JP2002069049A - Method for producing hydrazodicarbonamide - Google Patents

Method for producing hydrazodicarbonamide

Info

Publication number
JP2002069049A
JP2002069049A JP2000262638A JP2000262638A JP2002069049A JP 2002069049 A JP2002069049 A JP 2002069049A JP 2000262638 A JP2000262638 A JP 2000262638A JP 2000262638 A JP2000262638 A JP 2000262638A JP 2002069049 A JP2002069049 A JP 2002069049A
Authority
JP
Japan
Prior art keywords
hydrazodicarbonamide
reaction
producing
urea
general formula
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
JP2000262638A
Other languages
Japanese (ja)
Inventor
Takashi Konishi
隆 小西
Toshihiro Nomura
俊広 野村
Kiyoshi Yoshida
浄 吉田
Isamu Masumoto
勇 増本
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co 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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP2000262638A priority Critical patent/JP2002069049A/en
Publication of JP2002069049A publication Critical patent/JP2002069049A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing hydrazodicarbonamide in high yield. SOLUTION: This method for producing hydrazodicarbonamide is characterized in that a ketazine or a hydrazone is reacted with urea in the presence of soluble salts under a reduced pressure condition.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ゴムまたは樹脂用
途の熱分解型発泡剤であるアゾジカルボンアミドの合成
中間体として有用なヒドラゾジカルボンアミドの製造方
法に関するものである。
The present invention relates to a method for producing hydrazodicarbonamide useful as an intermediate for synthesizing azodicarbonamide which is a pyrolytic foaming agent for rubber or resin applications.

【0002】[0002]

【従来の技術】ヒドラゾジカルボンアミドの製造方法と
して、例えば(1)非酸化性鉱酸存在下でヒドラジンハ
イドレートまたはその塩類と尿素とを加熱反応させる方
法、(2)ケタジンと尿素とを水性媒体中、副生するケ
トンとアンモニアを常圧条件で系外に取り出しつつ加熱
反応させる方法などが挙げられる。
2. Description of the Related Art As a method for producing hydrazodicarbonamide, for example, (1) a method in which hydrazine hydrate or a salt thereof is reacted with urea in the presence of a non-oxidizing mineral acid, and (2) a method in which ketazine and urea are aqueous A method in which ketone and by-produced by-product and ammonia are taken out of the system under normal pressure conditions in the medium and heated and reacted is exemplified.

【0003】しかし、(1)の方法では、副生するアン
モニア当量に相当する量以上の非酸化性鉱酸を必要とす
るだけでなく、残液を廃水処理するには高度な処方を要
するという欠点がある。(2)の方法では、副生するケ
トンを系外に除去するためには比較的温度を上げて反応
を行わねばならず、その結果余剰尿素の熱分解による不
純物の生成が促進され、その不純物が目的物の品質悪
化、反応液の使用可能時間の低下、炭酸アンモニウムの
析出によるアンモニア、ケトン回収ラインの閉塞などの
悪影響を与えるという欠点がある。
[0003] However, the method (1) requires not only a non-oxidizing mineral acid in an amount equal to or more than the by-equivalent ammonia equivalent, but also requires a high-level formulation to treat the residual liquid as wastewater. There are drawbacks. In the method (2), in order to remove the by-product ketone out of the system, the reaction must be performed at a relatively high temperature. As a result, the generation of impurities due to thermal decomposition of excess urea is promoted, and the impurities are removed. However, there is a drawback in that the quality of the target product is deteriorated, the usable time of the reaction solution is reduced, and the ammonia and ketone recovery lines are blocked due to precipitation of ammonium carbonate.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、従来
技術における上記したような課題を解決し、尿素の分解
が少なくかつ高収率、高品質のヒドラゾジカルボンアミ
ドを製造する方法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems in the prior art and to provide a method for producing hydrazodicarbonamide of high quality with a low yield of urea, low yield and high yield. Is to do.

【0005】[0005]

【課題を解決するための手段】本発明者らは、鋭意研究
を重ねた結果、反応を減圧下で行い、副生するケトンと
アンモニアを強制的に系外に取り出すことにより低温で
も高収率で得、かつ尿素の熱分解を抑制することのでき
るヒドラゾジカルボンアミドの製造方法を見いだし本発
明に到達した。
Means for Solving the Problems As a result of intensive studies, the present inventors have conducted a reaction under reduced pressure, and forcibly taken out by-product ketone and ammonia out of the system to obtain a high yield even at a low temperature. And found a method for producing hydrazodicarbonamide which can suppress the thermal decomposition of urea, and reached the present invention.

【0006】すなわち本発明は、溶性塩類存在下、一般
式(1)で表される化合物と尿素とを減圧条件下で反応
させることを特徴とするヒドラゾジカルボンアミドの製
造方法に関するものである。
That is, the present invention relates to a method for producing hydrazodicarbonamide, comprising reacting a compound represented by the general formula (1) with urea under reduced pressure in the presence of a soluble salt.

【0007】[0007]

【化3】 {式中R1、R2はアルキル基を示す。これらは互いに結
合していてもよい。また、A−は、
Embedded image 中 In the formula, R 1 and R 2 each represent an alkyl group. These may be bonded to each other. A- is

【化4】 (式中R1、R3はアルキル基を示す。これらは互いに結
合していてもよい。)}
Embedded image (In the formula, R 1 and R 3 represent an alkyl group. These may be bonded to each other.)

【0008】[0008]

【発明の実施の形態】一般式(1)で表される化合物と
して、ヒドラゾン、ケタジンが挙げられる。ケタジンと
しては、アセトンアジン、メチルエチルアジンが挙げら
れる。これらは、単独、混合物のいずれでも使用でき
る。
BEST MODE FOR CARRYING OUT THE INVENTION Examples of the compound represented by the general formula (1) include hydrazone and ketazine. Examples of ketazine include acetone azine and methyl ethyl azine. These can be used alone or as a mixture.

【0009】本発明では、尿素、可溶性塩類、水性溶媒
の混合液に対して一般式(1)の化合物を連続的に加え
ることが好ましく、添加速度も一定でなくともよい。ま
た、一般式(1)の化合物と尿素を同時に加えてもよ
い。尿素の量は、一般式(1)の化合物に対して2〜1
5倍モル、好ましくは2.5〜6.0倍モルである。
In the present invention, it is preferable to continuously add the compound of the general formula (1) to a mixture of urea, soluble salts and an aqueous solvent, and the addition rate may not be constant. Further, the compound of the general formula (1) and urea may be added at the same time. The amount of urea is 2 to 1 based on the compound of the general formula (1).
It is 5 moles, preferably 2.5 to 6.0 moles.

【0010】可溶性塩類としては、酸化能力を有さず、
水に対する溶解度が0.1重量%以上である金属塩また
はアンモニウム塩類であれば、公知の化合物が使用でき
る。具体的には、硫酸アンモニウム、硝酸アンモニウ
ム、蟻酸ナトリウムなどを挙げることができる。これら
は、単独、混合いずれにおいても使用可能である。可溶
性塩類の使用量は、一般式(1)の化合物に対して0.
01〜3.0倍モル、好ましくは0.1〜2.0倍モル
である。
As soluble salts, they have no oxidizing ability,
Known compounds can be used as long as they are metal salts or ammonium salts having a solubility in water of 0.1% by weight or more. Specific examples include ammonium sulfate, ammonium nitrate, and sodium formate. These can be used either alone or as a mixture. The amount of the soluble salts to be used is 0.1 to the compound of the general formula (1).
The molar amount is from 01 to 3.0 times, preferably from 0.1 to 2.0 times.

【0011】本発明で用いる水性媒体は、水または水に
可溶なメタノール、エチレングリコールなどのアルコー
ル類である。これらは、単独、混合いずれにおいても使
用可能である。
The aqueous medium used in the present invention is water or water-soluble alcohols such as methanol and ethylene glycol. These can be used either alone or as a mixture.

【0012】本発明では、減圧条件下で反応を行うこと
により、強制的に副生するケトンとアンモニアを系外に
除去する。揮発性副生物との分離能力を要した十分な分
留管を取り付けた上で反応を行うことが望ましく、その
系内の圧力は66500〜99750Pa、好ましくは
66500〜86450Paである。反応温度は60〜
150℃、好ましくは60〜105℃である。反応進行
度合いなどにより変更しても良い。
In the present invention, by carrying out the reaction under reduced pressure, the by-product ketone and ammonia are forcibly removed from the system. It is desirable to carry out the reaction after attaching a sufficient fractionation pipe which requires a separating ability for volatile by-products, and the pressure in the system is 66500 to 99750 Pa, preferably 66500 to 86450 Pa. Reaction temperature is 60 ~
The temperature is 150C, preferably 60 to 105C. It may be changed depending on the degree of reaction progress.

【0013】[0013]

【実施例】次の実施例によって本発明をさらに詳細に説
明する。
The present invention will be described in more detail with reference to the following examples.

【0014】実施例1 尿素330g(5.5mol)、硫酸アンモニウム13
2g(1.0mol)及び水272gを攪拌機、温度
計、十分な能力を有する減圧分留装置、加熱浴を備えた
1l4つ口フラスコに添加した。混合液を攪拌しながら
加熱し、液温が102℃に達したら、四つ口フラスコに
備えた滴下ポンプから95%メチルエチルケタジン14
7g(1.0mol)を定常的に3時間かけて滴下し
た。滴下終了後さらに1時間反応させた。副生するケト
ン及びアンモニアを強制留去させるため、アスピレータ
ーを使用して減圧条件下で反応を行い、ケタジンが留出
しないよう減圧度を79800Pa前後に適宜調節し
た。反応液の温度は102〜103℃であった。
Example 1 330 g (5.5 mol) of urea, ammonium sulfate 13
2 g (1.0 mol) and 272 g of water were added to a 11-neck four-necked flask equipped with a stirrer, a thermometer, a vacuum fractionator having a sufficient capacity, and a heating bath. The mixture was heated with stirring, and when the temperature of the mixture reached 102 ° C., 95% methyl ethyl ketazine 14 was supplied from a dropping pump provided in the four-necked flask.
7 g (1.0 mol) was constantly added dropwise over 3 hours. After the completion of the dropwise addition, the reaction was further performed for 1 hour. The reaction was carried out under reduced pressure using an aspirator in order to forcibly remove by-produced ketone and ammonia, and the degree of reduced pressure was appropriately adjusted to about 79800 Pa so that ketazine was not distilled off. The temperature of the reaction solution was 102 to 103 ° C.

【0015】反応終了後、液温を60℃まで冷却し、生
成したヒドラゾジカルボンアミドの白色結晶を炉別した
後、さらに水で十分に洗浄した。この白色結晶を110
℃で乾燥秤量したところ108.3gであった。これ
は、滴下したケタジンに対して91.7%であった。ま
た、尿素を基準としたヒドラゾジカルボンアミドの選択
率は98.4%であり、分留装置、留出ラインなどに炭
酸アンモニウムの析出はみられなかった。
After the completion of the reaction, the liquid temperature was cooled to 60 ° C., and the formed white crystals of hydrazodicarbonamide were filtered off, and then sufficiently washed with water. This white crystal is
Dry weighing at 10 ° C. yielded 108.3 g. This was 91.7% based on the amount of ketazine dropped. The selectivity of hydrazodicarbonamide based on urea was 98.4%, and no precipitation of ammonium carbonate was observed in a fractionating apparatus, a distillation line, or the like.

【0016】比較例1 副生するメチルエチルケトンならびにアンモニアは常圧
下で系外に抜き出した以外は、実施例1と同様に行っ
た。得られたヒドラゾジカルボンアミドの白色結晶は4
9gであった。これは、滴下したケタジンに対して4
1.6%であった。
Comparative Example 1 The procedure of Example 1 was repeated, except that methyl by-product ketone and ammonia were extracted out of the system under normal pressure. The obtained hydrazodicarbonamide white crystals are 4
9 g. This is 4 to the dropped ketazine.
1.6%.

【0017】比較例2 副生するメチルエチルケトンならびにアンモニアは常圧
下で系外に抜き出し、且つ反応温度を106〜108℃
にした以外は、実施例1と同様に行った。得られたヒド
ラゾジカルボンアミドの白色結晶は108.5gであっ
た。これは、滴下したケタジンに対して91.9%であ
った。また、尿素を基準としたヒドラゾジカルボンアミ
ド選択率は93.6%であり、分留装置、留出ラインな
どに炭酸アンモニウムの析出が多量にみられた。
COMPARATIVE EXAMPLE 2 By-product methyl ethyl ketone and ammonia were taken out of the system under normal pressure, and the reaction temperature was set at 106 to 108 ° C.
The procedure was performed in the same manner as in Example 1, except that The amount of white crystals of the obtained hydrazodicarbonamide was 108.5 g. This was 91.9% based on the dropped ketazine. The hydrazodicarbonamide selectivity based on urea was 93.6%, and a large amount of ammonium carbonate was precipitated in a fractionating apparatus, a distillation line, and the like.

【0018】[0018]

【発明の効果】本発明の方法により、ヒドラゾジカルボ
ンアミドを高い収率で得ることができた。また、尿素の
熱分解による不純物生成も抑制される。
According to the method of the present invention, hydrazodicarbonamide can be obtained in a high yield. Further, generation of impurities due to thermal decomposition of urea is also suppressed.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 増本 勇 三重県四日市市日永東2丁目4番16号 三 菱瓦斯化 学株式会社四日市工場内 Fターム(参考) 4H006 AA02 AB84 AC13 AC57 BA02 BA34 BA36 BB14 BB31 BC10 BC11 4H039 CA73 CD10 CD90  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Isamu Masumoto F-term (reference) 4Y006 AA02 AB84 AC13 AC57 BA02 BA34 BA36 in Yokkaichi Plant, 2-4-1-16 Hinagahigashi, Yokkaichi City, Mie Prefecture BB14 BB31 BC10 BC11 4H039 CA73 CD10 CD90

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 可溶性塩類存在下、一般式(1)で表さ
れる化合物と尿素とを減圧条件下で反応させることを特
徴とするヒドラゾジカルボンアミドの製造方法。 【化1】 {式中R1、R2はアルキル基を示す。これらは互いに結
合していてもよい。また、A−は、 【化2】 (式中R1、R3はアルキル基を示す。これらは互いに結
合していてもよい。)}
1. A method for producing hydrazodicarbonamide, comprising reacting a compound represented by the general formula (1) with urea under reduced pressure in the presence of a soluble salt. Embedded image 中 In the formula, R 1 and R 2 each represent an alkyl group. These may be bonded to each other. A- is represented by the following: (In the formula, R 1 and R 3 represent an alkyl group. These may be bonded to each other.)
【請求項2】 66500〜99750Paで反応させ
る請求項1記載のヒドラゾジカルボンアミドの製造方
法。
2. The method for producing hydrazodicarbonamide according to claim 1, wherein the reaction is carried out at 66500 to 99750 Pa.
【請求項3】 副生するケトン及びアンモニアを強制的
に取り出しつつ反応させる請求項1記載のヒドラゾジカ
ルボンアミドの製造方法。
3. The method for producing hydrazodicarbonamide according to claim 1, wherein the reaction is carried out while forcibly removing ketone and ammonia as by-products.
【請求項4】 60〜105℃で反応させる請求項1記
載のヒドラゾジカルボンアミドの製造方法。
4. The method for producing hydrazodicarbonamide according to claim 1, wherein the reaction is carried out at 60 to 105 ° C.
【請求項5】 一般式(1)で表される化合物を連続的
に反応系内に導入する請求項1記載のヒドラゾジカルボ
ンアミドの製造方法。
5. The method for producing a hydrazodicarbonamide according to claim 1, wherein the compound represented by the general formula (1) is continuously introduced into the reaction system.
JP2000262638A 2000-08-31 2000-08-31 Method for producing hydrazodicarbonamide Pending JP2002069049A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000262638A JP2002069049A (en) 2000-08-31 2000-08-31 Method for producing hydrazodicarbonamide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000262638A JP2002069049A (en) 2000-08-31 2000-08-31 Method for producing hydrazodicarbonamide

Publications (1)

Publication Number Publication Date
JP2002069049A true JP2002069049A (en) 2002-03-08

Family

ID=18750292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000262638A Pending JP2002069049A (en) 2000-08-31 2000-08-31 Method for producing hydrazodicarbonamide

Country Status (1)

Country Link
JP (1) JP2002069049A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100618947B1 (en) * 2002-06-17 2006-09-01 주식회사 제이앤드제이 캐미칼 Method for preparing hydrazodicarbonamide using biuret as starting material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100618947B1 (en) * 2002-06-17 2006-09-01 주식회사 제이앤드제이 캐미칼 Method for preparing hydrazodicarbonamide using biuret as starting material

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