JP3509084B2 - Purification method of 2,6-diisopropylphenylcarbodiimide - Google Patents

Purification method of 2,6-diisopropylphenylcarbodiimide

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Publication number
JP3509084B2
JP3509084B2 JP05338895A JP5338895A JP3509084B2 JP 3509084 B2 JP3509084 B2 JP 3509084B2 JP 05338895 A JP05338895 A JP 05338895A JP 5338895 A JP5338895 A JP 5338895A JP 3509084 B2 JP3509084 B2 JP 3509084B2
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JP
Japan
Prior art keywords
diisopropylphenylcarbodiimide
methanol
purity
minutes
temperature
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 - Fee Related
Application number
JP05338895A
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Japanese (ja)
Other versions
JPH08217743A (en
Inventor
伸一 宮本
昭博 山根
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.)
Nippon Polyurethane Industry Co Ltd
Original Assignee
Nippon Polyurethane Industry Co Ltd
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Filing date
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Priority to JP05338895A priority Critical patent/JP3509084B2/en
Publication of JPH08217743A publication Critical patent/JPH08217743A/en
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Publication of JP3509084B2 publication Critical patent/JP3509084B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は2,6−ジイソプロピル
フェニルカルボジイミドの精製法に関する。
FIELD OF THE INVENTION The present invention relates to a method for purifying 2,6-diisopropylphenylcarbodiimide.

【0002】[0002]

【従来の技術】従来、2,6−ジイソプロピルフェニル
カルボジイミドの精製法としては、特公昭38−170
15号公報のように、蒸留法又は再結晶法が知られてい
る。さらに特開平5−4957号公報には、再結晶法の
溶媒としてイソプロピルアルコールを用いることが記載
されている。
2. Description of the Related Art Conventionally, a method for purifying 2,6-diisopropylphenylcarbodiimide has been disclosed in JP-B-38-170.
A distillation method or a recrystallization method is known as in JP-A-15. Further, JP-A-5-4957 describes the use of isopropyl alcohol as a solvent for the recrystallization method.

【0003】[0003]

【発明が解決しようとする課題】前述の蒸留法では、温
度200〜250℃、真空度1〜5mmHgの過酷な条
件となり、多大なエネルギーの消費となる。また、2,
6−ジイソプロピルフェニルカルボジイミド以外の物質
(異性体等)も留出せしめ、2,6−ジイソプロピルフ
ェニルカルボジイミドの純度低下を引き起こした。再結
晶法では、再結晶溶媒としてイソプロピルアルコールを
用いると、溶媒側に2,6−ジイソプロピルフェニルカ
ルボジイミドが多量に分配するため、再結晶操作を重ね
るたびに、得量が著しく低下する問題点があった。
In the above-mentioned distillation method, the conditions are severe such that the temperature is 200 to 250 ° C. and the degree of vacuum is 1 to 5 mmHg, resulting in great energy consumption. Also, 2,
Substances (such as isomers) other than 6-diisopropylphenylcarbodiimide were also distilled out, causing a decrease in the purity of 2,6-diisopropylphenylcarbodiimide. In the recrystallization method, when isopropyl alcohol is used as the recrystallization solvent, a large amount of 2,6-diisopropylphenylcarbodiimide is distributed to the solvent side, so that there is a problem that the yield is significantly reduced each time the recrystallization operation is repeated. It was

【0004】[0004]

【課題を解決するための手段】本発明者らは、前記課題
を解決するため鋭意研究した結果、2,6−ジイソプロ
ピルフェニルカルボジイミドの精製法において再結晶法
の溶媒としてメタノールを用いることにより、前記課題
が解決されることを見いだし本発明を完成するに至っ
た。すなわち本発明は、再結晶溶媒としてメタノールを
用いることを特徴とする2,6−ジイソプロピルフェニ
ルカルボジイミドの精製法である。また、再結晶の操作
を2又は3回繰り返す前記2,6−ジイソプロピルフェ
ニルカルボジイミドの精製法も本発明である。
Means for Solving the Problems The inventors of the present invention have conducted extensive studies as a result of solving the above problems, and as a result, in the purification method of 2,6-diisopropylphenylcarbodiimide, by using methanol as a solvent for the recrystallization method, The inventors have found that the problems are solved and completed the present invention. That is, the present invention is a method for purifying 2,6-diisopropylphenylcarbodiimide, which is characterized in that methanol is used as a recrystallization solvent. Further, the method for purifying the 2,6-diisopropylphenylcarbodiimide, in which the recrystallization operation is repeated 2 or 3 times, is also the present invention.

【0005】本発明を更に詳細に説明する。一般にカル
ボジイミド体の製造法は、イソシアネート化合物にアル
カリ触媒を加えて、加熱反応させる方法、チオウレア化
合物と有機金属の存在のもとで加熱反応させる方法、及
びウレア化合物に第3級アミンを添加して反応させる方
法があり、いずれの方法からも本発明に用いられる粗
2,6−ジイソプロピルフェニルカルボジイミド(以
下、粗カルボジイミド体と略す)を得ることができる。
例えば、イソシアネート化合物を使用する方法では、
2,6−ジイソプロピルアニリンにモノクロロベンゼン
溶媒を加えて濃度が40〜60重量%の混合液を作る。
その混合液にホスゲンガスを通しながら、まず60〜7
0℃でのコールド反応を行い、更に温度110〜130
℃に昇温してホット反応を行い相当するイソシアネート
化合物を得る。そのできたイソシアネート化合物を分離
蒸留することにより、2,6−ジイソプロピルフェニル
イソシアネートが得られる。粗カルボジイミド体は、上
記方法により得られた2,6−ジイソプロピルフェニル
イソシアネートに有機リン触媒を加えて温度150〜2
00℃,真空度300〜400mmHgの条件で反応さ
せることにより得られる。この粗カルボジイミド体のガ
スクロマトグラフによる純度は97%、融点は50〜5
1℃のものが得られる。
The present invention will be described in more detail. Generally, a method for producing a carbodiimide compound is a method in which an alkali catalyst is added to an isocyanate compound to cause a heat reaction, a method in which a thiourea compound and an organic metal are heated to react, and a tertiary amine is added to a urea compound. There is a method of reacting, and the crude 2,6-diisopropylphenylcarbodiimide (hereinafter, abbreviated as a crude carbodiimide compound) used in the present invention can be obtained by any method.
For example, in the method using an isocyanate compound,
A monochlorobenzene solvent is added to 2,6-diisopropylaniline to prepare a mixed solution having a concentration of 40 to 60% by weight.
While passing phosgene gas through the mixed solution, first, 60 to 7
Perform a cold reaction at 0 ° C, and further heat at 110-130.
A corresponding isocyanate compound is obtained by raising the temperature to ° C and performing a hot reaction. The resulting isocyanate compound is separated and distilled to obtain 2,6-diisopropylphenylisocyanate. The crude carbodiimide compound was prepared by adding an organic phosphorus catalyst to 2,6-diisopropylphenylisocyanate obtained by the above method, and then the temperature was 150 to 2
It is obtained by reacting at a temperature of 00 ° C. and a vacuum degree of 300 to 400 mmHg. The crude carbodiimide product had a gas chromatographic purity of 97% and a melting point of 50-5.
A product of 1 ° C. is obtained.

【0006】本発明の再結晶化操作を粗カルボジミド体
100gのスケールで説明する。スケールが大きくなれ
ば、使用する装置、時間もそれに応じて変える必要があ
る。粗カルボジミド体100gに対してメタノール15
0〜250mlを加え、内温60〜64℃まで加熱し、
15分程度混合撹拌する。その後内温を15分程度かけ
て30〜35℃まで下げ、結晶を析出させる。さらに−
10〜5℃まで30分程度かけて内温を下げ1時間程度
撹拌する。2〜3時間静置により固液2層に分離させた
のち、固体を濾過により分離して、メタノールを含んだ
精製2,6−ジイソプロピルフェニルカルボジイミド
(以下、精製カルボジイミド体と略す)を得る。さら
に、純度を上げるときは、分離した結晶物に、新しいメ
タノール100〜150mlを加え、上記操作を繰り返
し再結晶させる。その後、再結晶に用いたメタノール及
び水分を除去して精製カルボジイミド体を得る。この方
法は例えば、結晶物を60〜70℃まで加熱して溶解
し、窒素通気することでメタノールを強制飛散させ、そ
の後80〜98℃まで昇温して水分を取り除く方法が用
いられる。
The recrystallization operation of the present invention will be described on the scale of 100 g of the crude carbodiimide body. As the scale increases, the equipment used and the time needed to change accordingly. 15 g of methanol to 100 g of crude carbodiimide body
Add 0 to 250 ml and heat to an internal temperature of 60 to 64 ° C.
Mix and stir for about 15 minutes. Then, the internal temperature is lowered to 30 to 35 ° C. over about 15 minutes to precipitate crystals. Furthermore-
The internal temperature is lowered to 10 to 5 ° C over about 30 minutes, and the mixture is stirred for about 1 hour. After standing for 2-3 hours to separate into two layers of solid and liquid, the solid is separated by filtration to obtain purified 2,6-diisopropylphenylcarbodiimide containing methanol (hereinafter, abbreviated as purified carbodiimide body). Further, when increasing the purity, 100 to 150 ml of fresh methanol is added to the separated crystalline substance, and the above operation is repeated to recrystallize. Then, methanol and water used for recrystallization are removed to obtain a purified carbodiimide body. For this method, for example, a method is used in which the crystalline substance is heated to 60 to 70 ° C. to dissolve it, and nitrogen is aerated to forcefully disperse methanol, and then the temperature is raised to 80 to 98 ° C. to remove water.

【0007】[0007]

【実施例】以下に実施例、比較例により本発明について
具体的に説明するが、本発明がこれにより何等限定され
て解釈されるものではない。
EXAMPLES The present invention will be specifically described below with reference to Examples and Comparative Examples, but the present invention is not construed as being limited thereto.

【0008】実施例1 撹拌機、温度計、冷却コンデンサーを備えた500ml
容量の4つ口フラスコに、粗カルボジイミド体(ガスク
ロマトグラフによる純度97.6%、融点50.0〜5
1.0℃)100.0g及びメタノール200mlを仕
込んだ後、内温を64〜65℃に加熱し15分攪拌溶解
した。その後内温を10分程度かけて30〜35℃まで
下げ、結晶を析出させた。さらに、5℃まで30分程度
かけて内温を下げ1時間程度攪拌した。3時間静置によ
り固液2層に分離させた後、固体を濾過により分離し
た。室温で5〜10mmHgの減圧下1時間でメタノー
ルを除去し、その後35〜40℃で1昼夜乾燥して純白
色の精製2,6−ジイソプロピルフェニルカルボジイミ
ドを得た。回収量は90.1gであった。この物の融点
は51.0〜52.0℃、ガスクロマトグラフによる純
度は99.4%であった。
Example 1 500 ml equipped with stirrer, thermometer, cooling condenser
In a four-necked flask with a capacity, a crude carbodiimide compound (purity 97.6% by gas chromatography, melting point 50.0-5
(1.0 ° C.) 100.0 g and 200 ml of methanol were charged, the internal temperature was heated to 64-65 ° C., and the mixture was stirred and dissolved for 15 minutes. Then, the internal temperature was lowered to 30 to 35 ° C. over about 10 minutes to precipitate crystals. Further, the internal temperature was lowered to 5 ° C. over about 30 minutes, and the mixture was stirred for about 1 hour. After standing for 3 hours to separate into two layers of solid and liquid, the solid was separated by filtration. Methanol was removed at room temperature under reduced pressure of 5 to 10 mmHg for 1 hour, and then dried at 35 to 40 ° C for one day to obtain pure white purified 2,6-diisopropylphenylcarbodiimide. The recovered amount was 90.1 g. The melting point of this product was 51.0 to 52.0 ° C, and the purity by gas chromatography was 99.4%.

【0009】実施例2 冷却温度5℃の代わりに−10℃まで冷却した以外は実
施例1と同様に実施し純白色の結晶92.1gを得た。
この物の融点は51.0〜52.0℃、ガスクロマトグ
ラフによる純度は99.3%であった。
Example 2 92.1 g of pure white crystals were obtained in the same manner as in Example 1 except that the temperature was cooled to -10 ° C instead of 5 ° C.
The melting point of this product was 51.0 to 52.0 ° C., and the purity by gas chromatography was 99.3%.

【0010】実施例3 撹拌機、温度計、冷却コンデンサーを備えた500ml
容量の4つ口フラスコに、実施例1で用いた粗カルボジ
イミド体100.0g及びメタノール200mlを仕込
んだ後、内温を64〜65℃に加熱し15分攪拌溶解し
た。その後内温を10分程度かけて30〜35℃まで下
げ、結晶を析出させた。さらに、5℃まで30分程度か
けて内温を下げ1時間程度攪拌した。3時間静置により
固液2層に分離させた後、固体を濾過により分離して純
白色の結晶物を得た。さらに純度を上げるため、先に分
離した結晶物を4つ口フラスコに戻し新メタノール10
0mlを加え64〜65℃まで昇温した。15分混合攪
拌した後、内温を10分程度かけて30〜35℃まで下
げ、結晶を析出させた。さらに、5℃まで30分程度か
けて内温を下げ1時間程度攪拌した。3時間静置により
固液2層に分離させた後、固体を濾過により分離して純
白色の精製2,6−ジイソプロピルフェニルカルボジイ
ミドを得た。さらに、結晶物中のメタノールを完全に取
り除くため結晶物を60〜70℃まで加熱して溶解後、
窒素を吹き込んでメタノールを強制飛散させた。その後
80〜98℃まで昇温して水分を取り除き結晶物88.
7gを得た。この物の融点は51.5〜52.0℃、ガ
スクロマトグラフによる純度は99.9%であった。
Example 3 500 ml equipped with stirrer, thermometer, cooling condenser
After charging 100.0 g of the crude carbodiimide used in Example 1 and 200 ml of methanol in a four-necked flask having a capacity, the internal temperature was heated to 64 to 65 ° C. and dissolved with stirring for 15 minutes. Then, the internal temperature was lowered to 30 to 35 ° C. over about 10 minutes to precipitate crystals. Further, the internal temperature was lowered to 5 ° C. over about 30 minutes, and the mixture was stirred for about 1 hour. After allowing to stand for 3 hours to separate into two layers of solid and liquid, the solid was separated by filtration to obtain a pure white crystalline substance. In order to further raise the purity, the previously separated crystals were returned to a 4-neck flask and fresh methanol 10
0 ml was added and the temperature was raised to 64-65 ° C. After mixing and stirring for 15 minutes, the internal temperature was lowered to 30 to 35 ° C. over about 10 minutes to precipitate crystals. Further, the internal temperature was lowered to 5 ° C. over about 30 minutes, and the mixture was stirred for about 1 hour. After standing for 3 hours to separate into two layers of solid and liquid, the solid was separated by filtration to obtain pure white purified 2,6-diisopropylphenylcarbodiimide. Furthermore, in order to completely remove the methanol in the crystalline substance, the crystalline substance is heated to 60 to 70 ° C. and dissolved,
Nitrogen was blown in to forcibly scatter the methanol. Then, the temperature is raised to 80 to 98 ° C. to remove water, and the crystalline substance 88.
7 g was obtained. The melting point of this product was 51.5 to 52.0 ° C., and the purity by gas chromatography was 99.9%.

【0011】比較例1 メタノールに代えてエチルアルコールを用いた以外は実
施例1と同様に実施したが結晶は析出してこなかった。
Comparative Example 1 The same procedure as in Example 1 was carried out except that ethyl alcohol was used in place of methanol, but no crystals were deposited.

【0012】比較例2 メタノールに代えてイソプロピルアルコールを用いた以
外は実施例1と同様に実施し純白色の結晶86.5gを
得た。この物の融点は50.5〜51.5℃、ガスクロ
マトグラフによる純度は98.8%であった。
Comparative Example 2 86.5 g of pure white crystals were obtained in the same manner as in Example 1 except that isopropyl alcohol was used instead of methanol. The melting point of this product was 50.5 to 51.5 ° C, and the purity by gas chromatography was 98.8%.

【0013】比較例3 メタノールに代えてイソプロピルアルコールを用いたこ
と、冷却温度5℃の代わりに−10℃まで冷却したこと
以外は実施例1と同様に実施し純白色の結晶89.3g
を得た。この物の融点は50.5〜51.5℃、ガスク
ロマトグラフによる純度は98.5%であった。
Comparative Example 3 89.3 g of pure white crystals were prepared in the same manner as in Example 1 except that isopropyl alcohol was used in place of methanol and the temperature was cooled to -10 ° C instead of 5 ° C.
Got The melting point of this product was 50.5 to 51.5 ° C, and the purity by gas chromatography was 98.5%.

【0014】比較例4 マクマフォン入り充填塔、温度計、キャピラリー、冷却
コンデンサー、ナス型フラスコを備えた300ml容量
の4つ口ナシ型蒸留フラスコ装置に、粗カルボジイミド
体(ガスクロマトグラフによる純度97.0%、融点5
0.0〜51.0℃)100.0gを仕込減圧蒸留を行
い、塔頂より2,6−ジイソプロピルフェニルカルボジ
イミドを約152〜約162℃/0.05mmHgの条
件下で留出させ、淡黄色の結晶物85.3重量部の回収
量であった。この結晶物のガスクロマトグラフによる純
度は97.8%で、融点は50.0〜51.5℃であっ
た。
Comparative Example 4 A 300 ml capacity four-near pear-type distillation flask equipped with a packed column containing McMahon, a thermometer, a capillary, a cooling condenser, and an eggplant-shaped flask was used, and a crude carbodiimide compound (purity 97.0% by gas chromatography). , Melting point 5
(0.0-51.0 ° C) 100.0 g was charged and distilled under reduced pressure to distill 2,6-diisopropylphenylcarbodiimide from the top of the column under the conditions of about 152 to about 162 ° C / 0.05 mmHg, and a pale yellow color was obtained. The amount of crystals was 85.3 parts by weight. The gas chromatographic purity of this crystal was 97.8%, and the melting point was 50.0 to 51.5 ° C.

【0015】[0015]

【発明の効果】本発明によれば、これまで知られていた
再結晶溶媒を用いる場合や蒸留精製法よりも格段に高い
得量で、純度の良い2,6−ジイソプロピルフェニルカ
ルボジイミドが得られる。
EFFECTS OF THE INVENTION According to the present invention, 2,6-diisopropylphenylcarbodiimide having a high purity can be obtained with a much higher yield than in the case of using a known recrystallization solvent or in the distillation purification method.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 再結晶溶媒としてメタノールを用いるこ
とを特徴とする2,6−ジイソプロピルフェニルカルボ
ジイミドの精製法。
1. A method for purifying 2,6-diisopropylphenylcarbodiimide, which comprises using methanol as a recrystallization solvent.
【請求項2】 再結晶溶媒としてメタノールを用いる再
結晶の操作を2又は3回繰り返すことを特徴とする2,
6−ジイソプロピルフェニルカルボジイミドの精製法。
2. The recrystallization operation using methanol as a recrystallization solvent is repeated 2 or 3 times, 2.
A method for purifying 6-diisopropylphenylcarbodiimide.
JP05338895A 1995-02-17 1995-02-17 Purification method of 2,6-diisopropylphenylcarbodiimide Expired - Fee Related JP3509084B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05338895A JP3509084B2 (en) 1995-02-17 1995-02-17 Purification method of 2,6-diisopropylphenylcarbodiimide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05338895A JP3509084B2 (en) 1995-02-17 1995-02-17 Purification method of 2,6-diisopropylphenylcarbodiimide

Publications (2)

Publication Number Publication Date
JPH08217743A JPH08217743A (en) 1996-08-27
JP3509084B2 true JP3509084B2 (en) 2004-03-22

Family

ID=12941451

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3509084B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5290587B2 (en) * 2008-01-24 2013-09-18 帝人株式会社 Method for producing polylactic acid composition
EP3686239A1 (en) * 2019-01-23 2020-07-29 LANXESS Deutschland GmbH Hydrolytically stabilised polyethylene terephthalate (pet) - containing compositions
EP4079722A1 (en) * 2021-04-20 2022-10-26 LANXESS Deutschland GmbH Method for the preparation of carbodiimides

Also Published As

Publication number Publication date
JPH08217743A (en) 1996-08-27

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