JPH0615491B2 - Purification method of acetic anhydride - Google Patents

Purification method of acetic anhydride

Info

Publication number
JPH0615491B2
JPH0615491B2 JP7391686A JP7391686A JPH0615491B2 JP H0615491 B2 JPH0615491 B2 JP H0615491B2 JP 7391686 A JP7391686 A JP 7391686A JP 7391686 A JP7391686 A JP 7391686A JP H0615491 B2 JPH0615491 B2 JP H0615491B2
Authority
JP
Japan
Prior art keywords
acetic anhydride
exchange resin
diketene
ion exchange
ion
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 - Lifetime
Application number
JP7391686A
Other languages
Japanese (ja)
Other versions
JPS62246536A (en
Inventor
弘 三浦
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.)
Daicel Corp
Original Assignee
Daicel Chemical Industries 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 Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP7391686A priority Critical patent/JPH0615491B2/en
Publication of JPS62246536A publication Critical patent/JPS62246536A/en
Publication of JPH0615491B2 publication Critical patent/JPH0615491B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は無水酢酸の精製方法に関するものである。無水
酢酸は、アセチルセルロースの原料、医薬、農薬、染料
などに広く用いられている。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for purifying acetic anhydride. Acetic anhydride is widely used as a raw material for acetyl cellulose, medicines, agricultural chemicals, dyes and the like.

(従来技術および問題点) 無水酢酸の製法としては、酢酸、アセトンまたは酢酸メ
チル、酢酸エチル等の蒸気を熱分解して、生成するケテ
ンガスを酢酸に吸収、反応させて得る方法、無水塩化ア
ルミなどを触媒として酢酸にホスゲンと反応させる方
法、またはエチリデンジアセテートを塩化亜鉛等触媒の
存在下で加熱する方法などが知られている。これら公知
の方法で得られる無水酢酸には副反応として、ケテン自
身の2量化によるジケテンの生成、および反応工程等
で、無水酢酸自身の熱的経変等で生成すると考えられる
ジケテンが無水酢酸中に混入し、これらの無水酢酸を、
蒸留等公知の方法で精製しようとした場合、無水酢酸と
ジケテンとの沸点差が小さいこともあり、高還流比高段
数の精密蒸留を行う必要があり、エネルギーコストが高
いという問題があった。又、エネルギーコストを無視し
たとしても本発明のようにジケテンが不検出(5PPM以
下)の無水酢酢酸を得ることは不可能であった。
(Prior art and problems) As a method for producing acetic anhydride, a method in which vapor such as acetic acid, acetone or methyl acetate, ethyl acetate is thermally decomposed to absorb and react the produced ketene gas with acetic acid, anhydrous aluminum chloride, etc. There is known a method of reacting acetic acid with phosgene by using as a catalyst or a method of heating ethylidene diacetate in the presence of a catalyst such as zinc chloride. As a side reaction, acetic anhydride obtained by these known methods produces diketene by dimerization of ketene itself, and diketene, which is considered to be generated by thermal aging of acetic anhydride itself in a reaction step or the like, in acetic anhydride. And mix these acetic anhydrides with
In the case of purifying by a known method such as distillation, the boiling point difference between acetic anhydride and diketene may be small, and it is necessary to carry out precision distillation with a high reflux ratio and a high number of stages, resulting in a high energy cost. Further, even if the energy cost was ignored, it was impossible to obtain acetic anhydride without diketene detection (5 PPM or less) as in the present invention.

ジケテンは非常に反応性が高いため、特に医薬、農薬、
洗顔料等の原料に使用する無水酢酸は、不純物としての
ジケテンの含有量によってその商品価値が著しく左右さ
れる。
Diketene is very reactive, so
The commercial value of acetic anhydride used as a raw material for facial cleansers and the like significantly depends on the content of diketene as an impurity.

本発明は、工業的に有利にジケテン含有量の少い高品質
の無水酢酸を得るための精製方法を提供することを目的
とするものである。
An object of the present invention is to provide a purification method for industrially obtaining high-quality acetic anhydride having a low content of diketene.

(問題点を解決するための手段) 本発明者はジケテンを含む粗無水酢酸をイオン交換樹脂
で処理することにより、容易に高品質の無水酢酸が得ら
れることを見い出した。又、用いるイオン交換樹脂の種
類等によっては、この処理によりやや着色する場合もあ
るが、更に単蒸留程度の簡単な蒸留でこれをも解決する
ことができる事を見いだし本発明を完成した。
(Means for Solving Problems) The present inventors have found that high-quality acetic anhydride can be easily obtained by treating crude acetic anhydride containing diketene with an ion exchange resin. Further, depending on the type of ion exchange resin used and the like, this treatment may cause some coloration, but it was further found that this can be solved by simple distillation such as simple distillation, and the present invention was completed.

即ち、本発明は、ジケテンを含む粗無水酢酸をイオン交
換樹脂で処理し、必要に応じて該処理と同時にあるいは
該処理をした後に蒸留することを特徴とする無水酢酸の
精製方法である。
That is, the present invention is a method for purifying acetic anhydride, which comprises treating crude acetic anhydride containing diketene with an ion exchange resin and, if necessary, distilling the crude acetic anhydride simultaneously with or after the treatment.

イオン交換樹脂には大別して陰イオン交換樹脂と陽イオ
ン交換樹脂とがある。本発明にはこれらのいづれも使用
することができるが、ジケテン除去のために陰イオン交
換樹脂を使用することが好しい。
Ion exchange resins are roughly classified into anion exchange resins and cation exchange resins. Although any of these can be used in the present invention, it is preferable to use an anion exchange resin for removing the diketene.

具体的には陰イオン交換樹脂として、アンバーライトIR
A-68,IRA-94,IRA-93アンバーリストA−21等、陽イ
オン交換樹脂としてはアンバーリスト−15などが挙げ
られる。(アンバーライト、アンバーリストはローム・
アンド・ハース社の登録商標、オルガノ社販売品以下同
じ) イオン交換樹脂の量は特に規定する必要はないが、通
常、効率的には粗無水酢酸に対し0.1〜1.0wt%の範囲で
使用される。イオン交換樹脂の量が処理する原料粗無水
酢酸に対し、一定の場合は、処理温度は高い方が、ま
た、時間は長い方がその効果は大きい。温度についても
特に規定する必要はなく、実用的には室温程度が無水酢
酸の沸点である140℃程度の温度から選ばれる。本発
明の実施にあっては、所定量の原料粗無水酢酸に対し、
イオン交換樹脂を通常0.1〜1.0wt%程度加え、室温か
ら、130℃で1〜3時間攪拌処理するか、さらにその
処理液を100トール程度の減圧下で単蒸留に付するバ
ッチ方式で行うことができる。この場合、処理液の別
あるいは単蒸留等で回収されたイオン交換樹脂は繰り返
し使用することができる。
Specifically, as an anion exchange resin, Amberlite IR
A-68, IRA-94, IRA-93 Amberlyst A-21 and the like, and examples of the cation exchange resin include Amberlyst-15 and the like. (Amber Light, Amber List is ROHM
The registered trademark of And Haas Co., Ltd. and the product sold by Organo Co., Ltd.) It When the amount of the ion exchange resin is constant with respect to the raw material crude acetic anhydride to be treated, the effect is greater when the treatment temperature is higher and the treatment time is longer. The temperature does not need to be particularly specified either, and practically, the room temperature is selected from the temperature of about 140 ° C. which is the boiling point of acetic anhydride. In the practice of the present invention, for a predetermined amount of raw material crude acetic anhydride,
Ion-exchange resin is usually added in an amount of 0.1 to 1.0 wt% and stirred at room temperature at 130 ° C for 1 to 3 hours, or the treated solution is subjected to simple distillation under a reduced pressure of about 100 Torr in a batch system. You can In this case, the ion-exchange resin recovered by different treatment liquids or simple distillation can be repeatedly used.

また単蒸留装置の蒸発缶に所定量の原料粗無水酢酸を仕
込み約0.5〜1wt%程度に相当するイオン交換樹脂を入
れ、帯留時間が2〜8時間になるように連続的に仕込
み、連続的に留出させる方法でも処理できる。更には、
イオン交換樹脂を充填したカラムに粗無水酢酸を、室温
程度でおよそ2〜20時間循環させ、ジケテン濃度が所
定量以下になった後、この処理液を100トール程度の減
圧下で単蒸留に付することもできる。
In addition, a predetermined amount of crude acetic anhydride was charged into the evaporator of the simple distillation apparatus, an ion-exchange resin corresponding to about 0.5 to 1 wt% was charged, and continuously charged so that the distillation time was 2 to 8 hours. It can also be treated by a method of distilling it in. Furthermore,
Crude acetic anhydride is circulated in a column packed with an ion exchange resin at room temperature for about 2 to 20 hours, and after the diketene concentration falls below a predetermined amount, this treatment liquid is subjected to simple distillation under a reduced pressure of about 100 Torr. You can also do it.

この場合、イオン交換樹脂は、詰替えまたは再成するこ
となく繰返し使用できる。15回繰返し使用しても、特
に効果の減少は認められなかった。
In this case, the ion exchange resin can be used repeatedly without refilling or re-forming. Even after repeated use 15 times, no particular decrease in effect was observed.

(発明の効果) 簡単な方法で経済的に無水酢酸中のジケテンを5PPM以
下(不検出)にまで除去することができる。又処理に使
用したイオン交換樹脂の分離も簡単であり、得られた高
品質の無水酢酸は医農薬など精密化学分野原料として問
題なく使用することができる。
(Effect of the Invention) Diketene in acetic anhydride can be economically removed to 5 PPM or less (not detected) by a simple method. Further, the ion-exchange resin used for the treatment can be easily separated, and the obtained high-quality acetic anhydride can be used as a raw material for fine chemical fields such as medicines and agricultural chemicals without any problem.

実施例−1 原料粗無水酢酸を各フラスコに100gづつ入れ、それ
ぞれのフラスコに種類の異なるイオン交換樹脂、1gを
添加し、室温下1時間攪拌したのち、過しそれぞれに
ついて、ガスクロマトグラフィーによって分析した。そ
の結果は表−1の通りであった。なおイオン交換樹脂に
は水が含まれているので、この水分を十分除いて、用い
た。以下の実験に用いたものもいずれも同様の前処理を
して脱水したイオン交換樹脂を使用した。
Example-1 100 g of raw material crude acetic anhydride was placed in each flask, 1 g of a different kind of ion exchange resin was added to each flask, and the mixture was stirred at room temperature for 1 hour and then analyzed by gas chromatography. did. The results are shown in Table 1. Since the ion exchange resin contains water, this water was used after being sufficiently removed. The ion-exchange resins used in the following experiments were dehydrated by the same pretreatment.

実施例−2 各三角フラスコにそれぞれ原料粗無水酢酸100gを入
れ、これにイオン交換樹脂(アンバーリストA−21)
を0.1g,0.5gまたは1.0g入れた3水準と温度を30
℃,70℃および130℃の3水準、処理時間を1時間、2
時間および3時間の3水準をとり、所定温度で所定時間
攪拌処理した後、GC分析を行なった。その結果は表−2
の通りであった。
Example-2 100 g of raw material crude acetic anhydride was put in each Erlenmeyer flask, and ion-exchange resin (Amberlyst A-21) was put into this.
3 levels with 0.1g, 0.5g or 1.0g and temperature of 30
℃, 70 ℃ and 130 ℃ 3 levels, processing time 1 hour, 2
After 3 hours of time and 3 hours were taken and the mixture was stirred at a predetermined temperature for a predetermined time, GC analysis was performed. The results are shown in Table-2.
It was the street.

実施例−3および比較例1 蒸留フラスコに原料粗無水酢酸400gを入れイオン交換
樹脂(アンバーリストA−21)を2g加え、100トー
ル減圧下で、連続的に50ml/Hで仕込み連続的に50ml/
Hで留出させる蒸留を行った。本方法で約4000ml処理
し、この留出液についてGC分析した結果は表−3の通り
であった。なお無水酢酸中のジケテン約100ppmのものを
上記と全く同じ方法で処理したものからは、ジケテンは
全く検出されなかった。
Example-3 and Comparative Example 1 400 g of raw material crude acetic anhydride was placed in a distillation flask, 2 g of an ion exchange resin (Amberlyst A-21) was added, and continuously charged at 50 ml / H under a reduced pressure of 100 Torr and continuously 50 ml. /
Distillation was carried out by distilling with H 2. About 4,000 ml was treated by this method, and the result of GC analysis of this distillate was as shown in Table-3. No diketene was detected at all in the case where about 100 ppm of diketene in acetic anhydride was treated by the same method as above.

また、イオン交換樹脂を全く加えないほかは上記と全く
同様に処理した比較実験結果も表−3にした。
Table 3 also shows the results of a comparative experiment in which the same treatment as above was carried out except that no ion exchange resin was added.

実施例−4 循環設備を備えた容器に原料粗無水酢酸3000mlを入れ、
イオン交換樹脂(アンバーリストA−21)を30g充填
した塔を通して、ポンプを用いて、室温下150分循環し
た。この処理液と、100トール減圧下で単蒸留して得た
もののGC分析結果は表−4の通りであった。なおイオン
交換樹脂を結め替えることなく、前記方法で12回、同
じ原料粗無水酢酸を用い繰返し同様に実験して処理した
ものの品質は、いずれも、表−4に示したと同程度であ
り、特にイオン交換樹脂の性能の低下は認められなかっ
た。
Example-4 Put 3000 ml of raw material crude acetic anhydride into a container equipped with a circulation facility,
It was circulated for 150 minutes at room temperature using a pump through a column packed with 30 g of an ion exchange resin (Amberlyst A-21). Table 4 shows the GC analysis results of this treatment solution and that obtained by simple distillation under a reduced pressure of 100 Torr. Note that the quality of the product treated by repeating the same experiment using the same raw material crude acetic anhydride 12 times by the above-mentioned method without changing the ion-exchange resin was the same as shown in Table 4, In particular, no deterioration in the performance of the ion exchange resin was observed.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ジケテンを含む粗無水酢酸をイオン交換樹
脂で処理し、必要に応じて該処理と同時にあるいは該処
理をした後に蒸留することを特徴とする無水酢酸の精製
方法。
1. A method for purifying acetic anhydride, which comprises treating crude acetic anhydride containing diketene with an ion exchange resin and, if necessary, distilling the crude acetic anhydride simultaneously with or after the treatment.
JP7391686A 1986-03-31 1986-03-31 Purification method of acetic anhydride Expired - Lifetime JPH0615491B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7391686A JPH0615491B2 (en) 1986-03-31 1986-03-31 Purification method of acetic anhydride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7391686A JPH0615491B2 (en) 1986-03-31 1986-03-31 Purification method of acetic anhydride

Publications (2)

Publication Number Publication Date
JPS62246536A JPS62246536A (en) 1987-10-27
JPH0615491B2 true JPH0615491B2 (en) 1994-03-02

Family

ID=13531967

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7391686A Expired - Lifetime JPH0615491B2 (en) 1986-03-31 1986-03-31 Purification method of acetic anhydride

Country Status (1)

Country Link
JP (1) JPH0615491B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5175363A (en) * 1991-01-28 1992-12-29 Eastman Kodak Company Method for purification of carboxylic acids and anhydrides
US5264087A (en) * 1992-10-13 1993-11-23 Eastman Kodak Company Method for refining acetic anhydride by distillation
JP2012153667A (en) * 2011-01-27 2012-08-16 Mitsubishi Chemicals Corp Method for producing polyalkylene ether glycol and method for purifying acetic anhydride

Also Published As

Publication number Publication date
JPS62246536A (en) 1987-10-27

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