JPS6120539B2 - - Google Patents

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Publication number
JPS6120539B2
JPS6120539B2 JP52033260A JP3326077A JPS6120539B2 JP S6120539 B2 JPS6120539 B2 JP S6120539B2 JP 52033260 A JP52033260 A JP 52033260A JP 3326077 A JP3326077 A JP 3326077A JP S6120539 B2 JPS6120539 B2 JP S6120539B2
Authority
JP
Japan
Prior art keywords
reaction
glycine
solution
glycolonitrile
alkali
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
Application number
JP52033260A
Other languages
Japanese (ja)
Other versions
JPS53119820A (en
Inventor
Osamu Furuya
Kazuo Nakayasu
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP3326077A priority Critical patent/JPS53119820A/en
Publication of JPS53119820A publication Critical patent/JPS53119820A/en
Publication of JPS6120539B2 publication Critical patent/JPS6120539B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はイミノジ酢酸アルカリ塩の製造法に関
し、詳しくは遊離の苛性アルカリを実質的に含ま
ないグリシンアルカリ金属塩とグリコロニトリル
を60℃以下の温度にて、モル比1:0.8〜1.2の範
囲で反応させた後、苛性アルカリを加えて加水分
解せしめることによりイミノジ酢酸アルカリ金属
塩、更にはイミノジ酢酸を工業上有利に製造し得
る方法を提供せんとするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an alkali salt of iminodiacetic acid, and more specifically, a method for producing an alkali salt of iminodiacetic acid, in which a glycine alkali metal salt substantially free of free caustic alkali and glycolonitrile are mixed at a temperature of 60° C. or less, and the molar ratio The object of the present invention is to provide an industrially advantageous method for producing an alkali metal salt of iminodiacetic acid and furthermore, iminodiacetic acid, by reacting at a ratio of 1:0.8 to 1.2 and then hydrolyzing it by adding a caustic alkali. .

イミノジ酢酸はニトリロトリ酢酸などと同様
に、キレート作用を持つ化合物として種々の用途
を有する物質であるが、その工業的製造法につい
ては必ずしも充分満足すべき方法は見当らないの
が実情である。即ち、イミノシ酢酸の製造法とし
て従来よりいくつかの方法が知られているが、そ
の多くはニトリロトリ酢酸製造の際の副生物を分
離する方法の域を出ず、或いは仮えイミノジ酢酸
を主生成物とするものであつても可成り多量のニ
トリロトリ酢酸等が副生することは避けられず、
これらの分離の困難さと相俟つて、イミノジ酢酸
を高純度、高収量で得ることはできない。尚、イ
ミノジアセトニトリルをアルカリ加水分解すれば
不要な副生物を生成することなくイミノジ酢酸を
高収量で得ることができるが、しかし、イミノジ
アセトニトリルの製造自体は必ずしも容易ではな
くイミノジ酢酸の工業的製造法としては最良の方
法とは言い難い。
Iminodiacetic acid, like nitrilotriacetic acid and the like, is a substance that has various uses as a compound with a chelating effect, but the reality is that there is no fully satisfactory industrial method for producing it. In other words, several methods have been known for producing iminodiacetic acid, but most of them are limited to methods that separate by-products during the production of nitrilotriacetic acid, or methods that primarily produce iminodiacetic acid. Even if it is used as a product, it is inevitable that a considerable amount of nitrilotriacetic acid will be produced as a by-product.
Coupled with these difficulties in separation, iminodiacetic acid cannot be obtained with high purity and high yield. By alkaline hydrolysis of iminodiacetonitrile, iminodiacetic acid can be obtained in high yield without producing unnecessary by-products. However, the production of iminodiacetonitrile itself is not necessarily easy, and the industrial production of iminodiacetic acid is difficult. It is hard to say that this is the best manufacturing method.

本発明者等はイミノジ酢酸アルカリ塩を効率良
く製造する方法について種々検討した結果、実質
的に遊離の苛性アルカリを含まない水溶液中で、
グリシンアルカリ塩に対し、ほぼ等モルのグリコ
ロニトリルを加えて比較的低温で充分反応させた
後、添加したグリコロニトリルと等モル若しくは
僅かに過剰量の苛性アルカリを加えて加熱して加
水分解を行わせることにより、ニトリロトリ酢酸
塩等の副生を抑制し実質的にイミノジ酢酸塩のみ
を極めて高収率で合成し得ることを見出した。
As a result of various studies on methods for efficiently producing alkali iminodiacetic acid, the present inventors found that, in an aqueous solution containing substantially no free caustic alkali,
After adding approximately equimolar amount of glycolonitrile to glycine alkali salt and reacting sufficiently at a relatively low temperature, add caustic alkali in an amount equal to or slightly in excess of the added glycolonitrile and hydrolyze by heating. It has been found that by carrying out this process, by-products such as nitrilotriacetate can be suppressed and substantially only iminodiacetate can be synthesized in extremely high yield.

本発明の方法について更に詳細に説明すれば、
本発明に用いるグリシンアルカリ塩、例えば、グ
リシン酸ソーダはグリシン酸と苛性ソーダを等モ
ル混合して得られ、水溶液として反応に供される
が、ホルムアルデヒドと青酸又はグリコロニトリ
ルをアンモニアと反応させてグリシノニトリルと
し、これを苛性ソーダにて加水分解して得られる
グリシンソーダ水溶液等を用いても良い。但し、
この場合、過剰の遊離苛性ソーダの存在はグリコ
ロニトリルを加えた際これと望ましくない反応を
生じニトリロトリ酢酸ソーダ等の副生物を招く
他、反応液を不安定にし、着色や異常な発熱など
の原因となるため、事前にグリシンを加えてグリ
シンソーダに転換せしめるか或いは鉱酸を加えて
中和しておかなければならない。グリシンアルカ
リ塩の水溶液中の濃度は必ずしも制限はないが、
通常20〜50重量%程度であることが好ましい。こ
のグリシンアルカリ塩と反応させるグリコロニト
リルは通常水溶液として市販されているものが用
いられるが、青酸とホルムアルデヒドとの反応に
よつても容易に得ることができ、上記と同様に通
常20〜55重量%程度の濃度で用いられる。グリシ
ンソーダに対するグリコロニトリルの使用割合
は、多過ぎる場合には、未反応の残存グリコロニ
トリルが加水分解時にニトリロトリ酢酸塩又はグ
リコール酸塩となり無駄になるばかりでなく、こ
れらの副生は反応液からのイミノジ酢酸塩の分
離、回収に悪影響を及ぼし、また、少な過ぎる場
合は、反応上は特別の影響はないが反応原料とし
て比較的高価なグリシンが未反応で残存すること
となるため不経済である。従つて、本発明の方法
に於いては、グリシンアルカリ塩1モル当りグリ
コロニトリルは0.8〜1.2モル、好ましくはほぼ当
モルの割合で用いられる。
To explain the method of the present invention in more detail,
Glycine alkaline salt used in the present invention, for example, sodium glycinate, is obtained by mixing equimolar amounts of glycic acid and caustic soda and is subjected to the reaction as an aqueous solution. An aqueous glycine soda solution obtained by hydrolyzing sinonitrile with caustic soda may also be used. however,
In this case, the presence of excess free caustic soda causes an undesirable reaction with glycolonitrile when it is added, resulting in by-products such as sodium nitrilotriacetate, as well as destabilizing the reaction solution and causing discoloration and abnormal heat generation. Therefore, it is necessary to add glycine in advance to convert it to glycine soda, or to neutralize it by adding mineral acid. The concentration of glycine alkaline salt in an aqueous solution is not necessarily limited, but
Usually, it is preferably about 20 to 50% by weight. Glycolonitrile to be reacted with this alkali glycine salt is usually commercially available as an aqueous solution, but it can also be easily obtained by reaction with hydrocyanic acid and formaldehyde, and as above, it is usually 20 to 55% by weight. It is used at a concentration of about %. If the ratio of glycolonitrile to glycine soda is too large, unreacted residual glycolonitrile will not only become nitrilotriacetate or glycolate during hydrolysis and be wasted, but also these by-products will be lost to the reaction solution. If the amount is too small, it will have no particular effect on the reaction, but it will be uneconomical because glycine, which is relatively expensive as a reaction raw material, will remain unreacted. It is. Therefore, in the method of the present invention, glycolonitrile is used in a ratio of 0.8 to 1.2 mol, preferably approximately equimolar, per mol of glycine alkali salt.

グリシンアルカリ塩溶液とグリコロニトリル溶
液を上記の如き割合で混合すると反応は速みやか
に進行し、同時に可成りの発熱があり液温は上昇
する。このとき、余り高温になると反応液は着色
し、異常反応を生じて更に反応熱により液温は上
昇する事態を招き、非常に危険であるとともにニ
トリロトリ酢酸塩の副生が著しく目的物を収率良
く取得することもできない。反応温度は60℃以
下、望ましくは40℃以下に保つべきであり、その
ためには充分な冷却能力を持つ反応容器内で反能
を行う必要がある。
When the alkali glycine salt solution and the glycolonitrile solution are mixed in the above proportions, the reaction proceeds rapidly, and at the same time, considerable heat is generated and the temperature of the solution rises. At this time, if the temperature is too high, the reaction solution will be colored, an abnormal reaction will occur, and the temperature of the solution will further increase due to the reaction heat, which is extremely dangerous and the by-product of nitrilotriacetate will significantly reduce the yield of the target product. I can't even get it right. The reaction temperature should be kept below 60°C, preferably below 40°C, and for this purpose it is necessary to carry out the reaction in a reaction vessel with sufficient cooling capacity.

反応の進行は、例えば、反応液中の残存シアン
濃度を分析する等の方法により容易に知ることが
できるが、40℃ではほぼ1〜1.5時間、20℃では
ほぼ2〜3時間で反応は概ね完結し、反応出発原
料としてグリコロニトリルを所定量用いた場合に
は反応液中のシアン濃度は実質的に殆んど無視で
きるまでに低下する。
The progress of the reaction can be easily determined by, for example, analyzing the residual cyanide concentration in the reaction solution, but the reaction generally takes approximately 1 to 1.5 hours at 40°C and approximately 2 to 3 hours at 20°C. When the reaction is completed and a predetermined amount of glycolonitrile is used as a starting material for the reaction, the cyanide concentration in the reaction solution is reduced to a point where it can be virtually ignored.

こうして得た反応液を次に、原料グリコロニト
リルとほぼ等モル若しくは僅かに過剰の苛性アル
カリと混合し、加水分解せしめる。苛性アルカリ
は通常20〜50重量%の水溶液として用いられる
が、添加と共に急激な発熱があるが、徐々に混合
するか或いは充分な撹拌を行う等により支障なく
加水分解を進行せしめることができる。このとき
の温度は特に制限はないが、通常は60℃〜沸点ま
での範囲で滴宜行われる。実用上は加水分解反応
により生成するアンモニアの除去のため、少くと
も反応終了前一担反応液を沸煮せしめることが望
ましい。加水分解反応は反応液の沸点で行つた場
合には1〜2時間で終了する。
The reaction solution thus obtained is then mixed with caustic alkali in an amount approximately equal to or slightly in excess of the raw material glycolonitrile, and hydrolyzed. Caustic alkali is usually used as an aqueous solution of 20 to 50% by weight, and although it generates a rapid heat generation upon addition, hydrolysis can proceed without problems by gradual mixing or sufficient stirring. The temperature at this time is not particularly limited, but the dropwise addition is usually carried out in a range from 60°C to the boiling point. Practically speaking, it is desirable to boil the reaction solution at least before the end of the reaction in order to remove ammonia produced by the hydrolysis reaction. The hydrolysis reaction is completed in 1 to 2 hours when carried out at the boiling point of the reaction solution.

かくて、得られる反応終了後の液には最も好適
な条件下で反応を行つた場合には、原料のグリシ
ンアルカリ塩に対し95〜98%の高収率をもつてイ
ミノジ酢酸アルカリ塩が含まれ、ニトリロトリ酢
酸塩の副生は2〜5%程度であるが、これよりイ
ミノジ酢酸を単離するには通常の中和、分別晶析
等の手段により容易に行われる。
Thus, when the reaction is carried out under the most suitable conditions, the obtained solution after the reaction is completed contains iminodiacetic acid alkali salt with a high yield of 95 to 98% based on the raw material glycine alkali salt. The by-product of nitrilotriacetate is about 2 to 5%, but iminodiacetic acid can be easily isolated from this by conventional means such as neutralization and fractional crystallization.

尚、本発明の方法に於いては実質的に遊離の苛
性アルカリを含まないグリシンアルカリ塩とグリ
コロニトリルを所定のモル比で低温にて充分反応
させた後、引続き苛性アルカリと混合して加水分
解反応させることが必須の要件とされるが、因み
にグリシンと苛性ソーダの等モル混合物又はグリ
シンソーダの水溶液に、グリコロニトリルと苛性
ソーダを夫々等モル宛同時に加えて加熱反応させ
た場合には、イミノジ酢酸ソーダの他多量のニト
リロトリ酢酸ソーダが生成してこれらの混合物し
か得られない。このとき、グリシンソーダに対す
るグリコロニトリル及び苛性ソーダのモル比を増
すに従つてニトリロトリ酢酸ソーダの生成率が増
大するが、逆に1モル以下に減らしてももイミノ
ジ酢酸ソーダのみを選択的に得ることはできず、
むしろ未反応のグリシンソーダが残存する不利を
免れない。また、ニトリロトリ酢酸の製造方法と
してグリシンソーダ1モルに過剰の苛性ソーダ
(2モル)を加えておいて加熱し、これにグリコ
ロニトリルを2モル加えて加水分解する方法が知
られているが、それと同様な考え方でグリシンソ
ーダ1モルに苛性ソーダ1モルを先に加えて加熱
し、これにグリコロニトリル1モルを加える方法
を行つた場合にも前記と同様にイミノジ酢酸ソー
ダのみを選択的に合成することはできない。更に
また、予めグリコロニトリルと苛性ソーダを等モ
ル量で混合した場合には反応は時に爆発的に進行
して主生成物としてニトリロトリ酢酸ソーダが得
られる。この際、グリコール酸ソーダが可成り副
生することが知られているが、イミノジ酢酸ソー
ダの生成は極く僅かである。
In the method of the present invention, glycine alkaline salt containing substantially no free caustic alkali and glycolonitrile are sufficiently reacted at a predetermined molar ratio at low temperature, and then mixed with caustic alkali and hydrated. It is said that a decomposition reaction is an essential requirement, but if glycolonitrile and caustic soda are added in equal molar amounts to an equimolar mixture of glycine and caustic soda or an aqueous solution of glycine soda at the same time and subjected to a heating reaction, iminodic In addition to sodium acetate, a large amount of sodium nitrilotriacetate is produced, and only a mixture of these is obtained. At this time, as the molar ratio of glycolonitrile and caustic soda to glycine soda increases, the production rate of sodium nitrilotriacetate increases, but even if the ratio is reduced to 1 mole or less, only sodium iminodiacetate can be selectively obtained. cannot,
Rather, the disadvantage is that unreacted glycine soda remains. Also, a known method for producing nitrilotriacetic acid is to add excess caustic soda (2 moles) to 1 mole of glycine soda, heat it, and then add 2 moles of glycolonitrile to hydrolyze it. Using the same concept, if you first add 1 mol of caustic soda to 1 mol of glycine soda and heat it, then add 1 mol of glycolonitrile to this, only sodium iminodiacetate will be selectively synthesized in the same way as above. It is not possible. Furthermore, when equimolar amounts of glycolonitrile and caustic soda are mixed in advance, the reaction sometimes proceeds explosively to obtain sodium nitrilotriacetate as the main product. At this time, it is known that a considerable amount of sodium glycolate is produced as a by-product, but the production of sodium iminodiacetate is extremely small.

以下、本発明の方法について代表的な例を示し
更に具体的に説明するが、これらの例は本発明に
ついての理解を容易にするため、あえて反応条件
を絞つて例示するものであつて、本発明はこれら
によつて何ら限定的に解釈され得ないことは言う
までもない。
Hereinafter, representative examples of the method of the present invention will be shown and explained in more detail. However, these examples are intended to limit the reaction conditions to facilitate understanding of the present invention. It goes without saying that the invention cannot be construed as being limited in any way by these.

実施例 1 500mlの4ツ口フラスコに撹拌機、温度計、滴
下ロートおよび還流凝縮器をとりつけ、油浴中に
設置する。
Example 1 A 500 ml four-neck flask is equipped with a stirrer, a thermometer, a dropping funnel, and a reflux condenser, and placed in an oil bath.

グリシン37.5g(0.5モル)、苛性ソーダ50%溶
液40.0g(0.5モル)および水43.8gの混合液を入
れ、撹拌する。常温下でこれに、滴下ロートより
40%グリコロニトリル溶液71.3g(0.5モル)を
滴下する。発熱するのでよく撹拌し40℃以下で10
分間かけて滴下した。滴下終了後、液温40℃に保
ちつつ、1時間反応させた。1時間後の液中シア
ン濃度は硝酸銀滴定で0.01mmol/g以下であつ
た。
Add a mixture of 37.5 g (0.5 mol) of glycine, 40.0 g (0.5 mol) of 50% caustic soda solution, and 43.8 g of water and stir. Add to this at room temperature through a dropping funnel.
71.3 g (0.5 mol) of 40% glycolonitrile solution is added dropwise. Stir well and heat at 40°C or less as it generates heat.
It was added dropwise over a period of minutes. After the dropwise addition was completed, the reaction was continued for 1 hour while maintaining the liquid temperature at 40°C. The concentration of cyanide in the solution after 1 hour was determined by silver nitrate titration to be less than 0.01 mmol/g.

次いで、苛性ソーダ溶液40.0g(0.5モル)を
一度に加えると、発熱し液温が約80℃になり、ア
ンモニアが発生しはじめた。かまわずに加熱昇温
し沸点で2時間リフラツクスさせながら加熱し
た。反応終了後の液は210.1gあり、イミノジ酢
酸ソーダ482mmol、ニトリロトリ酢酸ソーダ8mm
olを含んでいた。反応収率はグリシンソーダに対
し96.4%である。反応液を50%硫酸によりPH2.4
まで中和した後、加熱濃縮し、芒硝の沈澱が晶出
しはじめたので、濃縮をやめ、少量の温水を加え
て芒硝の沈澱を再溶解した後、撹拌しつつ放冷し
た。イミノジ酢酸が晶出してきたので、33℃にて
過を行い、イミノジ酢酸を別した。水洗乾燥
後の重量は50.5gであり、イミノジ酢酸の純度は
98.2%でありニトリロ三酢酸1.5%を含んでい
た。液および水洗液を再加熱し、濃縮した。芒
硝の結晶が晶出してきたが、さらに濃縮し、イミ
ノジ酢酸が晶出しない範囲でできるだけ芒硝を晶
出させた後、熱時過を行い、芒硝を別した。
水洗乾燥後の重量は53.2gであり、芒硝の純度は
99.1%であつた。水洗液と液を合わせ、冷却し
た。イミノジ酢酸が晶出してきたので30℃で別
した。水洗乾燥後の重量は11.8gであり、イミノ
ジ酢酸の純度は97.4%であつた。2回の操作で得
られたイミノジ酢酸を合わせ、熱水にとかし、
0.5gの粉末活性炭を加えて処理した後、再結晶
した。イミノジ酢酸56.4g(純度99.0%)が得ら
れた。原料グリシンソーダからの収率は84.0%で
あつた。
Next, when 40.0 g (0.5 mol) of caustic soda solution was added at once, heat was generated, the liquid temperature reached approximately 80°C, and ammonia began to be generated. The temperature was raised without worrying, and the mixture was heated at the boiling point for 2 hours while being refluxed. There is 210.1g of liquid after the reaction, 482mmol of sodium iminodiacetate, 8mm of sodium nitrilotriacetate.
It contained ol. The reaction yield is 96.4% based on glycine soda. The reaction solution was adjusted to pH2.4 with 50% sulfuric acid.
After the mixture was neutralized to a maximum temperature, it was concentrated by heating, and as precipitates of Glauber's salt began to crystallize, concentration was stopped and a small amount of warm water was added to redissolve the precipitates of Glauber's salt, followed by cooling while stirring. Since iminodiacetic acid crystallized, it was filtered at 33°C to separate iminodiacetic acid. The weight after washing with water and drying is 50.5g, and the purity of iminodiacetic acid is
It was 98.2% and contained 1.5% nitrilotriacetic acid. The liquid and washings were reheated and concentrated. Although Glauber's salt crystals were crystallized, the mixture was further concentrated to crystallize as much Glauber's salt as possible without crystallizing iminodiacetic acid, and then subjected to heat aging to separate the Glauber's salt.
The weight after washing with water and drying is 53.2g, and the purity of Glauber's salt is
It was 99.1%. The water washing solution and the liquid were combined and cooled. Since iminodiacetic acid crystallized, it was separated at 30°C. The weight after washing with water and drying was 11.8 g, and the purity of iminodiacetic acid was 97.4%. The iminodiacetic acid obtained in the two operations was combined and dissolved in hot water.
After treatment by adding 0.5 g of powdered activated carbon, it was recrystallized. 56.4 g of iminodiacetic acid (purity 99.0%) was obtained. The yield from the raw material glycine soda was 84.0%.

実施例 2 グリシン酸ソーダとグリコロニトリルとの反応
を20℃で行つた他は全て実施例1と同様に反応さ
せたところ、1時間反応ぴ後の液中シアン濃度は
0.12mmol/gであり、更に加水分解反応終了後の
液はイミノジ酢酸ソーダ467mmol、ニトリロトリ
酢酸ソーダ21mmolを含んでいた。
Example 2 The reaction between sodium glycinate and glycolonitrile was carried out in the same manner as in Example 1, except that the reaction was carried out at 20°C. After 1 hour of reaction, the concentration of cyanide in the solution was as follows.
0.12 mmol/g, and the liquid after the completion of the hydrolysis reaction contained 467 mmol of sodium iminodiacetate and 21 mmol of sodium nitrilotriacetate.

比較例 1 グリシンソーダとグリコロニトリルとの反応を
65℃、30分間行つた他は全て実施例1と同様に反
応させたところ、加水分解反応終了後の液にはイ
ミノジ酢酸ソーダは277mmolしかなく、ニトリロ
トリ酢酸ソーダが147mmol含まれていた。また、
このときの反応液は赤褐色に着色していた。
Comparative example 1 The reaction between glycine soda and glycolonitrile
The reaction was carried out in the same manner as in Example 1 except that the reaction was carried out at 65° C. for 30 minutes, and the solution after the hydrolysis reaction contained only 277 mmol of sodium iminodiacetate and 147 mmol of sodium nitrilotriacetate. Also,
The reaction solution at this time was colored reddish brown.

比較例 2 40%グリコロニトリル溶液を92.7g(0.65モ
ル)用い、更に加水分解時に苛性ソーダ50%溶液
52.0g(0.65モル)に用いた他は全て実施例1と
同様に反応させたところ、加水分解反応終了後の
液にはイミノジ酢酸ソーダ460mmol、ニトリロト
リ酢酸ソーダ68mmol、グリコール酸ソーダ14mmol
が含まれていた。
Comparative Example 2 92.7g (0.65 mol) of 40% glycolonitrile solution was used, and 50% caustic soda solution was added during hydrolysis.
The reaction was carried out in the same manner as in Example 1 except that 52.0 g (0.65 mol) was used, and the solution after the hydrolysis reaction contained 460 mmol of sodium iminodiacetate, 68 mmol of sodium nitrilotriacetate, and 14 mmol of sodium glycolate.
was included.

比較例 3 グリシンソーダとグリコロニトリルとの反応の
際、反応液中に最初から0.05モルの遊離苛性ソー
ダを共存せしめて反応させた他は全て実施例1と
同様にして行つたところ、加水分解反応終了後の
液にはイミノジ酢酸ソーダは391mmolしかなく、
ニトリロトリ酢酸ソーダは73mmol含まれていた。
Comparative Example 3 The reaction between glycine soda and glycolonitrile was carried out in the same manner as in Example 1, except that 0.05 mol of free caustic soda was allowed to coexist in the reaction solution from the beginning, resulting in a hydrolysis reaction. After completion, the solution contained only 391 mmol of sodium iminodiacetate.
Sodium nitrilotriacetate contained 73 mmol.

Claims (1)

【特許請求の範囲】[Claims] 1 遊離の苛性アルカリを実質的に含まないグリ
シンアルカリ金属塩とグリコロニトリルを60℃以
下の温度で、モル比1;0.8〜1.2の範囲で反応さ
せた後、苛性アルカリを加えて加水分解せしめる
ことを特徴とするイミノジ酢酸アルカリ塩の製造
法。
1. After reacting a glycine alkali metal salt substantially free of free caustic alkali and glycolonitrile at a temperature of 60°C or lower at a molar ratio of 1 in the range of 0.8 to 1.2, a caustic alkali is added to cause hydrolysis. A method for producing an alkali salt of iminodiacetic acid, characterized by the following.
JP3326077A 1977-03-28 1977-03-28 Preparation of alkali aminodiacetate Granted JPS53119820A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3326077A JPS53119820A (en) 1977-03-28 1977-03-28 Preparation of alkali aminodiacetate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3326077A JPS53119820A (en) 1977-03-28 1977-03-28 Preparation of alkali aminodiacetate

Publications (2)

Publication Number Publication Date
JPS53119820A JPS53119820A (en) 1978-10-19
JPS6120539B2 true JPS6120539B2 (en) 1986-05-22

Family

ID=12381537

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3326077A Granted JPS53119820A (en) 1977-03-28 1977-03-28 Preparation of alkali aminodiacetate

Country Status (1)

Country Link
JP (1) JPS53119820A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0238900A (en) * 1988-07-28 1990-02-08 Power Reactor & Nuclear Fuel Dev Corp Removal and remover of stuck dust in off-gas piping in glass melting furnace

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55122747A (en) * 1979-03-14 1980-09-20 Showa Denko Kk Production of iminodiacetic acid derivative
JPS5780346A (en) * 1980-11-07 1982-05-19 Mitsubishi Chem Ind Ltd Production of alkali iminodiacetate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0238900A (en) * 1988-07-28 1990-02-08 Power Reactor & Nuclear Fuel Dev Corp Removal and remover of stuck dust in off-gas piping in glass melting furnace

Also Published As

Publication number Publication date
JPS53119820A (en) 1978-10-19

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