜鉛触
媒を用いれば反応が促進され反応時間を短縮できる。酸
触媒としては塩酸、硫酸、リン酸等の鉱酸またはギ酸、
酢酸、プロピオン酸等の有機酸が適しており、この酸触
媒の使用量は第三級アミン誘導体1モルに対し0.00
01モル〜0.5モル好ましくは0.001モル〜0.
2モルが適当である。また亜鉛触媒としては塩化亜鉛、
臭化亜鉛、酸化亜鉛、硫化亜鉛、水酸化亜鉛、炭酸亜鉛
、硫酸亜鉛、硝酸亜鉛、リン酸亜鉛、酢酸亜鉛、安臭香
酸亜鉛等の亜鉛化合物が適しており、使用量は第三級ア
ミン誘導体1モルに対し0.02モル〜0.1モル好ま
しくは0.04〜0.06モルが適当である。第三級ア
ミン誘導体とクロルギ酸エステルとを反応させ得られた
一般式()で表わされるカルバミン酸エステル(B−R
1′O−)の加水分解は、一般式()で表わされるナフ
タレン誘導体側鎖モノ塩素化物とカルバミン酸エステル
を含む反応混合物に塩酸、硫酸、硝酸等の鉱酸水溶液ま
たはギ酸、酢酸、プロピオン酸等の有機酸水溶液を加え
、O℃〜100℃好ましくは2『C〜80℃で行なう。
Although the reaction proceeds satisfactorily without a catalyst, the reaction can be accelerated and the reaction time can be shortened by using an acid catalyst or a zinc catalyst. As acid catalysts, mineral acids such as hydrochloric acid, sulfuric acid, phosphoric acid, or formic acid,
Organic acids such as acetic acid and propionic acid are suitable, and the amount of this acid catalyst used is 0.00 per mole of tertiary amine derivative.
01 mole to 0.5 mole, preferably 0.001 mole to 0.01 mole.
2 moles is suitable. In addition, zinc chloride,
Zinc compounds such as zinc bromide, zinc oxide, zinc sulfide, zinc hydroxide, zinc carbonate, zinc sulfate, zinc nitrate, zinc phosphate, zinc acetate, zinc benbrozoate, etc. are suitable, and the amount used is tertiary. A suitable amount is 0.02 mol to 0.1 mol, preferably 0.04 to 0.06 mol, per mol of the amine derivative. Carbamate ester (B-R
Hydrolysis of 1'O-) is carried out by adding an aqueous mineral acid solution such as hydrochloric acid, sulfuric acid, or nitric acid, or formic acid, acetic acid, or propionic acid to a reaction mixture containing a monochlorinated side chain of the naphthalene derivative represented by the general formula () and a carbamate ester. The reaction is carried out at 0°C to 100°C, preferably 2°C to 80°C.

加水分解反応の開始とともに炭酸ガスが発生する。加水
分解反応の終了後、反応系はナフタレン誘導体側鎖モノ
塩素化物を含む有機層とカルバミン酸エステルが加水分
解して生成したアルコールおよび脂肪族第二級アミンの
鉱酸または有機酸塩を含む水層の二層に分離し、両層を
分液することによつてナフタレン誘導体側鎖モノ塩素化
物は有機溶媒とともに分離することができ、さらに蒸留
等の常法の操作によつて目的とするナフタレン誘導体側
鎖モノ塩素化物を容易に収率よく分離精製できる。一方
残る水層は中和し、抽出、蒸留等の操作を行なえば加水
分解によつて生成した脂肪族第二級アミンを単離できる
。また、一般式(V)で表わされる酸クロリドとして一
般式(V−)で表わされる芳香族酸クロリドを用いる場
合には、無溶媒中または有機溶媒中で無触媒または触媒
の存在下、一般式()で表わされる第三級アミン誘導体
と芳香族クロリドを反応させ、一般式()で表わされる
ナフタレン誘導体側鎖モノ塩素化物と一般式()で表わ
される酸アミドを含む反応混合物を得、これを蒸留等の
常法による操作により目的とするナフタレン誘導体側鎖
モノ塩素化物を分離精製できる。
Carbon dioxide gas is generated with the start of the hydrolysis reaction. After the hydrolysis reaction is completed, the reaction system contains an organic layer containing a monochlorinated side chain of a naphthalene derivative, an alcohol produced by hydrolysis of a carbamate ester, and water containing a mineral acid or an organic acid salt of an aliphatic secondary amine. By separating the two layers and separating both layers, the side chain monochlorinated product of the naphthalene derivative can be separated together with the organic solvent, and then the desired naphthalene can be separated by conventional operations such as distillation. Derivative side chain monochlorinated products can be easily separated and purified with good yield. On the other hand, the remaining aqueous layer is neutralized, and the aliphatic secondary amine produced by hydrolysis can be isolated by performing operations such as extraction and distillation. In addition, when using an aromatic acid chloride represented by the general formula (V-) as the acid chloride represented by the general formula (V), the general formula A tertiary amine derivative represented by () is reacted with an aromatic chloride to obtain a reaction mixture containing a naphthalene derivative side chain monochlorinated product represented by general formula () and an acid amide represented by general formula (). The desired side chain monochlorinated naphthalene derivative can be separated and purified by operations such as distillation using conventional methods.

第三級アミン誘導体と芳香族酸クロリドとの反応は無溶
媒中または有機溶媒中で無触媒または触媒の存在下両者
を混合し加熱攪拌して行なう。芳香族酸クロリドの使用
量は第三級アミン誘導体1モルに対し1モル以上使用し
ても反応に支障はないが好ましくは1モルが適当である
。反応は通常は無溶媒中で行なうが、有機溶媒中で行な
つても反応に支障はない。有機溶媒としてはベンゼン、
トルエン、キシレン等の芳香族炭化水素類およびクロロ
ベンゼン、ジクロロベンゼン、クロロトルエン、ジクロ
ロトルエン等のハロゲン置換芳香族炭化水素類があげら
れる。反応温度は30℃〜300℃好ましくは70℃〜
250℃が適当である。
The reaction between the tertiary amine derivative and the aromatic acid chloride is carried out by mixing the two in the absence of a catalyst or in the presence of a catalyst in a solvent-free or organic solvent, and heating and stirring the mixture. The aromatic acid chloride may be used in an amount of 1 mole or more per mole of the tertiary amine derivative without any problem in the reaction, but preferably 1 mole is appropriate. The reaction is usually carried out without a solvent, but the reaction can be carried out in an organic solvent without any problem. Benzene as an organic solvent,
Examples include aromatic hydrocarbons such as toluene and xylene, and halogen-substituted aromatic hydrocarbons such as chlorobenzene, dichlorobenzene, chlorotoluene, and dichlorotoluene. The reaction temperature is 30°C to 300°C, preferably 70°C to
250°C is suitable.

反応は無触媒でも十分進行するが、触媒を用いれば反応
が促進され反応時間を大幅に短縮できる。触媒としては
塩化亜鉛、臭化亜鉛、酸化亜鉛、硫化亜鉛、水酸化亜鉛
、炭酸亜鉛、硫酸亜鉛、硝酸亜鉛、リン酸亜鉛、酢酸亜
鉛、安息香酸亜鉛等の亜鉛化合物が適しており、使用量
は第三級アミン誘導体1モルに対し0.02モル〜0.
1モル好ましくは0.04モル〜0.06モルが適当で
ある。第三級アミン誘導体と芳香族酸クロリドを反応さ
せ得られた反応混合物はそのまま蒸留等の常法の操作に
よつて目的とするナフタレン誘導体側鎖モノ塩素化物を
容易に収率よく分離精製できる。
Although the reaction proceeds satisfactorily without a catalyst, the use of a catalyst accelerates the reaction and significantly shortens the reaction time. Suitable catalysts include zinc compounds such as zinc chloride, zinc bromide, zinc oxide, zinc sulfide, zinc hydroxide, zinc carbonate, zinc sulfate, zinc nitrate, zinc phosphate, zinc acetate, and zinc benzoate. is 0.02 mol to 0.02 mol to 1 mol of tertiary amine derivative.
1 mol, preferably 0.04 mol to 0.06 mol, is suitable. The reaction mixture obtained by reacting a tertiary amine derivative with an aromatic acid chloride can be directly subjected to a conventional operation such as distillation to easily separate and purify the desired naphthalene derivative side chain monochlorinated product with good yield.

またナフタレン誘導体側鎖モノ塩素化物を分離精製した
残渣はさらに高真空蒸留等の常法の操作によつて芳香族
酸アミドを単離できる。次に本発明の方法における特徴
とその利点について説明する。
Further, the aromatic acid amide can be isolated from the residue obtained by separating and purifying the side chain monochlorinated product of the naphthalene derivative by a conventional operation such as high vacuum distillation. Next, the features and advantages of the method of the present invention will be explained.

本発明の方法における特徴はナフタレン誘導体を側鎖塩
素化して得られるナフタレン誘導体側鎖モノ、ジおよび
トリ塩素化物および核塩素化物を含む粗ナフタレン誘導
体側鎖塩素化物からナフタレン誘導体側鎖モノ塩素化物
を容易に高収率、高純度で分離精製できることであり、
農薬、医薬等の製造中間体として有用なナフタレン誘導
体側鎖モノ塩素化物を製造する工程において利点を生じ
る。ナフタレン誘導体側鎖モノ塩素化物は対応するナフ
タレン誘導体の側鎖塩素化により製造されるが、この際
副生物としてナフタレン誘導体側鎖モノ塩素化物と近似
の沸点を有するナフタレン誘導体側鎖ジおよびトリ塩素
化物および核塩素化物が生成する。
The feature of the method of the present invention is to obtain monochlorinated naphthalene derivative side chains from crude naphthalene derivative side chain chlorinated products, including mono-, di- and tri-chlorinated products and nuclear chlorinated products obtained by side-chain chlorination of naphthalene derivatives. It can be easily separated and purified with high yield and high purity.
Advantages arise in the process of producing side chain monochlorinated naphthalene derivatives useful as intermediates in the production of agricultural chemicals, medicines, etc. Side chain monochlorinated naphthalene derivatives are produced by side chain chlorination of the corresponding naphthalene derivatives, and in this case, side chain di- and trichlorinated naphthalene derivatives having a boiling point similar to that of the side chain monochlorinated naphthalene derivatives are produced as by-products. and nuclear chlorides are produced.

従来、これらの副生物を含む粗ナフタレン誘導体側鎖塩
素化物からのナフタレン誘導体側鎖モノ塩素化物の分離
精製は蒸留または精留による方法で行なつている。しか
し、蒸留または精留による分離精製法ではナフタレン誘
導体側鎖モノ塩素化物と前記副生物との沸点差が小さい
ために分離精製がきわめて困難であり、これらの方法で
は完全に分離精製を行なうことが容易でないため得られ
るナフタレン誘導体側鎖モノ塩素化物は低純度、低収率
であつた。しかし、ここで本発明の方法を実施すればナ
フタレン誘導体を側鎖塩素化して得られた粗ナフタレン
誘導体側鎖塩素化物からナフタレン誘導体側鎖モノ塩素
化物を前記副生物と容易に分離精製できしかも高純度、
高収率で得られるという利点を生じる。
Conventionally, separation and purification of monochlorinated side chains of naphthalene derivatives from crude chlorinated side chains of naphthalene derivatives containing these by-products has been carried out by distillation or rectification. However, separation and purification using distillation or rectification is extremely difficult due to the small boiling point difference between the side chain monochlorinated product of the naphthalene derivative and the above-mentioned by-product, and these methods cannot completely separate and purify the product. Since this is not easy, the side chain monochlorinated naphthalene derivatives obtained had low purity and low yield. However, if the method of the present invention is carried out here, the side chain monochlorinated product of the naphthalene derivative can be easily separated and purified from the above-mentioned by-products from the crude naphthalene derivative side chain chlorinated product obtained by side chain chlorination of the naphthalene derivative. purity,
This gives rise to the advantage of being obtained in high yields.

本発明の方法で一般式(V)で表わされる酸クロリドと
して一般式(V−1)で表わされるクロルギ酸エステル
を用いて実施した場合はナフタレン誘導体側鎖モノ塩素
化物のほかに、用いた一般式()で表わされる脂肪族第
二級アミンが高収率で回収でき、さらにこれを再使用で
きるという利点があり、一般式(−)で表わされる芳香
族酸クロリドを用いて実施した場合は、ナフタレン誘導
体側鎖モノ塩素化物のほかに農薬、医薬等の製造中間体
として有用な芳香族酸アミドを高収率で単離製造できる
という利点がある。
When carrying out the method of the present invention using a chloroformic acid ester represented by the general formula (V-1) as the acid chloride represented by the general formula (V), in addition to the naphthalene derivative side chain monochlorinated product, the general It has the advantage that the aliphatic secondary amine represented by the formula () can be recovered in high yield and can be reused, and when carried out using the aromatic acid chloride represented by the general formula (-), In addition to side chain monochlorinated products of naphthalene derivatives, this method has the advantage of being able to isolate and produce aromatic acid amides, which are useful as intermediates in the production of agricultural chemicals, medicines, etc., in high yields.

以下実施例により本発明をさらに詳しく説明する。The present invention will be explained in more detail with reference to Examples below.

実施例 1(1)温度計、冷却管、滴下ロードおよび撹
拌機を備えた1,e四つロフラスコに2−メチルナフタ
レンを側鎖塩素化して得られた純度70.6%の粗2−
クロロメチルナフタレン250tおよびベンゼン300
m1を仕込み、これに撹拌下ジエチルアミン75.07
(1.03モル)を滴下した後、加温し50′Cで4時
間反応させた。
Example 1 (1) Crude 2-methylnaphthalene with a purity of 70.6% obtained by side chain chlorination of 2-methylnaphthalene in a 1,e four-bottle flask equipped with a thermometer, condenser, dropping load and stirrer.
250 tons of chloromethylnaphthalene and 300 tons of benzene
ml of diethylamine and 75.07 g of diethylamine under stirring.
(1.03 mol) was added dropwise, and the mixture was heated and reacted at 50'C for 4 hours.

ついで得られた反応液に攪拌下濃塩酸1207(1.1
5モル)を加え室温で30分反応させた。
Then, concentrated hydrochloric acid 1207 (1.1
5 mol) was added thereto and reacted for 30 minutes at room temperature.

反応終了後、得られた反応液を21分液ロードに移し分
液した。得られた水層は】O%苛性ソーダ水溶液で中和
した後、エチルエーテルを加えてN−N−ジエチル−2
−ナフチルメチルアミンを抽出し、ついで得られたエチ
ルエーテル抽出溶液を濃縮しエチルエーテルを留去して
N−N−ジエチル−2−ナフチルメチルアミン211.
07を得た。得られたN−N−ジエチル2−ナフチルメ
チルアミンをガスクロマトグラフイ一により分析した結
果、純度99.9%であり、粗2−クロロメチルナフタ
レン中の2一クロロメチルナフタレンを基準とする純収
率は98.8%であつた。(2)前記(1)と同様の1
1?四つロフラスコに前記(1)で得られた純度99.
9%のN−N−ジエチル−2−ナフチルメチルアミン2
11.07(0.988モル)およびベンゼン200m
1を仕込み、これに攪拌下室温でクロルギ酸メチル1。
After the reaction was completed, the obtained reaction solution was transferred to a 21-separation load and separated. The obtained aqueous layer was neutralized with 0% caustic soda aqueous solution, and ethyl ether was added to give N-N-diethyl-2
- Naphthylmethylamine is extracted, and the resulting ethyl ether extracted solution is concentrated and the ethyl ether is distilled off to remove N-N-diethyl-2-naphthylmethylamine 211.
I got 07. The resulting N-N-diethyl 2-naphthylmethylamine was analyzed by gas chromatography and found to have a purity of 99.9%, with a pure yield based on 2-chloromethylnaphthalene in the crude 2-chloromethylnaphthalene. The rate was 98.8%. (2) 1 similar to (1) above
1? The purity obtained in (1) above is 99.
9% N-N-diethyl-2-naphthylmethylamine 2
11.07 (0.988 mol) and benzene 200m
To this was added methyl chloroformate 1 at room temperature under stirring.

000モルを滴下した後、加温し50℃で6時間反応さ
せた。
After adding 000 mol dropwise, the mixture was heated and reacted at 50° C. for 6 hours.

ついで得られた反応液に室温で攪拌下30%硫酸水溶液
1207を加えた後、加温し50℃で炭酸ガスの発生が
終るまで反応させ加水分解した。加水分解反応終了後、
反応液を室温まで冷却した後11分液ロードに移し分液
した。
Next, 30% aqueous sulfuric acid solution 1207 was added to the obtained reaction solution at room temperature with stirring, and the mixture was heated and reacted at 50° C. until the generation of carbon dioxide gas was completed for hydrolysis. After the hydrolysis reaction is completed,
After the reaction solution was cooled to room temperature, it was transferred to an 11-minute liquid load and separated.

得られた有機層を水100m1で2回洗浄し、ついで無
水硫酸ナトリウムで乾燥した後、ベンゼンを減圧留去し
、さらに減圧蒸留を行ない沸点168〜169℃/20
m7!1Hgの2−クロロメチルナフタレン133.7
yを得た。これをガスクロマトグラフイ一により分析し
た結果純度99.7%であり、粗P−クロロ塩化ベンジ
ル中のP−クロロ塩化ベンジルを基準とする収率(回収
率)は75.5%であつた。一方、加水分解反応後、反
応液を分液して得られた水層を10%苛性ソーダ水溶液
を加えて中和した後、エチルエーテルを加えてジエチル
アミンを抽出した。
The obtained organic layer was washed twice with 100 ml of water, then dried over anhydrous sodium sulfate, and then benzene was distilled off under reduced pressure, and further vacuum distillation was performed to obtain a boiling point of 168-169°C/20°C.
m7!1 Hg of 2-chloromethylnaphthalene 133.7
I got y. Analysis of this by gas chromatography revealed that the purity was 99.7%, and the yield (recovery rate) based on P-chlorobenzyl chloride in the crude P-chlorobenzyl chloride was 75.5%. On the other hand, after the hydrolysis reaction, the aqueous layer obtained by separating the reaction solution was neutralized by adding a 10% aqueous solution of caustic soda, and then ethyl ether was added to extract diethylamine.

エチルエーテル抽出溶液は水100m1で2回洗浄し、
ついで無水硫酸ナトリウムで乾燥した後、エチルエーテ
ルを留去し、さらに蒸留を行ない沸点52〜55℃/7
60mmHgのジエチルアミン53.37(回収率71
.0%)を得た。実施例 2 実施例1の前記(1)と同様にして得られたN−Nジエ
チル−2−ナフチルメチルアミン211.07(0.9
88モル)、ベンゼン200m1および濃硫酸17の混
合溶液に攪拌下室温でクロルギ酸メチル1.000モル
を滴下した後、加温し50℃で4時間反応させた。
The ethyl ether extraction solution was washed twice with 100 ml of water,
Then, after drying over anhydrous sodium sulfate, ethyl ether was distilled off, and further distillation was performed to reduce the boiling point to 52-55°C/7.
Diethylamine 53.37 at 60 mmHg (recovery 71
.. 0%) was obtained. Example 2 N-N diethyl-2-naphthylmethylamine 211.07 (0.9
88 mol), 200 ml of benzene, and 17 ml of concentrated sulfuric acid were added dropwise to a mixed solution of 1.000 mol of methyl chloroformate at room temperature while stirring, and then heated and reacted at 50° C. for 4 hours.

反応終了後、実施例1と同様に操作して2−クロロメチ
ルナフタレン136.57およびジエチルアミン52.
77(回収率70.2%)を得た。
After the reaction was completed, the same procedure as in Example 1 was carried out to obtain 136.57% of 2-chloromethylnaphthalene and 52.57% of diethylamine.
77 (recovery rate 70.2%) was obtained.

得られた2−クロロメチルナフタレンをガスクロマトグ
ラフイ一により分析した結果、純度99.8%であり、
粗2−メチルナフタレン側鎖モノ塩素化物中の2−クロ
ルメチルナフタレンを基準とする収率(回収率)は77
.2%であつた。実施例 3 (1)実施例1および実施例2と同様にして1−クロロ
−2−クロロメチルナフタレン1.0モルを含有する粗
1−クロロ−2−クロロメチルナフタレンとジエチルア
ミン1.0モルとをクロロトル壬ン300m1中で反応
させ第三級アミン誘導体を得た。
The resulting 2-chloromethylnaphthalene was analyzed by gas chromatography and found to have a purity of 99.8%.
The yield (recovery rate) based on 2-chloromethylnaphthalene in the crude 2-methylnaphthalene side chain monochlorinated product is 77.
.. It was 2%. Example 3 (1) In the same manner as in Example 1 and Example 2, crude 1-chloro-2-chloromethylnaphthalene containing 1.0 mol of 1-chloro-2-chloromethylnaphthalene and 1.0 mol of diethylamine were prepared. was reacted in 300 ml of chlorotol to obtain a tertiary amine derivative.

(2)実施例1および実施例2と同様に操作して前記(
1)で得られた第三級アミン誘導体とクロルギ酸エステ
ル1.0モルとをベンゼン200m1中で濃塩酸を加え
て反応させ、得られた反応溶液を加水分解し、目的とす
る1−クロロ−2−クロロメチルナフタレンを得た。
(2) Perform the same operation as in Example 1 and Example 2 to
The tertiary amine derivative obtained in step 1) and 1.0 mol of chloroformic acid ester are reacted in 200 ml of benzene by adding concentrated hydrochloric acid, and the resulting reaction solution is hydrolyzed to obtain the desired 1-chloro- 2-chloromethylnaphthalene was obtained.

得られた結果を表−1及び2に示した。The obtained results are shown in Tables 1 and 2.

尚、(1)および(2)での純度はガスクロマトグラフ
ィ一による分析結果であり、純収率は粗1−クロロ−2
−クロロメチルナフタレン中の純1クロロ−2−クロロ
メチルナフタレンを基準とする収率である。
In addition, the purity in (1) and (2) is the result of analysis by gas chromatography, and the pure yield is crude 1-chloro-2.
-Yield based on pure 1-chloro-2-chloromethylnaphthalene in chloromethylnaphthalene.

実施例 4 (1)実施例1の前記(1)の方法と同様にして粗2ク
ロロメチルナフタレンとジエチルアミンからN−N−ジ
エチル−2−ナフチルメチルアミン211.0tを得た
Example 4 (1) 211.0 t of N-N-diethyl-2-naphthylmethylamine was obtained from crude 2chloromethylnaphthalene and diethylamine in the same manner as in the method (1) of Example 1 above.

純度99.9%oこのものの純収率は98.8%であつ
た。(2)前記(1)と同様の装置を備えた500m1
四つ口フラスコに前記(1)で得られたN−N−ジエチ
ルー2−ナフチルメチルアミン211,07(0.98
8モル)およびO−トルイル酸クロリド0.998モル
を仕込み、攪拌下加熱し180℃〜200℃で20時間
反応させた。
The purity was 99.9%, and the pure yield was 98.8%. (2) 500m1 equipped with the same equipment as in (1) above
N-N-diethyl-2-naphthylmethylamine 211,07 (0.98
8 mol) and 0.998 mol of O-toluic acid chloride were charged, heated under stirring, and reacted at 180°C to 200°C for 20 hours.

反応終了後、得られた反応液を減圧蒸留し沸点168℃
〜169℃/20mmHgの2−クロロメチルナフタレ
ン139.27を得た。
After the reaction is complete, the resulting reaction solution is distilled under reduced pressure to a boiling point of 168°C.
139.27 of 2-chloromethylnaphthalene was obtained at ˜169° C./20 mmHg.

これをガスクロマトグラフイ一により分析した結果、純
度99.8%であり粗2−クロロメチルナフタレン中の
2−クロロメチルナフタレンを基準とする収率(回収率
)は78.7%であつた。実施例 5(1)実施例3の
前記(1)と同様にして粗1−クロロ−2−クロロメチ
ルナフタレン(純度70.4%)3007(純1−クロ
ロ−2−クロロメチルナフタレン含量1モル)とジエチ
ルアミン75.07(1.03モル)とから純度99.
8%のN−Nジエチル−1−クロロ−2−ナフチルメチ
ルアミン245.87を得た。
Analysis of this by gas chromatography revealed that the purity was 99.8% and the yield (recovery rate) based on 2-chloromethylnaphthalene in crude 2-chloromethylnaphthalene was 78.7%. Example 5 (1) Crude 1-chloro-2-chloromethylnaphthalene (purity 70.4%) 3007 (purity 1-chloro-2-chloromethylnaphthalene content: 1 mol) in the same manner as in (1) of Example 3. ) and diethylamine 75.07 (1.03 mol) with a purity of 99.
245.87 of 8% N-N diethyl-1-chloro-2-naphthylmethylamine was obtained.

純収率98.8%o(2)前記(1)で得られたN−N
−ジエチル−1−ク口ロー2−ナフチルアミン245.
87(0.988モル)および塩化亜鉛6.87(0.
05モル)の混合溶液に攪拌下加熱して140〜160
℃で1.5時間かけて安息香酸クロリド138.97(
0.988モル)を滴下し反応させた。反応は安息香酸
クロリドの滴下とともに進行し、滴下終了時に完結する
。反応終了後、得られた反応液を減圧蒸留し沸点173
〜17『C/20mmHgの1−クロロ2−クロロメチ
ルナフタレン192.6yを得た。
Pure yield 98.8% o (2) N-N obtained in (1) above
-diethyl-1-kuro-2-naphthylamine 245.
87 (0.988 mol) and zinc chloride 6.87 (0.988 mol).
A mixed solution of 0.05 mol) was heated with stirring to give a
Benzoic acid chloride 138.97 (
0.988 mol) was added dropwise to react. The reaction proceeds as the benzoyl chloride is added dropwise, and is completed at the end of the dropwise addition. After the reaction is complete, the resulting reaction solution is distilled under reduced pressure to a boiling point of 173.
192.6y of 1-chloro2-chloromethylnaphthalene with C/20 mmHg was obtained.

得られた1−クロロ−2−クロロ−メチルナフタレンを
ガスクロマトグラフイにより分析した結果純度99,8
%であり粗1−クロロ−2クロロ−メチルナフタレン中
の1−クロロ2−メチルナフタレンを基準とする収率(
回収率)は91.0%であつた。また、1−クロロ−2
−クロロメチルナフタレンの蒸留残渣をさらに高真空蒸
留し沸点100℃/1mmHgのN−N−ジエチル安香
酸アミドを収率90.5%で得た。
The resulting 1-chloro-2-chloro-methylnaphthalene was analyzed by gas chromatography and found to have a purity of 99.8.
% and the yield based on 1-chloro-2-methylnaphthalene in crude 1-chloro-2-chloro-methylnaphthalene (
The recovery rate) was 91.0%. Also, 1-chloro-2
The distillation residue of -chloromethylnaphthalene was further distilled under high vacuum to obtain N-N-diethylbenzoic acid amide with a boiling point of 100° C./1 mmHg in a yield of 90.5%.

Claims (1)

【特許請求の範囲】 1 一般式 A−CH_3………( I ) (式中Aは▲数式、化学式、表等があります▼示し、Y
は水素原子またはハロゲン原子を示す。 )で表わされるナフタレン誘導体を側鎖塩素化して生成
する一般式A−CH_2Cl………(II) (式中Aは前記と同一の意味を示す。 )で表わされるナフタレン誘導体側鎖モノ塩素化物を分
離精製する方法において[1]上記一般式( I )で表
わされるナフタレン誘導体を側鎖塩素化して得られた粗
ナフタレン誘導体側鎖塩素化物に一般式▲数式、化学式
、表等があります▼………(III)(式中RおよびR′
は互いに同一かまたは異なる低級アルキル基を示す。 )で表わされる脂肪族第二級アミンを反応させ一般式▲
数式、化学式、表等があります▼………(IV)(式中R
、R′およびAは前記と同一の意味を示す。 )で表わされる第三級アミン誘導体を生成させ単離する
第一工程[2]第一工程で得られた上記一般式(IV)で
表わされる第三級アミン誘導体と一般式▲数式、化学式
、表等があります▼………(V)(式中Bは低級アルコ
キシ基または ▲数式、化学式、表等があります▼で表わされるフェニ
ル基を示す。 Zはハロゲン原子、低級アルキル基、低級アルコキシ基
、ニトロ基またはシアノ基を示し、nは0、1、2また
は3を示し、nが2または3である場合にはZは互いに
異なる基であつてもよい。 )で表わされる酸クロリドを反応させ、上記一般式(I
I)で表わされるナフタレン誘導体側鎖モノ塩素化物を
分離する第2工程からなることを特徴とする粗ナフタレ
ン誘導体側鎖塩素化物から上記一般式(II)で表わされ
るナフタレン誘導体側鎖モノ塩素化物を分離精製する方
法。 2 一般式 A−CH_3………( I ) (式中Aは▲数式、化学式、表等があります▼を示し、
Yは水素原子またはハロゲン原子を示す。 )で表わされるナフタレン誘導体を側鎖塩素化して生成
する一般式A−CH_2Cl………(II) (式中Aは前記と同一の意味を示す。 )で表わされるナフタレン誘導体側鎖モノ塩素化物を分
離精製する方法において[1]上記一般式( I )で表
わされるナフタレン誘導体を側鎖塩素化して得られた粗
ナフタレン誘導体側鎖塩素化物に一般式▲数式、化学式
、表等があります▼………(III)(式中RおよびR′
は互いに同一かまたは異なる低級アルキル基を示す。 )で表わされる脂肪族第二級アミンを反応させ一般式▲
数式、化学式、表等があります▼………(IV)(式中R
、R′およびAは前記と同一の意味を示す。 )で表わされる第三級アミン誘導体を生成させ単離する
第1工程[2]酸触媒の存在下、第1工程で得られた上
記一般式(IV)で表わされる第三級アミン誘導体と一般
式▲数式、化学式、表等があります▼………(V− I
)(式中B′は低級アルコキシ基を示す。 )で表わされる酸クロリドを反応させ、上記一般式(I
I)で表わされるナフタレン誘導体側鎖モノ塩素化物を
分離する第2工程からなることを特徴とする粗ナフタレ
ン誘導体側鎖塩素化物から上記一般式(II)で表わされ
るナフタレン誘導体側鎖モノ塩素化物を分離精製する方
法。 3 一般式 A−CH3………( I ) (式中Aは▲数式、化学式、表等があります▼を示し、
Yは水素原子またはハロゲン原子を示す。 )で表わされるナフタレン誘導体を側鎖塩素化して生成
する一般式A−CH_2Cl………(II) (式中Aは前記と同一の意味を示す。 )で表わされるナフタレン誘導体側鎖モノ塩素化物を分
離精製する方法において[1]上記一般式( I )で表
わされるナフタレン誘導体を側鎖塩素化して得られた粗
ナフタレン誘導体側鎖塩素化物に一般式▲数式、化学式
、表等があります▼………(III)(式中RおよびR′
は互いに同一かまたは異なる低級アルキル基を示す。 )で表わされる脂肪族第二級アミンを反応させ一般式▲
数式、化学式、表等があります▼………(IV)(式中R
、R′およびAは前記と同一の意味を示す。 )で表わされる第三級アミン誘導体を生成させ単離する
第1工程[2]亜鉛触媒の存在下、第1工程で得られた
上記一般式(IV)で表わされる第三級アミン誘導体と一
般式▲数式、化学式、表等があります▼………(V−I
I)(式中B″は▲数式、化学式、表等があります▼で
表わされるフェニル基を示し、Zはハロゲン原子、低級
アルキル基、低級アルコキシ基、ニトロ基またはシアノ
基を示し、nは0、1、2または3を示し、nが2また
は3である場合にはZは互いに異なる基であつてもよい
。 )で表わされる酸クロリドを反応させ、上記一般式(I
I)で表わされるナフタレン誘導体側鎖モノ塩素化物を
分離する第2工程からなることを特徴とする粗ナフタレ
ン誘導体側鎖塩素化物からなる上記一般式(II)で表わ
されるナフタレン誘導体側鎖モノ塩素化物を分離精製す
る方法。
[Claims] 1 General formula A-CH_3......(I) (In the formula, A represents ▲a mathematical formula, a chemical formula, a table, etc.▼, and Y
represents a hydrogen atom or a halogen atom. ) The general formula A-CH_2Cl produced by side chain chlorination of the naphthalene derivative represented by (II) (wherein A has the same meaning as above) In the separation and purification method, [1] The crude naphthalene derivative side chain chlorinated product obtained by side chain chlorination of the naphthalene derivative represented by the above general formula (I) has the general formula ▲ mathematical formula, chemical formula, table, etc. ▼... ...(III) (in the formula R and R'
represent lower alkyl groups that are the same or different from each other. ) is reacted with the aliphatic secondary amine represented by the general formula ▲
There are mathematical formulas, chemical formulas, tables, etc. ▼……(IV) (R in the formula
, R' and A have the same meanings as above. ) The first step of producing and isolating the tertiary amine derivative represented by [2] the tertiary amine derivative represented by the above general formula (IV) obtained in the first step and the general formula ▲ mathematical formula, chemical formula, There are tables, etc.▼......(V) (In the formula, B represents a lower alkoxy group or a phenyl group represented by ▲There are mathematical formulas, chemical formulas, tables, etc.▼.Z is a halogen atom, a lower alkyl group, a lower alkoxy group , represents a nitro group or a cyano group, n represents 0, 1, 2 or 3, and when n is 2 or 3, Z may be mutually different groups. and the above general formula (I
A second step of separating the monochlorinated side chain of the naphthalene derivative represented by I) from the chlorinated side chain of the crude naphthalene derivative represented by general formula (II) above. A method of separation and purification. 2 General formula A-CH_3……(I) (In the formula, A indicates ▲There are mathematical formulas, chemical formulas, tables, etc.▼,
Y represents a hydrogen atom or a halogen atom. ) The general formula A-CH_2Cl produced by side chain chlorination of the naphthalene derivative represented by (II) (wherein A has the same meaning as above) In the separation and purification method, [1] The crude naphthalene derivative side chain chlorinated product obtained by side chain chlorination of the naphthalene derivative represented by the above general formula (I) has the general formula ▲ mathematical formula, chemical formula, table, etc. ▼... ...(III) (in the formula R and R'
represent lower alkyl groups that are the same or different from each other. ) is reacted with the aliphatic secondary amine represented by the general formula ▲
There are mathematical formulas, chemical formulas, tables, etc. ▼……(IV) (R in the formula
, R' and A have the same meanings as above. ) The first step of producing and isolating the tertiary amine derivative represented by formula (IV) [2] In the presence of an acid catalyst, the tertiary amine derivative represented by the general formula (IV) obtained in the first step and the general Formulas▲There are mathematical formulas, chemical formulas, tables, etc.▼……(V- I
) (in the formula, B' represents a lower alkoxy group) to react the acid chloride represented by the above general formula (I
A second step of separating the monochlorinated side chain of the naphthalene derivative represented by I) from the chlorinated side chain of the crude naphthalene derivative represented by general formula (II) above. A method of separation and purification. 3 General formula A-CH3……(I) (In the formula, A indicates ▲There are mathematical formulas, chemical formulas, tables, etc.▼,
Y represents a hydrogen atom or a halogen atom. ) The general formula A-CH_2Cl produced by side chain chlorination of the naphthalene derivative represented by (II) (wherein A has the same meaning as above) In the separation and purification method, [1] The crude naphthalene derivative side chain chlorinated product obtained by side chain chlorination of the naphthalene derivative represented by the above general formula (I) has the general formula ▲ mathematical formula, chemical formula, table, etc. ▼... ...(III) (in the formula R and R'
represent lower alkyl groups that are the same or different from each other. ) is reacted with the aliphatic secondary amine represented by the general formula ▲
There are mathematical formulas, chemical formulas, tables, etc. ▼……(IV) (R in the formula
, R' and A have the same meanings as above. ) The first step of producing and isolating the tertiary amine derivative represented by formula (IV) [2] In the presence of a zinc catalyst, the tertiary amine derivative represented by the general formula (IV) obtained in the first step and the general Formulas▲There are mathematical formulas, chemical formulas, tables, etc.▼……(V-I
I) (In the formula, B″ represents a phenyl group represented by ▲There are mathematical formulas, chemical formulas, tables, etc.▼, Z represents a halogen atom, lower alkyl group, lower alkoxy group, nitro group, or cyano group, and n represents 0 , 1, 2 or 3, and when n is 2 or 3, Z may be a mutually different group.
The side chain monochlorinated product of the naphthalene derivative represented by the above general formula (II), which consists of a second step of separating the side chain monochlorinated product of the naphthalene derivative represented by I), consisting of the chlorinated product of the crude naphthalene derivative side chain. A method of separating and purifying.
JP18399481A 1981-11-16 1981-11-16 Separation and purification method for monochlorinated side chains of naphthalene derivatives Expired JPS5943934B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18399481A JPS5943934B2 (en) 1981-11-16 1981-11-16 Separation and purification method for monochlorinated side chains of naphthalene derivatives

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18399481A JPS5943934B2 (en) 1981-11-16 1981-11-16 Separation and purification method for monochlorinated side chains of naphthalene derivatives

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP10406576A Division JPS5331628A (en) 1976-08-31 1976-08-31 Isolation and purification of aromatic compounds with monohalogenated side chains

Publications (2)

Publication Number Publication Date
JPS57114528A JPS57114528A (en) 1982-07-16
JPS5943934B2 true JPS5943934B2 (en) 1984-10-25

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