JPS5826852A - Purifying method of crude phenylhydrazine - Google Patents

Purifying method of crude phenylhydrazine

Info

Publication number
JPS5826852A
JPS5826852A JP12644181A JP12644181A JPS5826852A JP S5826852 A JPS5826852 A JP S5826852A JP 12644181 A JP12644181 A JP 12644181A JP 12644181 A JP12644181 A JP 12644181A JP S5826852 A JPS5826852 A JP S5826852A
Authority
JP
Japan
Prior art keywords
phenylhydrazine
crude
parts
alkaline earth
alkali
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.)
Granted
Application number
JP12644181A
Other languages
Japanese (ja)
Other versions
JPS6139302B2 (en
Inventor
Michio Katou
加藤 廸夫
Shigeo Wake
和気 繁夫
Toyomitsu Shimizu
豊満 清水
Yoshihide Mori
森 美秀
Michiichi Sano
佐野 道一
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP12644181A priority Critical patent/JPS5826852A/en
Publication of JPS5826852A publication Critical patent/JPS5826852A/en
Publication of JPS6139302B2 publication Critical patent/JPS6139302B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To purify crude phenylhydrazine into a purified, almost colorless and transparent substance having improved color tone in purifying the crude phenylhydrazine after distilling away an extracting agent by the rectification or simple distillation, by the presence of hydroxide of an alkali metal or alkaline earth metal. CONSTITUTION:A salt of phenylhydrazine obtained by the diazotation reduction and hydrolysis of aniline is neutralized with an alkali and extracted with an organic solvent. The extracting agent is then distilled away to give crude phenylhydrazine, which is then rectified or distilled simply in the presence of 0.06- 10wt% one or two or more hydroxides of an alkali metal or alkaline earth metal, e.g. sodium or lithium hydroxide, at an operating pressure of 200mm.Hg or less and purified to give a colorless transparent phenylhydrazine. This method reduces the volatility of volatile colored substances, and inhibits the formation of the volatile colored substances by the thermal decomposition of the phenylhydrazine itself.

Description

【発明の詳細な説明】 本発明はアニリンのジアゾ化、7元、加水分解反応1こ
よっr fE4られたフェニルヒドラジンの塩をアルカ
リ、こよって中和し有ゆ溶媒にC抽出後、抽剤を留去し
C?%られる類フェニルヒドラジンからほぼ偏色透明な
るフェニルヒドラジンを得る方ゆ、こ関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention involves the diazotization, 7-element, and hydrolysis reaction of aniline. After neutralizing the resulting phenylhydrazine salt with an alkali and extracting it with an aqueous solvent, Distill C? The present invention relates to a method for obtaining almost polarized and transparent phenylhydrazine from phenylhydrazine of which %.

フェニルヒドラジンは挿々の医薬、1整、染料等の重要
な基幹中間物としC使用さn、rいる。アニリンのジア
ゾ化、覆元、加水分解反応、こよっCフェニルヒドラジ
ンを製造する方法は、例えばオーガニックシンセシス[
Organic 5ynthesis coll、vo
l、1,442.1982年、(j、)1,0oler
nan ) +コf載、:nてい6よう1こ、一般的に
はアニリンの塩酸塩を亜硝酸ナトリウムによっCジアゾ
化してジアゾニウム塩にし、これ、こ亜硫酸ナトリウム
を作用させてフェニルヒドラジンジスルホン酸ナトリウ
ム塩を得、ついで塩酸を用いr tan水分解反応を行
い、生成しrこフェニルヒドラジンの塩酸塩をアルカリ
本曇こより中和してフェニルヒドラジンを得ることがで
きる。このフェニルヒドラジンをベンゼン、トルエン、
キシレン等のフェニルヒドラジンIζ対する親和性の高
い有機溶媒會こより抽出しなσ)ち、抽剤を留去しで目
的とする粗フェニルヒドラジンを得ることができる。通
常このよう、こしで得らnjこ粗フェニルヒドラジンを
蒸留1こ付す事1こより哨製し、晴フェニルヒドラジン
を得ることができる。
Phenylhydrazine is used as an important basic intermediate in various pharmaceuticals, chemicals, dyes, etc. Methods for producing phenylhydrazine, such as diazotization of aniline, diazotization, and hydrolysis reactions, include, for example, organic synthesis [
Organic 5 synthesis coll, vo
l, 1,442.1982, (j,) 1,0oler
Generally speaking, aniline hydrochloride is C-diazotized with sodium nitrite to form a diazonium salt, and this is treated with sodium sulfite to form phenylhydrazine disulfonic acid. After obtaining the sodium salt, a r tan water splitting reaction is performed using hydrochloric acid, and the resulting phenylhydrazine hydrochloride is neutralized with an alkaline solution to obtain phenylhydrazine. This phenylhydrazine can be mixed into benzene, toluene,
The target crude phenylhydrazine can be obtained by extraction using an organic solvent having high affinity for phenylhydrazine Iζ such as xylene (σ), and then distilling off the extractant. Normally, the crude phenylhydrazine obtained by straining is subjected to one column of distillation to obtain clear phenylhydrazine.

しかじaから、この方法1こおいC/F4られるフェニ
ルヒドラジンはその1L1.質、とおいて必ずしも#尼
できるものではなく、特電こ製品が着色しCいるという
X点があり、この改良が強く望まれていな。ト配オーガ
ニックシンセシスf (Jrganic 8ynthe
sis Co11.vol、l、443゜1932年、
 (j、H6Coleman ) +コも、コ(7) 
方法+コより得られたフェニルヒドラジンは黄色を呈し
た液体である事が2ti2されており、まt二本発明者
ら、こよるq細なる検討精巣lこおいでも、この着色の
問題は粗フヱニルヒドラジンの哨沼をくり返すFlat
こよつCも、あるいは単なる精留条件の改良會こよつで
もぜ決されケいことが判明した。
From the above, the phenylhydrazine produced by this method 1C/F4 is 1L1. In terms of quality, it is not necessarily something that can be improved, and there is a point that the special electric product is colored and there is a strong desire for improvement. Jrganic 8ynthe
sis Co11. vol, l, 443゜1932,
(j, H6Coleman) + ko, ko (7)
It has been reported that the phenylhydrazine obtained by the method is a yellow liquid, and the inventors of the present invention have thoroughly examined the testicles and found that this problem of coloration has not been solved. Flat that repeats the swamp of Fenylhydrazine
It became clear that Koyotsu C could not be resolved by simply improving the rectification conditions.

又、特開昭54−149B2@公報電こは、粗フェニル
ヒドラジンよりほとんど無色透明かつJIS−4879
5+こよる酢ヤ溶液ヂスト1こおいC十分透明なより高
品質のフエニlレヒドラらンを得る。こあtこり、粗フ
エニIレヒドラジンをアルカリ金属またはアルカリ土類
金属の水酸化物より2ばれた1棒以ヒと原町処理したの
ち、グリコール類の存在下1こ蒸留する方法が記載され
ているが、この方法ではグ作中、ζおけるフェニルヒド
ラジン自体の熱分解、こよる揮発性着色物質の生成を十
分抑制することができrい等のに点を有している。
In addition, JP-A-54-149B2 @ Publication Telephone is almost colorless and transparent than crude phenylhydrazine and JIS-4879.
5 + 1 oz. of vinegar solution 1 oz. C Obtain a higher quality phenylene rehydran that is sufficiently transparent. A method has been described in which crude phenolic rehydrazine is treated with a mixture of alkali metal or alkaline earth metal hydroxides and then distilled in the presence of glycols. However, this method has drawbacks such as the inability to sufficiently suppress the thermal decomposition of phenylhydrazine itself in ζ during production, and the resulting formation of volatile colored substances.

木発明者等はこれらのX点を改善すべく悦。Wood inventors and others are happy to improve these X points.

竜検討を重ねた結果、抽剤歿去後の粗フエニ的とするフ
ェニルヒドラジンを得る際舌こ、アルカリ金属またはア
ルカリ土類金属の水酸化物より選ばれた1%または2棒
以ヒを存在させることtこよって、色調の著しく改良さ
れたほぼ無色汚明なるフェニルヒドラジンが得られるこ
とを見出し、本発明を完成する。こ至−1こ。
As a result of repeated studies, it was found that when obtaining crude phenylhydrazine after extraction, 1% or 2 or more rods selected from hydroxides of alkali metals or alkaline earth metals should be present. It was discovered that by doing so, it was possible to obtain phenylhydrazine which was substantially colorless and had a significantly improved color tone, thereby completing the present invention. Koto-1ko.

ところで、アルカリ金属またはアルカリ土すると黄色を
畳びたフェニルヒドラジンが留出物としで得られ、例え
ば操作圧力が300rnHfの場合、留出物のガードナ
ー色数〔JIS K54001こよる方法)は約4〜5
である。
By the way, when alkali metals or alkaline earths are used, yellowish phenylhydrazine is obtained as a distillate. For example, when the operating pressure is 300 rnHf, the Gardner color number of the distillate (method according to JIS K54001) is about 4 to 5
It is.

この着色の曜因あるいは唄因となる物質φこついでは現
在のところ不明であり、アルカリ金属またはアルカリ土
類金属の水酸化物の作中機構、こついても不明であるが
、通常の物理的吸着作用をもつFIφ色剤とじC知らe
tcいる活性炭、酸化アルミナ、ケイノウ上等では、何
ら着色防止効毛が得られず本発明の方法であるアルカリ
金属またはアルカリ土類金層の水酸化物を本発明の方法
中こ従っC用いることをこより、特異的rこ著しい効囃
を発揮することは贅くべぎことである。
The substance responsible for this coloring or staining is currently unknown, and the mechanism behind the formation of alkali metal or alkaline earth metal hydroxides is also unknown, but normal physical FIφ colorant binding with adsorption action
Activated carbon, alumina oxide, carbon dioxide, etc., which contain tc, do not provide any anti-coloration effect, and the method of the present invention is to use the hydroxide of an alkali metal or alkaline earth gold layer in the method of the present invention. Therefore, it is a luxury to be able to exert a specific and remarkable effect.

本発明の方法、こ用いられるアルカリ金了またはアルカ
リ土類金属の水酸化物としては、容易、こ手1こ入る市
販の水酸化ナトリウム、水酸化カリウム、水酸化リチウ
ム、水酸化マグネシウム、水酸化カルシウム等が好まし
く使用−こあたっCはこれらの水溶液として用いること
も可能であるし、もしくは固体のままでする。これより
水を分喘する必要がある場合lこは水を含まない固体の
アルカリ全厚またはアルカリ土類金属の水酸化物を使用
する方が望ましい。
The hydroxides of alkali metals or alkaline earth metals used in the method of the present invention are commercially available such as sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide, and hydroxide. Calcium etc. are preferably used - Koatto C can be used as an aqueous solution of these or remain as a solid. If it is necessary to separate water from this, it is preferable to use a solid alkali full thickness or alkaline earth metal hydroxide that does not contain water.

アルカリ金属またはアルカリ土類金属の水酸化物を想フ
ェニルヒドラジン脅こ添加する方法は拮ンし恨定されな
いが、目的とするフェニルヒドラジンを蒸留TこよっC
精製し塔頂より製品を得る場合lこは、蒸貿塔への供給
吻である粗フェニルヒドラジン1こ添加する方が望ま品
のフェニルヒドラジンを留出させる場合會こ金;礪また
はアルカリ土類金属の水酸化物を添加しCもその効果は
同じである。あるいは粗フェニルヒドラジンを予めアル
カリ金属まtこ留出物としC2する方法でも良いが、該
固体との接触後の籾フェニルヒドラジン中−こはある一
定虐度以ヒのアルカリ金胃またはアルカリ土類金属の水
酸化物が存在しCいaければな明′rるフェニルヒドラ
ジンを得るIC′、こアルカリ金蛎またはアルカリ土類
金暎の水酸化物より選ばれた1種または2種以上の存在
下で実施することが必要であり、これ1とよ−で粗フェ
ニルヒドラジン中シこ含まれCいる揮発性着本発明方法
参こむけるアルカリ金1べまたはアルカリ土類金属の水
酸化物の共存所は一役、こ゛阻フェニルヒドラジンイと
対しr O,06〜10重1%であ1ば良い。共存M′
がこの下限未満の少嘱の場合、こけ着色防■ヒj1果は
若干甲められるものの充分満足できるものではない。副
えは一般的方法によって得られた粗フエ、ニルヒドラジ
ンVこ対し、0.05重量%の水情化すrlI2〜3の
フェニルヒドラジンが得られたっ10 ip *i%を
越えて多畷、こ添加した場合會とは、着色防IE効果は
十分であるがアルカリ金属ま粘性が異常1と高くなり、
通信のポンプ等1こよる抜き出しが困難、こりる。この
ため高沸物の抜き出しを容易1こするため、ある惰のフ
ェニレンの損失が大となり不経済である。
Although the method of adding an alkali metal or alkaline earth metal hydroxide to phenylhydrazine is not prohibited, it is possible to distill the desired phenylhydrazine.
When purifying the product and obtaining it from the top of the column, it is better to add 1 g of crude phenylhydrazine, which is the supply port to the distillation column, to distill out the desired product, phenylhydrazine. The same effect can be obtained by adding metal hydroxide to C. Alternatively, a method may be used in which crude phenylhydrazine is made into an alkali metal distillate in advance and subjected to C2, but after contact with the solid, the paddy phenylhydrazine contains alkali gold or alkaline earth with a certain degree of severity. In order to obtain phenylhydrazine in the presence of a metal hydroxide, one or more selected from the hydroxides of alkali metals or alkaline earth metals are used. It is necessary to carry out the process in the presence of crude phenylhydrazine containing carbon, which is a volatile compound of alkali gold or alkaline earth metal hydroxide used in the process of the present invention. Coexistence with phenylhydrazine plays a role, and 1% by weight of rO,06-10 is sufficient. Coexistence M′
If it is less than this lower limit, the resistance to discoloration may be slightly improved, but it is not fully satisfactory. As a side dish, crude feed and nylhydrazine V were obtained by a general method, and 0.05% by weight of phenylhydrazine with rlI2 to 3 was obtained. When added, the coloring prevention IE effect is sufficient, but the alkali metal viscosity becomes abnormally high.
It is difficult to remove the communication pump, etc., and it becomes stiff. For this reason, it is easy to remove high-boiling substances, which results in a large loss of phenylene, which is uneconomical.

トコロチ、アルカリ金属またはアルカリ土はぼ何色透明
なるフェニルヒドラジンを得る場合、その操作は連埴あ
るいは回分式のいずれでも自いが、操作圧力は200f
fH?以下で実施する必要がある。この子方よりも謂い
場合、とは、アルカリ金属またはアルカリ土類金属の水
酸化物が存在しCいCも、フェニルヒドラジンの熱分解
、こより揮発性着色物質が生成し、これ、こより製品の
フェニルヒドラジンが黄色を呈するよう、こなり、該ア
ルカリ金園またはアルカリ土類金属の水酸化物の添力口
が無意味Vこなる。したがっC1できるだけ操作田力を
低クシ、フェニルヒドラジンの蒸発温!を低く朋え熱分
wlを抑制する必ヴがある。
Tokorochi, alkali metals or alkaline earths When obtaining transparent phenylhydrazine of any color, the operation can be carried out either continuously or batchwise, but the operating pressure is 200 f.
fH? It is necessary to perform the following. In other words, in the presence of alkali metal or alkaline earth metal hydroxides, volatile colored substances are produced from the thermal decomposition of phenylhydrazine, and from this, the product is When phenylhydrazine appears yellow, the addition of alkaline metal hydroxide or alkaline earth metal hydroxide becomes meaningless. Therefore, C1 should be operated as low as possible, the evaporation temperature of phenylhydrazine! It is necessary to keep the temperature low to suppress the heat content.

また酸素暑こよるフェニルヒドラジンの酸化・こも注意
しなければりらTいことは良く知られ流中もしくは−J
iふん囲q下で行われる。
It is also well known that one must be careful about the oxidation of phenylhydrazine due to oxygen heat.
It is carried out under i and q.

本発明の方法によるフェニルヒドラジンの精製方法の対
冑となる粗フェニルヒドラジンはアニリンのジアゾ化、
還元、加水分解反応、こより合成されるが本発明方法の
実師はこれらのジアゾ化反応、還元反応、加水分解反応
の方法−こよっては制心さ4るものではない。
Crude phenylhydrazine, which is the antidote to the method for purifying phenylhydrazine according to the method of the present invention, is obtained by diazotizing aniline,
Although it is synthesized through reduction and hydrolysis reactions, the method of the present invention is not limited to these diazotization reactions, reduction reactions, and hydrolysis reactions.

以下本発明の方法を実権例にょっC更、こ具体的。こ説
明するが、本発明はこれらの実施例Iこのみ心電される
ものではない。
The method of the present invention will be described in more detail below as an actual example. However, the present invention is not limited to these embodiments.

実権例1 攪拌機、滴下ロート、棒状濡寒計および冷却装置を備え
たt、oooccの円筒状セパラブルフラスコ−こ2部
重唯%塩酸水溶液500部とアニリン100部を仕込み
、寒削で内容物を0℃lこ冷却しながら、滴下ロートよ
り36重看%亜硝酸ナトリウム水溶液215部を注いで
ジアゾ化反応纂行い、反応液815部を得た。次iこ別
1こ準備しCおいた亜Ek灼ナトリウム205部、貢亜
硫駿ナトリウム110部、水700部よりなるη元剤水
溶液虻こ、OC,こ保った前記ジアゾ化父応液を少量ず
つ注入した。その後45℃トこ30分間保持したのち、
90C+と昇温し単・こ60分間その温母−こ保持しな
がら還元反応を行った。次、ここの還元反応液「こ滴下
ロートより85重惜%塩酸水溶液230部を少量ずつ滴
下したのち、90℃の温守で90分間保持しC加水分解
反応を行−tコ。
Practical Example 1 A cylindrical separable flask of 200 mm, equipped with a stirrer, a dropping funnel, a rod-shaped cryostat, and a cooling device, was charged with 2 parts, 500 parts of a heavy % hydrochloric acid aqueous solution, and 100 parts of aniline, and the contents were cooled down. While cooling the mixture to 0° C., 215 parts of a 36% sodium nitrite aqueous solution was poured into the mixture through a dropping funnel to carry out a diazotization reaction, thereby obtaining 815 parts of a reaction solution. Next, prepare a separate aqueous solution of η base agent consisting of 205 parts of cauterized sodium chloride, 110 parts of sodium sulfite, and 700 parts of water, and add the diazotized parent reaction solution kept in OC. Injected in small quantities. After that, after holding at 45℃ for 30 minutes,
The temperature was raised to 90C+ and the reduction reaction was carried out while maintaining the temperature for 60 minutes. Next, 230 parts of an 85% hydrochloric acid aqueous solution was added dropwise little by little from the reducing reaction solution through the dropping funnel, and the mixture was kept at 90°C for 90 minutes to carry out a C hydrolysis reaction.

ついでこの加水分解反応液を40℃まで金部し、滴下ロ
ートより49重着%水酸牛ナトリウム水溶液400部を
加えC中和したのち、800部のトルエンで3回佃出を
行った。史rこ抽出したトルエン相を全部用めr、lo
OflMrの誠■下でトルエンを留去し、釜より伸フェ
ニルヒドラジン110部を得た。
Next, this hydrolysis reaction solution was cooled to 40° C., and 400 parts of a 49% weighted sodium hydroxide aqueous solution was added from the dropping funnel to neutralize the solution, followed by dipping three times with 800 parts of toluene. Use all of the extracted toluene phase.
Toluene was distilled off under an OflMr. 110 parts of expanded phenylhydrazine was obtained from the flask.

この相フェニルヒドラジン(こi直径約5卵のペレット
状の水酸化ナトリウム2部を添加し、300CCの丸穴
フラスコを用いC1しCフェニルヒドラジン100部を
得た。
2 parts of sodium hydroxide in the form of pellets of about 5 eggs in diameter were added to this phase phenylhydrazine, and the mixture was purified using a 300 CC round hole flask to obtain 100 parts of C phenylhydrazine.

このフェニルヒドラジンはほぼ午色透明であり、そのガ
ードナー色数は1α下であっtこ。
This phenylhydrazine is transparent, almost daylight color, and its Gardner color number is below 1α.

実施例2 実施例1で使用した水酸化ナトリウム2部の代わりイこ
水酸化カルシウム2部を用いた以外は実権例1と同様ケ
こ行い、フェニルヒドラジン100部を得たが、はぼ何
色透明であり、そのガードナー色数はIQ下であった。
Example 2 The same procedure as in Example 1 was carried out except that 2 parts of calcium hydroxide was used instead of 2 parts of sodium hydroxide used in Example 1, and 100 parts of phenylhydrazine was obtained. It was transparent and its Gardner color number was below IQ.

実権例8 水酸化ナトリウム2部1こ代えで4部、6部、8部とそ
れぞれ別個りこ用いた以外は実り 椎例1と−じ方法で弔蒸Iを行ったところ留出したフェ
ニルヒドラジンは何れの場合もほぼ測色透明でありガー
ドナー色数もすべrl以下であったっ 実施例4 水酸化ナトリウム2部、と代えで水酸化カリウム、水酸
化マグネシウム及び水酸化リチウムを各2@宛それぞれ
別4ptこ用いた以外は実権例1と同様1こ行ないフェ
ニルヒドラジンをびたが、いずれの場合もほぼ無色洒明
でありガードナー色数はすべrlQ下であった。
Practical example 8 Distilled phenylhydrazine was obtained when vaporization I was carried out in the same manner as in practical example 1, except that 2 parts of sodium hydroxide was replaced with 1 part and 4 parts, 6 parts, and 8 parts were used separately. In all cases, the colorimetry was almost transparent, and the Gardner color number was below RL.Example 4: In place of 2 parts of sodium hydroxide, potassium hydroxide, magnesium hydroxide, and lithium hydroxide were each added separately to 2 parts each. Phenylhydrazine was applied once in the same manner as in Practical Example 1, except that 4pt was used, but in each case, it was almost colorless and bright, and the Gardner color number was all below rlQ.

実権例5 直径約5Mのペレット状の水酸化ナトリウム100部を
充填した塔卆こ、実施例1と全く同様の方法で得た粗フ
ェニルヒドラジンllO部を通蒔−させたのち、理論段
数5段の充填塔を具備した蒸留フラスコ、こ仕込み、岩
素ガスをキャピラリーより魔人しながら5yHfの械圧
下、還流比2の条件下で精留を行い、留分としc1フェ
ニルヒドラジン95部を得たが、このフェニルヒドラジ
ンははぼ伊色透明でガードナー色数はlLJ、下であ−
た。また水酸化す(リウム充填塔を通過後の粗フェニル
ヒドラジン中の水酸化ナトリウム−咋は0.15重筆%
であった。
Practical example 5 A column filled with 100 parts of pelletized sodium hydroxide with a diameter of about 5M was sown with 110 parts of crude phenylhydrazine obtained in exactly the same manner as in Example 1, and then the number of theoretical plates was 5. This was charged into a distillation flask equipped with a packed column, and the gas was distilled from the capillary under the mechanical pressure of 5yHf under the conditions of a reflux ratio of 2 to obtain 95 parts of c1 phenylhydrazine as a fraction. However, this phenylhydrazine is pale yellow and transparent, and its Gardner color number is 1LJ, which is below.
Ta. In addition, hydroxide (sodium hydroxide in crude phenylhydrazine after passing through a lithium-packed tower is 0.15%)
Met.

比較例1 実施例1と全く同様の方法で得た粗フェニルヒドラジン
110部を水酸化ナトリウムを添加せず・こ、窒素ガス
を導入しなから望 10 w H−y の4千下で川魚7させ、留出物とし
Cフェニルヒドラジン100部を得たが黄褐色を串び、
そのガードナー色数は約5 で +  っ tこ。
Comparative Example 1 110 parts of crude phenylhydrazine obtained in exactly the same manner as in Example 1 was mixed with freshwater fish at 4,000 ml of 10 w H-y without adding sodium hydroxide and without introducing nitrogen gas. 7 to obtain 100 parts of C phenylhydrazine as a distillate, but a yellowish brown color was obtained.
The number of Gardner colors is approximately 5.

比較例2 と同様、こ行い、フェニルヒドラジン100部を得たが
黄褐色1こ着色し、そのガードナー色数は4であっすこ
This was carried out in the same manner as in Comparative Example 2, and 100 parts of phenylhydrazine was obtained, but one part was colored yellowish brown, and the Gardner color number was 4, which was the same color.

比較例3 実施例1で使用した水酸化ナトリウム2部の代わり1こ
O,05邪の水酸化ナトリウムを用いたU外は実施例I
と同横蕃と行い、フェニルヒドラジン100部を得たが
、ややl fhを♀し、そのガードナー色数は約2.5
代理人 弁理士 木村鳴昔。
Comparative Example 3 In place of 2 parts of sodium hydroxide used in Example 1, 1.05% sodium hydroxide was used except for Example I.
100 parts of phenylhydrazine was obtained using the same method as above, but the color was slightly l fh, and the Gardner color number was about 2.5.
Agent: Patent attorney Kimura Narumi.

Claims (1)

【特許請求の範囲】 l)アニリンのジアゾ化、7元、加水分解反応−こよっ
C得ら1なフェニルヒドラジンの塩をアルカリ?こよっ
で中和し有機溶媒にT:押出後、抽剤を留去しで得られ
る類フェニルヒドラジンをアルカリ金属またはアルカリ
土類金鴛の透明なるフェニルヒドラジンを得ることを持
活とする類フェニルヒドラジンの精製方法。 2)アルカリ金属またはアルカリ土類金属の水酸化物よ
り選ばれた1種または2種以上の存在蚤が粗フェニルヒ
ドラジン鹸こ対し0.06〜10重量%である特許請求
の範囲第1項?載以下である特許請求の範囲第1項記載
の方法。
[Claims] l) Diazotization, 7-element, and hydrolysis reaction of aniline - Is the salt of 1 phenylhydrazine obtained with an alkali? After extrusion, the extractant is distilled off to obtain a transparent phenylhydrazine of an alkali metal or alkaline earth metal. Method for purifying hydrazine. 2) Claim 1, wherein one or more types of fleas selected from hydroxides of alkali metals or alkaline earth metals are present in an amount of 0.06 to 10% by weight based on the crude phenylhydrazine sapon. A method according to claim 1, which includes:
JP12644181A 1981-08-11 1981-08-11 Purifying method of crude phenylhydrazine Granted JPS5826852A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12644181A JPS5826852A (en) 1981-08-11 1981-08-11 Purifying method of crude phenylhydrazine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12644181A JPS5826852A (en) 1981-08-11 1981-08-11 Purifying method of crude phenylhydrazine

Publications (2)

Publication Number Publication Date
JPS5826852A true JPS5826852A (en) 1983-02-17
JPS6139302B2 JPS6139302B2 (en) 1986-09-03

Family

ID=14935279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12644181A Granted JPS5826852A (en) 1981-08-11 1981-08-11 Purifying method of crude phenylhydrazine

Country Status (1)

Country Link
JP (1) JPS5826852A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000020381A1 (en) * 1998-10-05 2000-04-13 Zeneca Limited Purification procedure for phenylhydrazines
JP2012246274A (en) * 2011-05-31 2012-12-13 Sumitomo Chemical Co Ltd Method for producing phenylhydrazines
CN103130678A (en) * 2013-03-12 2013-06-05 东力(南通)化工有限公司 Method for increasing concentration of methylhydrazine aqueous solution from 40% to 98%
CN114082209A (en) * 2021-12-08 2022-02-25 启东亚太药业有限公司 Negative pressure distillation phenylhydrazine separation and purification equipment and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000020381A1 (en) * 1998-10-05 2000-04-13 Zeneca Limited Purification procedure for phenylhydrazines
JP2012246274A (en) * 2011-05-31 2012-12-13 Sumitomo Chemical Co Ltd Method for producing phenylhydrazines
CN103130678A (en) * 2013-03-12 2013-06-05 东力(南通)化工有限公司 Method for increasing concentration of methylhydrazine aqueous solution from 40% to 98%
CN114082209A (en) * 2021-12-08 2022-02-25 启东亚太药业有限公司 Negative pressure distillation phenylhydrazine separation and purification equipment and method

Also Published As

Publication number Publication date
JPS6139302B2 (en) 1986-09-03

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