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JPH0560815B2 - - Google Patents
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JPH0560815B2 - - Google Patents

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Publication number
JPH0560815B2
JPH0560815B2 JP114886A JP114886A JPH0560815B2 JP H0560815 B2 JPH0560815 B2 JP H0560815B2 JP 114886 A JP114886 A JP 114886A JP 114886 A JP114886 A JP 114886A JP H0560815 B2 JPH0560815 B2 JP H0560815B2
Authority
JP
Japan
Prior art keywords
diethylaminoethanol
product
dissolved oxygen
ppm
oxygen concentration
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
JP114886A
Other languages
Japanese (ja)
Other versions
JPS62161749A (en
Inventor
Teruo Itokazu
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 JP114886A priority Critical patent/JPS62161749A/en
Publication of JPS62161749A publication Critical patent/JPS62161749A/en
Publication of JPH0560815B2 publication Critical patent/JPH0560815B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、ジエチルアミンと酸化エチレンから
合成されたジエチルアミノエタノールを精溜し、
あるいは精溜せずに、窒素ガス等の不活性ガスと
効率的に接触せしめることにより、該液中の溶存
酸素濃度を1ppm以下にすることで、経時着色を
防止することを特徴とするジエチルアミノエタノ
ールの製造方法に関するものである。
[Detailed Description of the Invention] <Industrial Application Field> The present invention rectifies diethylaminoethanol synthesized from diethylamine and ethylene oxide,
Alternatively, diethylaminoethanol is characterized in that discoloration over time is prevented by reducing the dissolved oxygen concentration in the liquid to 1 ppm or less by efficiently contacting it with an inert gas such as nitrogen gas without rectification. The present invention relates to a manufacturing method.

〈従来技術〉 ジエチルアミノエタノールは、ジエチルアミン
と酸化エチレンとの付加反応により合成されるも
のであり、通常液状のジエチルアミンへ酸化エチ
レンを液体または気体の状態で添加することによ
り反応し、ジエチルアミノエタノールとなる。ま
た、この時低級脂肪族アルコールを溶媒とするこ
とにより反応は非常に促進されることも知られて
いる。こうして得られたジエチルアミノエタノー
ルの反応液中にはジエチルアミノエタノール以外
に様々な化合物が含まれる。例えば原料のジエチ
ルアミン、酸化エチレン及び溶媒として使用した
アルコール、そして副反応により生成した各種化
合物等がある。これらのものは蒸溜により分離さ
れて純度の高い目的物のジエチルアミノエタノー
ルが得られる。
<Prior Art> Diethylaminoethanol is synthesized by an addition reaction between diethylamine and ethylene oxide. Usually, diethylaminoethanol is produced by adding ethylene oxide in a liquid or gaseous state to diethylamine in a liquid state. It is also known that the reaction is greatly accelerated by using a lower aliphatic alcohol as a solvent. The reaction solution of diethylaminoethanol thus obtained contains various compounds in addition to diethylaminoethanol. Examples include diethylamine as a raw material, ethylene oxide, alcohol used as a solvent, and various compounds produced by side reactions. These substances are separated by distillation to obtain the target product, diethylaminoethanol, with high purity.

〈発明が解決しようとする問題点〉 しかしながら、得られたジエチルアミノエタノ
ールは純度も99.5%以上あり、着色もAPHA5以
下と殆んど無色のものであるが、このものは経時
的に着色してくる。蒸溜の条件をさらに精密に
し、例えば蒸溜塔の段数を増加させたり、還流比
を増やしたりして純度を99.9%以上としても経時
的に着色してくることは避け難かつた。
<Problems to be solved by the invention> However, the obtained diethylaminoethanol has a purity of 99.5% or more and is almost colorless with APHA5 or less, but this product becomes colored over time. . Even if the distillation conditions were made more precise, such as by increasing the number of stages in the distillation column or increasing the reflux ratio to achieve a purity of 99.9% or higher, it was difficult to avoid coloring over time.

ジエチルアミノエタノールは、産業界において
塗料や医薬等の原料として、また各種有機合成中
間体として幅広い用途を持ち、この品質を上げる
ことは強く要望されていた。
Diethylaminoethanol has a wide range of uses in industry as a raw material for paints and medicines, and as an intermediate for various organic synthesis, and there has been a strong desire to improve its quality.

〈問題点を解決するための手段〉 そこで、本発明者は鋭意検討を重ねた結果、経
時着色の原因としてジエチルアミノエタノール中
の溶存酸素が深く関係していることを見い出し、
本発明を完成するに至つた。以下本発明について
詳細に説明する。
<Means for Solving the Problems> Therefore, as a result of extensive studies, the present inventor discovered that dissolved oxygen in diethylaminoethanol is deeply related to the cause of coloring over time.
The present invention has now been completed. The present invention will be explained in detail below.

本発明に使用されるジエチルアミノエタノール
はジエチルアミンと酸化エチレンとの反応により
得られたもので、溶媒として低級脂肪族アルコー
ルを使用したものも含まれる。低級脂肪族アルコ
ールとしては、メタノール、エタノール、n−プ
ロパノール等があげられる。ここで、得られた反
応後を蒸溜塔に導き、低沸点物及び高沸点物の不
純物を分離し、高純度のジエチルアミノエタノー
ルが得られる。ジエチルアミノエタノールの沸点
は162℃であり、常圧蒸溜では液の温度が高く、
微量の分解物が発生し、これも悪い影響が考えら
れるため、減圧蒸溜にて実施することが一般的で
ある。
The diethylaminoethanol used in the present invention is obtained by the reaction of diethylamine and ethylene oxide, and includes those using lower aliphatic alcohols as a solvent. Examples of lower aliphatic alcohols include methanol, ethanol, n-propanol, and the like. Here, the obtained reaction product is led to a distillation column to separate low-boiling point impurities and high-boiling point impurities, and high-purity diethylaminoethanol is obtained. The boiling point of diethylaminoethanol is 162℃, and the temperature of the liquid is high during atmospheric distillation.
Since a small amount of decomposition products are generated, which can also have a negative effect, distillation is generally carried out under reduced pressure.

対象原料が反応液及び半製品の場合には(再)
精溜の時、あるいは製品の場合にはそのままで、
これを窒素ガス等の不活性ガスと効率的に接触せ
しめることから成る。これらの効率的接触とは、
窒素等の不活性ガスの導入箇所及びその添加量に
よつて自ずと定まるものである。即ち、導入する
箇所は蒸溜塔の塔底でも塔項でもかまわないし、
また留出中あるいは後の液中に窒素ガス等の不活
性ガスを流通させて実施することも可能である。
添加量については特に規定されないが、実験によ
つて適宜決定される。
If the target raw materials are reaction liquids and semi-finished products (re)
At the time of rectification or in the case of products, leave it as is,
It consists of bringing this into efficient contact with an inert gas such as nitrogen gas. These efficient contacts are
This is naturally determined by the point where the inert gas such as nitrogen is introduced and the amount of the inert gas added. In other words, the introduction point may be at the bottom of the distillation column or at the column section.
It is also possible to carry out the distillation by passing an inert gas such as nitrogen gas through the liquid during or after distillation.
The amount added is not particularly specified, but is appropriately determined through experiments.

必要なことは、目的物の液中の溶存酸素濃度を
下げることである。通常、窒素ガス等の不活性ガ
スを導入しない場合の蒸溜塔からの溜出液は溶存
酸素濃度は2〜3ppmであり、経時着色を防ぐた
めには、1ppm、より好ましくは0.5ppm以下が肝
要である。
What is necessary is to lower the dissolved oxygen concentration in the target liquid. Normally, when an inert gas such as nitrogen gas is not introduced, the dissolved oxygen concentration in the distillate from a distillation tower is 2 to 3 ppm, and in order to prevent discoloration over time, it is important to keep the dissolved oxygen concentration at 1 ppm, more preferably 0.5 ppm or less. be.

〈実施例〉 以下、実施例及び比較例をもつて、詳細に説明
する。
<Example> The following is a detailed explanation using examples and comparative examples.

ここでは便宜上、経時着色に対する促進テスト
として目的物をガラス容器に密封し、80℃の恒温
槽で10時間保持した後、着色度(APHA)で評
価した。
Here, for convenience, as an accelerated test for coloration over time, the object was sealed in a glass container, kept in a constant temperature bath at 80°C for 10 hours, and then evaluated based on the degree of coloration (APHA).

実施例 1 ジエチルアミノエタノール反応液(ジエチルア
ミノエタノール93.0重量%、ジエチルアミン3.0
重量%、その他副生物4.0重量%を含有するもの)
を1000g、回分式蒸溜塔(目皿、30段)を付備し
た1の缶に仕込んだ。蒸溜塔は200mmHgの圧力
に保たれ還流比3にて精溜を行つた。この際、塔
底部にキヤピラリーにより窒素ガスを5N/Hr
で導入した。
Example 1 Diethylaminoethanol reaction solution (diethylaminoethanol 93.0% by weight, diethylamine 3.0% by weight)
(wt%) and other by-products (containing 4.0 wt%)
1000g of the distillate was charged into a can equipped with a batch distillation column (perforated plate, 30 stages). The distillation column was maintained at a pressure of 200 mmHg and rectification was performed at a reflux ratio of 3. At this time, nitrogen gas was supplied to the bottom of the tower at 5N/Hr using a capillary.
It was introduced in

初めに、低沸点物を含んだ溜分として90gと
り、さらに製品溜分として765g(純度99.9%、溶
存酸素濃度0.2ppm)が得られた。
First, 90 g of a fraction containing low-boiling substances was taken, and then 765 g of a product fraction (purity 99.9%, dissolved oxygen concentration 0.2 ppm) was obtained.

この製品のAPHAは5であつた。これを100ml
のガラス容器に密封し、80℃に保たれ恒温槽に10
時間放置した後のAPHAは8であつた。
The APHA of this product was 5. 100ml of this
Seal it in a glass container and place it in a constant temperature bath kept at 80℃ for 10 minutes.
APHA was 8 after being left for an hour.

比較例 窒素ガスを導入しない以外は実施例1と同様に
して行つた。低沸点物を含んだ溜分は95gとな
り、さらに製品溜分として725g(純度99.9%、溶
存酸素濃度2.5ppm)が得られた。
Comparative Example The same procedure as in Example 1 was carried out except that nitrogen gas was not introduced. The fraction containing low-boiling substances was 95 g, and an additional 725 g of product fraction (purity 99.9%, dissolved oxygen concentration 2.5 ppm) was obtained.

この製品のAPHAは5であり、実施例1と同
様の経時テスト後のAPHAは70であつた。
The APHA of this product was 5, and the APHA after the same aging test as in Example 1 was 70.

実施例 2 比較例で得られた製品を500g仕込液とした以
外は、実施例1と同様にして行つた。初溜分とし
て42gとり、さらに製品溜分として、355g(純度
99.9%、溶存酸素濃度0.2ppm)が得られた。
Example 2 The same procedure as in Example 1 was carried out except that 500 g of the product obtained in the comparative example was used as the charging solution. 42g was taken as the initial distillate, and 355g (purity) was taken as the product distillate.
99.9%, dissolved oxygen concentration 0.2 ppm) was obtained.

この製品のAPHAは5であり、このものの経
時テストの後のAPHAは8であつた。
The APHA of this product was 5, and the APHA of this product after time testing was 8.

実施例 3 比較例で得られた製品(APHA5、溶存酸素量
2.5ppm)を100mlのガラス容器に入れ、8mmφの
ガラス管を使用して窒素ガスを50N/Hで5時
間流通させた(常圧室温)。
Example 3 Product obtained in comparative example (APHA5, amount of dissolved oxygen
2.5ppm) was placed in a 100ml glass container, and nitrogen gas was passed through it at 50N/H for 5 hours using an 8mmφ glass tube (normal pressure and room temperature).

この製品の溶存酸素量は0.1ppmであり、この
ものの経時テスト後のAPHAは6であつた。
The dissolved oxygen content of this product was 0.1 ppm, and the APHA of this product was 6 after the aging test.

Claims (1)

【特許請求の範囲】[Claims] 1 ジエチルアミンと酸化エチレンから合成され
たジエチルアミノエタノールを精溜し、あるいは
精溜せずに、窒素ガス等の不活性ガスと効率的に
接触せしめることにより、該液中の溶存酸素濃度
を1ppm以下にすることで、経時着色を防止する
ことを特徴とするジエチルアミノエタノールの製
造方法。
1 By rectifying diethylaminoethanol synthesized from diethylamine and ethylene oxide, or without rectifying it, by bringing it into efficient contact with an inert gas such as nitrogen gas, the dissolved oxygen concentration in the liquid can be reduced to 1 ppm or less. A method for producing diethylaminoethanol, which is characterized by preventing discoloration over time.
JP114886A 1986-01-07 1986-01-07 Production of diethylamino ethanol Granted JPS62161749A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP114886A JPS62161749A (en) 1986-01-07 1986-01-07 Production of diethylamino ethanol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP114886A JPS62161749A (en) 1986-01-07 1986-01-07 Production of diethylamino ethanol

Publications (2)

Publication Number Publication Date
JPS62161749A JPS62161749A (en) 1987-07-17
JPH0560815B2 true JPH0560815B2 (en) 1993-09-03

Family

ID=11493355

Family Applications (1)

Application Number Title Priority Date Filing Date
JP114886A Granted JPS62161749A (en) 1986-01-07 1986-01-07 Production of diethylamino ethanol

Country Status (1)

Country Link
JP (1) JPS62161749A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5107028A (en) * 1991-03-18 1992-04-21 Ethyl Corporation Process for treating tert-amines
US5118852A (en) * 1991-03-18 1992-06-02 Ethyl Corporation Tert-amine treatment
US5103053A (en) * 1991-03-18 1992-04-07 Ethyl Corporation Process for treating tert-amines

Also Published As

Publication number Publication date
JPS62161749A (en) 1987-07-17

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