JPS62164672A - Method for producing 1,2-dimethylimidazole - Google Patents
Method for producing 1,2-dimethylimidazoleInfo
- Publication number
- JPS62164672A JPS62164672A JP735186A JP735186A JPS62164672A JP S62164672 A JPS62164672 A JP S62164672A JP 735186 A JP735186 A JP 735186A JP 735186 A JP735186 A JP 735186A JP S62164672 A JPS62164672 A JP S62164672A
- Authority
- JP
- Japan
- Prior art keywords
- methylimidazole
- dimethylimidazole
- distillate
- small amount
- ammonia
- 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.)
- Pending
Links
- GIWQSPITLQVMSG-UHFFFAOYSA-N 1,2-dimethylimidazole Chemical compound CC1=NC=CN1C GIWQSPITLQVMSG-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- LEQAOMBKQFMDFZ-UHFFFAOYSA-N glyoxal Chemical compound O=CC=O LEQAOMBKQFMDFZ-UHFFFAOYSA-N 0.000 claims abstract description 22
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 claims abstract description 20
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 17
- MCTWTZJPVLRJOU-UHFFFAOYSA-N 1-methyl-1H-imidazole Chemical compound CN1C=CN=C1 MCTWTZJPVLRJOU-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229940015043 glyoxal Drugs 0.000 claims abstract description 12
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 6
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 239000000047 product Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 5
- 239000012736 aqueous medium Substances 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 9
- LXBGSDVWAMZHDD-UHFFFAOYSA-N 2-methyl-1h-imidazole Chemical compound CC1=NC=CN1 LXBGSDVWAMZHDD-UHFFFAOYSA-N 0.000 description 6
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- XLSZMDLNRCVEIJ-UHFFFAOYSA-N methylimidazole Natural products CC1=CNC=N1 XLSZMDLNRCVEIJ-UHFFFAOYSA-N 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- PTBPTNCGZUOCBK-UHFFFAOYSA-N 2,4,5-trimethyl-1h-imidazole Chemical compound CC1=NC(C)=C(C)N1 PTBPTNCGZUOCBK-UHFFFAOYSA-N 0.000 description 1
- -1 7cetaldehyde Chemical compound 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012533 medium component Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
本発明は品質の優れた1、2−ジメチルイミダゾールを
工業的有利に製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to an industrially advantageous method for producing 1,2-dimethylimidazole of excellent quality.
[従来の技術1
1.2−ジメチルイミダゾールは各種の有(幾薬品の中
間体としてその用途が期待される化合物である。[Prior Art 1] 1,2-Dimethylimidazole is a compound that is expected to be used as an intermediate for various chemicals.
該化合物はグリオキザール、7セトアルデヒド、メチル
アミン及びアンモニアを反応させて製造される。The compound is prepared by reacting glyoxal, 7cetaldehyde, methylamine and ammonia.
[発明が解決しようとする問題点1
しかしながら、上記の方法においては少量の1−メチル
イミダゾールの副生が避けられず、該不純物を除去して
l111#な1,2−ジメチルイミダゾールを製造する
ことが必要とされるのであるが、通常の蒸留繰作では両
者の沸点が接近しているため、完全な精製は不可能であ
る。[Problem to be solved by the invention 1 However, in the above method, a small amount of 1-methylimidazole is unavoidably produced, and it is necessary to remove this impurity to produce l111# 1,2-dimethylimidazole. However, since the boiling points of the two products are close to each other in normal distillation operations, complete purification is impossible.
[問題点を解決するための手段1
しかるに本発明者等は上記の問題点を解決し、工業的有
利に品質の良好な1,2−ツメチルイミダゾールを装遺
し得る方法を見出すべく鋭意研究を重ねた結果、(1)
グリオキザール、アセトアルデヒド、メチルアミン及び
アンモニアを反応させる工程、
(2)反応生成液を蒸留して少量の1−メチルイミダゾ
ールを含有する1、2−ジメチルイミダゾール留出液を
得る工程、
(3)留出液を冷却して1,2−ジメチルイミダゾール
を選択的に晶析させる工程、
(4)晶析物から1−メチルイミダゾールを除去する工
程
の結合よりなる方法を実施する場合、目的を達成出来る
ことを見出し、本発明を完成するに到った。[Means for Solving the Problems 1] However, the present inventors have conducted extensive research in order to solve the above problems and to find a method that can industrially advantageously incorporate 1,2-trimethylimidazole of good quality. As a result of stacking, (1)
A step of reacting glyoxal, acetaldehyde, methylamine and ammonia, (2) A step of distilling the reaction product to obtain a 1,2-dimethylimidazole distillate containing a small amount of 1-methylimidazole, (3) Distillation The objective can be achieved when carrying out a method consisting of a step of selectively crystallizing 1,2-dimethylimidazole by cooling the liquid, and (4) a step of removing 1-methylimidazole from the crystallized product. They discovered this and completed the present invention.
以下、本発明の各工程について具体的に説明する。Each step of the present invention will be specifically explained below.
第1工程
グリオキザール、アセトアルデヒド、メチルアミン及び
アンモニアを反応させて1,2−ジメチルイミダゾール
を製造する。First Step Glyoxal, acetaldehyde, methylamine and ammonia are reacted to produce 1,2-dimethylimidazole.
反応媒体は水であるが、必要に応じてメタノール、エタ
ノール、プロパツール等の水と相溶性のある有機溶媒を
少量使用しても差支えない。反応に当って、前記原料の
仕込み方法は特に制限はなく、一括仕込み、連続仕込み
、分割仕込み等任意の手段が採用できる。通常は水性媒
体中にメチルアミンを仕込み、続いてアンモニアガス(
又はアンモニア水)を徐々に導入する。その後グリオキ
ザール及びアセトアルデヒドを滴下しながら供給する。The reaction medium is water, but if necessary, a small amount of an organic solvent compatible with water such as methanol, ethanol, propatool, etc. may be used. In the reaction, the method of charging the raw materials is not particularly limited, and any method such as batch charging, continuous charging, divided charging, etc. can be adopted. Typically, methylamine is introduced into an aqueous medium, followed by ammonia gas (
or ammonia water) is gradually introduced. Glyoxal and acetaldehyde are then added dropwise.
原料の仕込み組成はモル比でグリオキザール/アセトア
ルデヒド/メチルアミン/アンモニア=1/1.0〜1
.5/1〜1.5/1〜1.5、好ましくは1/1.0
〜1.2/1.0〜1.2/1.0〜1.2の範囲が適
当である。溶媒の使用量はグリオキザール1モル当り、
100〜300m1(原料中の水等の媒体成分となるも
のを含む)が好ましい、メチルアミンとアンモニアの混
合時の反応の温度は30℃以下、好ましくは20〜30
℃が望ましい。又、グリオキザール及び7セトアルデヒ
ドの添加時には系の温度を60〜90℃、好ましくは7
0〜80℃に調整し、滴下終了後0.5〜1.0時間程
度熟成すれば1.2−ジメチルイミダゾールを含む反応
生成液が得られる。反応終了後は膣液を直接あるいは適
宜濃縮して次工程に送る。The charging composition of raw materials is glyoxal/acetaldehyde/methylamine/ammonia = 1/1.0 to 1 in molar ratio.
.. 5/1 to 1.5/1 to 1.5, preferably 1/1.0
A range of 1.2/1.0 to 1.2/1.0 to 1.2 is suitable. The amount of solvent used is per mole of glyoxal,
The reaction temperature when mixing methylamine and ammonia is preferably 100 to 300 m1 (including those serving as medium components such as water in the raw materials), and is preferably 30 to 30 °C, preferably 20 to 30 °C.
℃ is preferable. Also, when adding glyoxal and 7cetaldehyde, the temperature of the system should be 60 to 90°C, preferably 7°C.
A reaction product solution containing 1,2-dimethylimidazole can be obtained by adjusting the temperature to 0 to 80°C and aging for about 0.5 to 1.0 hours after the completion of the dropwise addition. After the reaction is completed, the vaginal fluid is sent to the next step either directly or after being concentrated as appropriate.
第2工程
反応生成液を蒸留に付す。反応液中には数々の不純物が
含有されるので、通常減圧下で蒸留する。蒸留器として
は公知の任意のものが使用可能である。蒸留条件として
は17−18Torr、90−95℃が適当である。The second step reaction product liquid is subjected to distillation. Since the reaction solution contains many impurities, it is usually distilled under reduced pressure. Any known distiller can be used. Suitable distillation conditions are 17-18 Torr and 90-95°C.
留出液の組成は1.2−ジメチルイミダゾールを主成分
として不純物として少量(約10%重量%以下)の1−
メチルイミダゾール及び溶媒(水)が含まれる。The composition of the distillate is mainly composed of 1,2-dimethylimidazole and a small amount (approximately 10% by weight or less) of 1-dimethylimidazole as an impurity.
Contains methylimidazole and solvent (water).
第3工程 上記で得られた留出液を次に冷却する。Third step The distillate obtained above is then cooled.
かかる操作によって1,2−ジメチルイミダゾールのみ
が選択的に結晶として沈澱する。冷却温度は10℃以下
、好ましくは5〜7℃程度が効率的である。高温では充
分な析出がおこらず、目的物の収率が低下する。かかる
冷却温度では1−メチルイミダゾールは液状のまま存在
するのでかかる晶析によって1,2−ジメチルイミダゾ
ールに少量の1−メチルイミダゾールや水が付着したウ
ェントケーキが得られる。By this operation, only 1,2-dimethylimidazole is selectively precipitated as crystals. The efficient cooling temperature is 10°C or less, preferably about 5 to 7°C. At high temperatures, sufficient precipitation does not occur and the yield of the target product decreases. Since 1-methylimidazole exists in a liquid state at such a cooling temperature, a wet cake in which a small amount of 1-methylimidazole and water are attached to 1,2-dimethylimidazole is obtained by such crystallization.
第4工程
かかるウェントケーキから遠心分離等の周知の手段によ
って液体が除去される。該繰作によってほぼ完全に不純
物である1−メチルイミダゾールを除くことが出来る。Fourth step: The liquid is removed from the wet cake by known means such as centrifugation. By this repeated operation, 1-methylimidazole, which is an impurity, can be almost completely removed.
必要であれば、上記の1,2−ツメチルイミダゾールの
結晶を再結晶等の周知の繰作によって精製すれば、目的
とする高純度の1.2−ジメチルイミダゾールが収得可
能である。If necessary, the desired 1,2-dimethylimidazole of high purity can be obtained by purifying the above crystals of 1,2-dimethylimidazole by a well-known process such as recrystallization.
[作 用1
本発明においては(1)〜(4)工程を実施することに
よって1−メチルイミダゾールをほとんど含有しない高
純度の1.2−ジメチルイミダゾールが製造可能である
。[Function 1] In the present invention, high purity 1,2-dimethylimidazole containing almost no 1-methylimidazole can be produced by carrying out steps (1) to (4).
[実施例1
次に実施例を挙げて本発明の方法を更に具体的に説明す
る。[Example 1] Next, the method of the present invention will be explained in more detail with reference to Examples.
実施例1
水122.4gを仕込んだ反応容器に42%メチルアミ
ン溶液133.8g(1,8モル)を室温下に導入した
。同温を保ちながら25%アンモニア水溶液122.h
(1,8モル)をゆっくり仕込んだ。系を70°Cに昇
温し、40%グリオキザール2611? (1,8モ
ル)と60%アセトアルデヒド水溶液132g(1,8
モル)の混合物を徐々に滴下した。滴下終了後、1時間
熟成して反応を終了した。Example 1 133.8 g (1.8 mol) of a 42% methylamine solution was introduced at room temperature into a reaction vessel containing 122.4 g of water. 25% ammonia aqueous solution 122. while maintaining the same temperature. h
(1.8 mol) was slowly charged. The system was heated to 70°C and 40% glyoxal 2611? (1,8 mol) and 132 g (1,8 mol) of 60% acetaldehyde aqueous solution
mol) was gradually added dropwise. After completion of the dropwise addition, the mixture was aged for 1 hour to complete the reaction.
反応生成液をロータリーエバポレーターを使用して、バ
ス温140′C″C″濃縮した後、該濃縮液を減圧蒸留
に付して90−95°C/ 1.7−18 Torrの
条件下に1,2−ノ′メチルイミグゾールを主成分とす
る留出液を得た。The reaction product liquid was concentrated using a rotary evaporator at a bath temperature of 140'C''C'', and the concentrated liquid was subjected to vacuum distillation under the conditions of 90-95°C/1.7-18 Torr. A distillate containing ,2-no'methyl imiguzole as the main component was obtained.
(1,2−ツメチルイミダゾール90%、1−メチルイ
ミダゾール9.6%、水0.4%の組成比)次にこの留
出液を攪拌下に5℃まで冷却して1.2−ツメチルイミ
ダゾールの結晶を選択的に晶析させ、上記結晶のウェッ
トケーキな得た。(Composition ratio of 1,2-methylimidazole 90%, 1-methylimidazole 9.6%, water 0.4%) Next, this distillate was cooled to 5°C with stirring and the 1.2-methylimidazole was cooled to 5°C with stirring. Methylimidazole crystals were selectively crystallized to obtain a wet cake of the above crystals.
ヌッチェ吸引ビンを使用してアスピレータ減圧下で該ウ
ェットケーキに含有される1−メチルイミダゾール及び
水を除去した。得られた1、2−ツメチルイミダゾール
中にはわずか1%の1−メチルイミダゾールが含有され
ていたに過ぎなかった。The 1-methylimidazole and water contained in the wet cake were removed under aspirator vacuum using a Nutsche suction bottle. The obtained 1,2-trimethylimidazole contained only 1% of 1-methylimidazole.
1.2−ジメチルイミダゾールの収率は仕込みグリオキ
ザールに対して74%であった。The yield of 1,2-dimethylimidazole was 74% based on the glyoxal charged.
尚、対照例として前記留出液を更に蒸留に付し、精製を
行っtこが、1,2−ン゛メチルイミダゾール及び1−
メチルイミダゾールの分離は不充分であり、実施例の如
き成績は得られなかった。As a control example, the distillate was further subjected to distillation and purified.
Separation of methylimidazole was insufficient, and results similar to those of the Examples were not obtained.
実施例2
実施例1と同一の方法を行った。次に得られた1、2−
ツメチルイミダゾールの結晶を再度熱溶融し、続いて2
5°Cまで冷却し、再結晶を行った。Example 2 The same method as in Example 1 was carried out. Then the obtained 1, 2-
The crystals of trimethylimidazole were heated and melted again, and then 2
It was cooled to 5°C and recrystallized.
1.2−ジメチルイミダゾールの純度は更に向上しく1
−メチルイミダゾールの含有率は0.1%)、着色のな
い品質の優れた結晶が得られた。1. The purity of 2-dimethylimidazole is further improved1.
- The content of methylimidazole was 0.1%), and crystals of excellent quality and no coloring were obtained.
[効 果1
本発明の方法で得られる1、2−ツメチルイミダゾール
は医薬、農薬をはじめとする各種化合物の中間体として
有用である。[Effect 1] 1,2-trimethylimidazole obtained by the method of the present invention is useful as an intermediate for various compounds including medicines and agricultural chemicals.
Claims (4)
ン及びアンモニアを反応させる工程、(1) A step of reacting glyoxal, acetaldehyde, methylamine and ammonia,
ールを含有する1,2−ジメチルイミダゾール留出液を
得る工程、(2) a step of distilling the reaction product liquid to obtain a 1,2-dimethylimidazole distillate containing a small amount of 1-methylimidazole;
を選択的に晶析させる工程、(3) cooling the distillate to selectively crystallize 1,2-dimethylimidazole;
程 の結合よりなる1,2−ジメチルイミダゾールの製造法
。(4) A method for producing 1,2-dimethylimidazole comprising the steps of removing 1-methylimidazole from a crystallized product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP735186A JPS62164672A (en) | 1986-01-16 | 1986-01-16 | Method for producing 1,2-dimethylimidazole |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP735186A JPS62164672A (en) | 1986-01-16 | 1986-01-16 | Method for producing 1,2-dimethylimidazole |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS62164672A true JPS62164672A (en) | 1987-07-21 |
Family
ID=11663533
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP735186A Pending JPS62164672A (en) | 1986-01-16 | 1986-01-16 | Method for producing 1,2-dimethylimidazole |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62164672A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005082551A (en) * | 2003-09-10 | 2005-03-31 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1-substituted imidazoles |
| JP2007095983A (en) * | 2005-09-29 | 2007-04-12 | Sanyo Chem Ind Ltd | Manufacturing method of electrolyte for electrochemical element |
| JP2007246505A (en) * | 2006-02-16 | 2007-09-27 | Sanyo Chem Ind Ltd | Production method of alkylimidazole |
| JP2007269658A (en) * | 2006-03-30 | 2007-10-18 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing dialkylimidazole and dialkylimidazole obtained thereby |
| JP2007302641A (en) * | 2006-05-15 | 2007-11-22 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1,2-disubstituted imidazole |
| JP2007320910A (en) * | 2006-06-01 | 2007-12-13 | Sanyo Chem Ind Ltd | Method for producing alkylimidazole |
| JP2012067140A (en) * | 2012-01-06 | 2012-04-05 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1,2-disubstituted imidazole |
| JP2012211122A (en) * | 2011-03-22 | 2012-11-01 | Nippon Synthetic Chem Ind Co Ltd:The | Method for production of 1,2-dialkylimidazole, and 1,2-dialkylimidazole obtained thereby |
| JP2016222615A (en) * | 2015-06-01 | 2016-12-28 | 日本合成化学工業株式会社 | Method for producing 1,2-disubstituted imidazole |
-
1986
- 1986-01-16 JP JP735186A patent/JPS62164672A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005082551A (en) * | 2003-09-10 | 2005-03-31 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1-substituted imidazoles |
| JP2007095983A (en) * | 2005-09-29 | 2007-04-12 | Sanyo Chem Ind Ltd | Manufacturing method of electrolyte for electrochemical element |
| JP2007246505A (en) * | 2006-02-16 | 2007-09-27 | Sanyo Chem Ind Ltd | Production method of alkylimidazole |
| JP2007269658A (en) * | 2006-03-30 | 2007-10-18 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing dialkylimidazole and dialkylimidazole obtained thereby |
| JP2007302641A (en) * | 2006-05-15 | 2007-11-22 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1,2-disubstituted imidazole |
| JP2007320910A (en) * | 2006-06-01 | 2007-12-13 | Sanyo Chem Ind Ltd | Method for producing alkylimidazole |
| JP2012211122A (en) * | 2011-03-22 | 2012-11-01 | Nippon Synthetic Chem Ind Co Ltd:The | Method for production of 1,2-dialkylimidazole, and 1,2-dialkylimidazole obtained thereby |
| JP2012067140A (en) * | 2012-01-06 | 2012-04-05 | Nippon Synthetic Chem Ind Co Ltd:The | Method for producing 1,2-disubstituted imidazole |
| JP2016222615A (en) * | 2015-06-01 | 2016-12-28 | 日本合成化学工業株式会社 | Method for producing 1,2-disubstituted imidazole |
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