JPH01139568A - Production of 4-methylimidazole - Google Patents

Production of 4-methylimidazole

Info

Publication number
JPH01139568A
JPH01139568A JP29610487A JP29610487A JPH01139568A JP H01139568 A JPH01139568 A JP H01139568A JP 29610487 A JP29610487 A JP 29610487A JP 29610487 A JP29610487 A JP 29610487A JP H01139568 A JPH01139568 A JP H01139568A
Authority
JP
Japan
Prior art keywords
ammonia
mgx
formaldehyde
reaction
ammonium sulfate
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
Application number
JP29610487A
Other languages
Japanese (ja)
Inventor
Koichi Takeuchi
竹内 黄一
Kenichi Arai
研一 荒井
Mitsuaki Senda
光昭 千田
Mitsuo Itakura
板倉 光雄
Naokazu Shiotani
塩谷 直和
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP29610487A priority Critical patent/JPH01139568A/en
Publication of JPH01139568A publication Critical patent/JPH01139568A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title substance in high purity and yield, by reacting methylglyoxal with formaldehyde and ammonium in the presence of ammonium sulfate while retaining pH to low region using a lower fatty acid and ammonia. CONSTITUTION:Methylglyoxal(MGX) is reacted with formaldehyde and ammonia in the presence of ammonium sulfate at 70-80 deg.C for 2-5hr while retaining pH to 2-4 by a lower fatty acid (e.g., acetic acid or formic acid) and ammonia to provide the title substance useful as an intermediate for medicine. The reaction method is carried out by adding a lower fatty acid to ammonium sulfate to afford an aqueous solution adjusted to pH2-4 and dropping a mixture of MGX and formaldehyde or each simultaneously MGX and formaldehyde to the aqueous solution while adding ammonium water solution or ammonia gas thereto. According to the above-mentioned method, production of methylene bisimidazoles which are by-products is suppressed and the production process is simplified.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、高純度4−メチルイミダゾール(以下、4−
Mlと略記する。)の製造方法に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention provides high purity 4-methylimidazole (hereinafter referred to as 4-methylimidazole).
It is abbreviated as Ml. ).

4−1’IIは医薬品を製造するための価値ある中間体
である。
4-1'II is a valuable intermediate for manufacturing pharmaceuticals.

〔従来の技術〕[Conventional technology]

4−門Iの製造方法としては米国特許第3,715.3
65号に記載がある。該発明は電離定数がt x to
−3より大きい酸のアンモニウム塩を用い、PH7以下
の水媒体中でグリオキザール又はメチルグリオキザール
(以下、MGKと略記する。)をホルムアルデヒドと反
応させて、イミダゾール類を製造するものであり、核酸
として特に硫酸アンモニウム及び蓚酸を挙げている。
4-A method for producing phylum I is described in U.S. Patent No. 3,715.3.
It is stated in No. 65. The invention has an ionization constant of t x to
Imidazole is produced by reacting glyoxal or methylglyoxal (hereinafter abbreviated as MGK) with formaldehyde in an aqueous medium with a pH of 7 or less using an ammonium salt of an acid larger than -3, and is particularly useful as a nucleic acid. Ammonium sulfate and oxalic acid are listed.

MGXから4−Mlを製造する具体例としては、MGX
 。
As a specific example of producing 4-Ml from MGX, MGX
.

硫酸アンモニウム及びホルムアルデヒドを混合し、これ
にアンモ斗ア水を滴下して、PH4,7からPH4,4
で反応せしめ、その後、水酸化カルシウムを添加して、
アンモニアを飛散させ、硫酸根を硫酸カルシウムとして
沈澱させ、沈澱物を濾別した後、脱水、蒸留して4−M
Iを得ると開示している。しかしながら、その製品純度
はガスクロマトグラフ分析による面積純度で77.2%
、収率は59%である。
Mix ammonium sulfate and formaldehyde, add ammonia water dropwise to this, and adjust the pH from 4.7 to 4.4.
to react, then add calcium hydroxide,
Ammonia is scattered, sulfate radicals are precipitated as calcium sulfate, the precipitate is filtered, dehydrated and distilled to produce 4-M
It is disclosed that I will be obtained. However, the product purity is 77.2% based on area purity as determined by gas chromatography analysis.
, the yield is 59%.

医薬中間体として用いるには、更に精製操作が必要とな
り、そのため収率が低下し、該方法は満足なものではな
い、また、特開昭57−9766には前記米国特許を改
良する方法として、PI(が7以上の条件下、原料の供
給順序に特徴をもたせて、アンモニアとアルデヒドとM
GXを反応させて、4−MIを得ることが開示されてい
る。 PHが7以上で、且つアンモニアを用いることに
より、反応器の腐食の問題及び大量のvA@塩溶液によ
る余分の操作が必要なくなり、米国特許第3,715,
365号より有利であると示されている。
For use as a pharmaceutical intermediate, further purification operations are required, resulting in a lower yield, and the method is not satisfactory. In addition, Japanese Patent Application Laid-Open No. 57-9766 discloses a method for improving the above-mentioned U.S. patent. Under conditions where PI (is 7 or more), ammonia, aldehyde and M
It is disclosed that 4-MI is obtained by reacting GX. By having a pH of 7 or more and using ammonia, the problem of reactor corrosion and the need for extra operations with large volumes of vA@salt solution are avoided, and U.S. Patent No. 3,715,
No. 365 has been shown to be more advantageous.

しかし、実施例に示されるごと<、PH9,2〜9.4
の領域で反応すると?IGχの分解が起こり、アセトア
ルデヒドが生成し、2.4−ジメチルイミダゾール(以
下、D旧と略記する。)の副生が多くなる。該特許では
、この副生を抑制するために希薄溶液で実施しているが
完全でない。
However, as shown in the examples, pH9.2-9.4
What if you react in the area of ? Decomposition of IGχ occurs, acetaldehyde is produced, and a large amount of 2,4-dimethylimidazole (hereinafter abbreviated as D-old) is produced as a by-product. In this patent, a dilute solution is used to suppress this by-product, but it is not perfect.

更に特開昭60−104072号及び特開昭60−10
5664号では、米国特許第3,715,365号の改
良法として、MGXに対して総水量を規制することによ
り、高純度の4−Mlを高収率で得ているが、米国特許
と同じようにアンモニア源として蓚酸アンモニウムを用
いるために、4−旧の蓚酸塩の濾過及びアンモニアで同
温を分解した後の蓚酸アンモニウムの濾過と濾過工程が
多く、プロセスが複雑となり、経済的でない。
Furthermore, JP-A-60-104072 and JP-A-60-10
No. 5664 is an improved method of U.S. Patent No. 3,715,365, in which high-purity 4-Ml is obtained at a high yield by regulating the total amount of water for MGX, but it is the same as the U.S. patent. In order to use ammonium oxalate as an ammonia source, there are many steps such as filtration of 4-old oxalate, filtration of ammonium oxalate after decomposition of the same temperature with ammonia, and the process becomes complicated and uneconomical.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明者らは、DMIの副生及び4−MI 2モルとホ
ルムアルデヒド1モルより生成するメチレンビスイミダ
ゾール類の副生を抑制し、且つ反応濃度が濃く、濾過等
の複雑な工程を含まない、簡略化された工業的に容易に
実施可能な、高純度、高収率の4−旧が得られるプロセ
スを開発すべく検討した。
The present inventors suppressed the by-product of DMI and the by-product of methylene bisimidazoles generated from 2 moles of 4-MI and 1 mole of formaldehyde, and the reaction concentration was high, and it did not involve complicated steps such as filtration. A study was carried out to develop a simplified process that can be easily carried out industrially and which can obtain 4-old with high purity and high yield.

〔問題点を解決するための手段および作用〕本発明者ら
は、原料のMGXの分解によって生成するアセトアルデ
ヒドが副生成物であるDMIの生成の原因であること、
そのMGXが低PHeI域では安定であること、メチレ
ンビスイミダゾール類も低P!(領域では抑制されるこ
とを見出し、本発明を完成させるに至った。
[Means and effects for solving the problem] The present inventors have discovered that acetaldehyde produced by decomposition of the raw material MGX is the cause of the production of the by-product DMI;
MGX is stable in the low PHeI range, and methylene bisimidazoles are also low P! (We have found that this can be suppressed in this region, and have completed the present invention.)

即ち、本発明は、メチルグリ゛オキザール、ホルムアル
デヒドとアンモニアとを硫酸アンモニウム存在下、低級
脂肪酸及びアンモニアを用いてPHを2〜4に保ちなが
ら、反応させることを特徴とする4−メチルイミダゾー
ルの製造方法である。
That is, the present invention is a method for producing 4-methylimidazole, which is characterized by reacting methylglyoxal, formaldehyde, and ammonia in the presence of ammonium sulfate while maintaining the pH at 2 to 4 using a lower fatty acid and ammonia. be.

本発明を詳述すれば、本発明は、硫酸アンモニウムの存
在下、低級脂肪酸及びアンモニアを用いてPH2〜4に
Iilながら、MGXとホルムアルデヒドを水媒体中で
反応させることを特徴とする4−[の製造方法である。
More specifically, the present invention is characterized in that MGX and formaldehyde are reacted in an aqueous medium using a lower fatty acid and ammonia in the presence of ammonium sulfate while adjusting the pH to 2 to 4. This is the manufacturing method.

P)Iが4を超えると、DMTは勿論のことメチレンビ
スイミダゾール類の副生が多くなり、収率が低下し、且
つ、4−1ffとDFIIが箔単に分離することが不可
能なため純度も低下する。
P) If I exceeds 4, not only DMT but also methylene bisimidazoles will be produced as by-products, resulting in a lower yield, and it will be difficult to separate 4-1ff and DFII using a foil, resulting in poor purity. also decreases.

一方、PHが2未満では、急激に反応速度が遅くなり、
反応が完全に終了しないので好ましくない。
On the other hand, when the pH is less than 2, the reaction rate decreases rapidly,
This is not preferred because the reaction does not complete completely.

反応を終了させるまで長時間を要するか或いは短時間で
も高温で反応させると重合物が増加し、収率が低下する
If it takes a long time to complete the reaction or if the reaction is carried out at a high temperature even for a short time, the amount of polymerized products increases and the yield decreases.

本発明では原料中に水が入っているので水媒体中で反応
させることになる。
In the present invention, since water is contained in the raw materials, the reaction is carried out in an aqueous medium.

本発明の製造方法によれば、硫酸アンモニウムの存在下
、MGXとホルムアルデヒド及びアンモニアとを反応さ
せるが、硫酸アンモニウムの使用量はMGXに対して1
以上であれば良く、アンモニアは反応に使用されると共
に反応P)Iを2〜4に維持するために使用されるので
、モル比は2以上となる。
According to the production method of the present invention, MGX is reacted with formaldehyde and ammonia in the presence of ammonium sulfate, and the amount of ammonium sulfate used is 1 to MGX.
The molar ratio will be 2 or more since ammonia is used in the reaction and is also used to maintain the reaction P)I at 2 to 4.

ホルムアルデヒドの過剰は、MGXに対して1.1倍程
度は可能であるが、それを越えると副反応を促進し、不
都合である。また1未満となるとDMIの副生が増加し
、好ましくない。
It is possible to use formaldehyde in excess of about 1.1 times that of MGX, but if it exceeds this, side reactions will be promoted, which is disadvantageous. Moreover, if it is less than 1, the by-product of DMI will increase, which is not preferable.

反応温度は50〜ioo ’c、好ましくは70〜80
℃が良い。
The reaction temperature is 50-ioo'c, preferably 70-80
℃ is good.

反応時間は温度に依存するが2〜5時間で良い。The reaction time depends on the temperature, but may be 2 to 5 hours.

反応方法としては、反応進行中のPHを2〜4に維持す
るために、硫酸アンモニウムに低級脂肪酸を加えてPH
2〜4とした水溶液にMGXとホルムアルデヒドの混合
液を滴下、若しくはMGXとホルムアルデヒドを各々同
時に滴下させながら、アンモニア水溶液又はアンモニア
ガスを追加して反応を実施する。
The reaction method involves adding lower fatty acids to ammonium sulfate to maintain the pH during the reaction between 2 and 4.
A mixture of MGX and formaldehyde is added dropwise to the aqueous solution prepared in Examples 2 to 4, or an ammonia aqueous solution or ammonia gas is added while simultaneously dropping MGX and formaldehyde to carry out the reaction.

前記の方法で反応が終了した反応系中には、4−?lI
の硫酸塩及び低級脂肪酸塩が生成しているので、反応系
をアルカJJ性にして、溶媒で抽出後、減圧蒸留して4
−Mlを分取する。
In the reaction system where the reaction was completed by the above method, 4-? lI
Since sulfates and lower fatty acid salts of
- Separate Ml.

〔実施例〕〔Example〕

以下、実施例を挙げ本発明を具体的に説明する。 The present invention will be specifically described below with reference to Examples.

実施例1′ 攪拌機、還流コンデンサー付の12ガラス製セパラブル
フラスコに蒸留水316.9g、硫酸アンモニウム14
5.4gを仕込み、溶解後、更に酢酸14.8gを仕込
んで、PHを3とし、80°Cまで昇温する。昇温後、
80°CでP)lの微調節を行い、PH3を確認後、4
0重量%MGX水溶液177.6gと37重量%ホルマ
リン80.8gの混合液を2時間で滴下した。その間P
H3を維持するために28重量%アンモニア水溶液51
.9gを追加しながら行った0滴下終了後、同じPH値
で2時間熟成反応を行い、反応を完結させた。
Example 1' 316.9 g of distilled water and 14 ammonium sulfate were placed in a 12 glass separable flask equipped with a stirrer and a reflux condenser.
5.4 g was charged, and after dissolving, 14.8 g of acetic acid was further charged, the pH was adjusted to 3, and the temperature was raised to 80°C. After raising the temperature,
After finely adjusting P)l at 80°C and confirming PH3,
A mixed solution of 177.6 g of 0 wt % MGX aqueous solution and 80.8 g of 37 wt % formalin was added dropwise over 2 hours. Meanwhile P
28 wt% ammonia aqueous solution 51 to maintain H3
.. After 0 dropwise addition, which was carried out while adding 9 g, the aging reaction was carried out for 2 hours at the same pH value to complete the reaction.

HPLC分析結果、4−M1収率(対MGX、以下同じ
)は87.5%、DMI(対MGX、以下同じ)0.2
5%であった。
As a result of HPLC analysis, the yield of 4-M1 (relative to MGX, the same applies below) is 87.5%, and the DMI (relative to MGX, the same applies below) is 0.2.
It was 5%.

実施例2 実施例1と同様の反応器を用い、蒸留水316.9g、
硫酸アンモニウム145.4gを仕込み、80°Cに昇
温しで熔解させ、更に酢酸0.5gを仕込んでPHを4
とした。PH4を確認後、40重量%MGX水溶液17
7.6gと37重量%ホルマリン80.8gの混合液を
2時間で滴下した。その間PH4を維持するために28
重量%アンモニア水溶液63.8gを追加しながら行っ
た。滴下終了後、同じPH値で2時間熟成反応を行い、
反応を完結させた。 HPLC分析結果、4−旧収率は
86.0%、DM+収率は0.44%であった。
Example 2 Using a reactor similar to Example 1, 316.9 g of distilled water,
Charge 145.4 g of ammonium sulfate, raise the temperature to 80°C to melt it, and then charge 0.5 g of acetic acid to adjust the pH to 4.
And so. After confirming PH4, 40% by weight MGX aqueous solution 17
A mixed solution of 7.6 g and 80.8 g of 37% by weight formalin was added dropwise over 2 hours. 28 to maintain pH4 during that time.
The process was carried out while adding 63.8 g of a wt% ammonia aqueous solution. After completing the dropwise addition, an aging reaction was carried out for 2 hours at the same pH value.
The reaction was completed. HPLC analysis results showed that the 4-old yield was 86.0% and the DM+ yield was 0.44%.

実施例3 実施例1と同様の反応器を用い、蒸留水316.9g、
硫酸アンモニウム145.4gを仕込み、80°Cに昇
温しで溶解させ、更に酢酸0.5gを仕込んでPHを4
とした。PH4を確認後、40重量%門GX水溶液17
7.6gと37重量%ホルマリン80.8gの混合液を
2時間で滴下した。その間PH2,5を維持するために
28重量%アンモニア水溶液56.9gを追加しながら
行った。
Example 3 Using the same reactor as in Example 1, 316.9 g of distilled water,
Charge 145.4 g of ammonium sulfate, raise the temperature to 80°C to dissolve it, and then charge 0.5 g of acetic acid to adjust the pH to 4.
And so. After confirming PH4, add 40% by weight GX aqueous solution 17
A mixed solution of 7.6 g and 80.8 g of 37% by weight formalin was added dropwise over 2 hours. During this time, 56.9 g of a 28% by weight ammonia aqueous solution was added to maintain the pH at 2.5.

滴下終了後、同じPH値で2時間熟成反応を行い、反応
を完結させた。HPLC分析結果、4−旧収率は87.
9%、DMI収率は0.33%であった。
After completion of the dropwise addition, an aging reaction was carried out for 2 hours at the same pH value to complete the reaction. As a result of HPLC analysis, the 4-former yield was 87.
9%, and the DMI yield was 0.33%.

実施例4 実施例1と同様の反応器を用い、葺留水316.9g、
硫酸アンモニウム145.4gを仕込み、80°Cに昇
温しで溶解させ、更に蟻酸0.2gを仕込んでPHを4
とした。PH4を確認後、40重量%MGX水溶液17
7.6gと37重量%ホル゛?リン80.8gの混合液
を2時間で滴下した。その間PH4を維持するために2
8重景%アンモニア水溶液60.3gを追加しながら行
った。滴下終了後、同じPH値で2時間熟成反応を行い
、反応を完結させた。HPLC分析結果、4−M1収率
は85.7%、D[収率は0.41%であった。
Example 4 Using the same reactor as in Example 1, 316.9 g of Fukidashi water,
Charge 145.4 g of ammonium sulfate, raise the temperature to 80°C to dissolve it, and further charge 0.2 g of formic acid to adjust the pH to 4.
And so. After confirming PH4, 40% by weight MGX aqueous solution 17
7.6g and 37% by weight hol? A mixed solution containing 80.8 g of phosphorus was added dropwise over 2 hours. 2 to maintain pH4 during that time.
This was carried out while adding 60.3 g of an 8% ammonia aqueous solution. After completion of the dropwise addition, an aging reaction was carried out for 2 hours at the same pH value to complete the reaction. As a result of HPLC analysis, the yield of 4-M1 was 85.7% and the yield of D was 0.41%.

比較例1 実施例1において、酢酸を添加せず、硫酸アンモニウム
のみとし、そのままのPH5,1を28重量%アンモニ
ア水溶液を追加して維持しながら、実施例1と同じよう
に反応を行った。その結果、4−M1収率は80%、D
旧収率は0.62%であった。
Comparative Example 1 The reaction was carried out in the same manner as in Example 1, without adding acetic acid, using only ammonium sulfate, and maintaining the same pH of 5.1 by adding a 28% by weight ammonia aqueous solution. As a result, the 4-M1 yield was 80%, D
The previous yield was 0.62%.

比較例2 比較例1において、28重量%アンモニア水溶液の追加
はなく、反応にしたがってPI(が低下するままに反応
を行った。熟成反応2時間後のPHは1.2であり、そ
の結果、4−M1収率は79.4%、DMI収率は0.
77%であった。
Comparative Example 2 In Comparative Example 1, the 28 wt % ammonia aqueous solution was not added, and the reaction was carried out with the PI decreasing as the reaction progressed. The pH after 2 hours of the aging reaction was 1.2, and as a result, 4-M1 yield was 79.4%, DMI yield was 0.
It was 77%.

〔発明の効果〕〔Effect of the invention〕

本発明の方法によって得られた4−旧は、特別の精製を
しなくても純度は97%以上で、D旧収率は1%以下で
あり、4−旧収率は85%を下がることはない。
The 4-old obtained by the method of the present invention has a purity of 97% or more without special purification, and the D-old yield is 1% or less, and the 4-old yield is less than 85%. There isn't.

特許出願人  三井東圧化学株式会社Patent applicant: Mitsui Toatsu Chemical Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] (1)メチルグリオキザール、ホルムアルデヒドとアン
モニアとを硫酸アンモニウム存在下、低級脂肪酸及びア
ンモニアを用いてPHを2〜4に保ちながら、反応させ
ることを特徴とする4−メチルイミダゾールの製造方法
(1) A method for producing 4-methylimidazole, which comprises reacting methylglyoxal, formaldehyde, and ammonia in the presence of ammonium sulfate while keeping the pH at 2 to 4 using a lower fatty acid and ammonia.
(2)低級脂肪酸が酢酸または蟻酸である特許請求の範
囲第1項記載の方法。
(2) The method according to claim 1, wherein the lower fatty acid is acetic acid or formic acid.
JP29610487A 1987-11-26 1987-11-26 Production of 4-methylimidazole Pending JPH01139568A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29610487A JPH01139568A (en) 1987-11-26 1987-11-26 Production of 4-methylimidazole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29610487A JPH01139568A (en) 1987-11-26 1987-11-26 Production of 4-methylimidazole

Publications (1)

Publication Number Publication Date
JPH01139568A true JPH01139568A (en) 1989-06-01

Family

ID=17829184

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29610487A Pending JPH01139568A (en) 1987-11-26 1987-11-26 Production of 4-methylimidazole

Country Status (1)

Country Link
JP (1) JPH01139568A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6177575B1 (en) * 1998-06-12 2001-01-23 E. I. Du Pont De Nemours And Company Process for manufacture of imidazoles

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6177575B1 (en) * 1998-06-12 2001-01-23 E. I. Du Pont De Nemours And Company Process for manufacture of imidazoles

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