JPS62267257A - Production of glycolonitrile - Google Patents

Production of glycolonitrile

Info

Publication number
JPS62267257A
JPS62267257A JP61110837A JP11083786A JPS62267257A JP S62267257 A JPS62267257 A JP S62267257A JP 61110837 A JP61110837 A JP 61110837A JP 11083786 A JP11083786 A JP 11083786A JP S62267257 A JPS62267257 A JP S62267257A
Authority
JP
Japan
Prior art keywords
reaction
sodium acetate
acid
formalin
solution
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.)
Granted
Application number
JP61110837A
Other languages
Japanese (ja)
Other versions
JPH0730004B2 (en
Inventor
Yasuhiro Sato
安宏 佐藤
Hideo Ogata
秀雄 緒方
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 JP61110837A priority Critical patent/JPH0730004B2/en
Publication of JPS62267257A publication Critical patent/JPS62267257A/en
Publication of JPH0730004B2 publication Critical patent/JPH0730004B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To obtain a compound useful as a synthetic intermediate for hydantoins in high purity and yield while suppressing formation of by-products and preventing coloring, by adding prussic acid to a formalin solution containing dissolved sodium acetate, carrying out at a specific pH value and removing the prussic acid. CONSTITUTION:Crystals or an aqueous solution of sodium acetate is added to formalin and dissolved therein to give a formalin solution and prussic acid kept at a temperature within the range of 15-30 deg.C is then added thereto. Since the pH of the reaction solution varies with the addition of the prussic acid, acetic acid or sodium acetate is added, as necessary, to keep the pH of the reaction solution at 4.8-6.0 and carry out the reaction. The pH of the reaction solution is then adjusted to <=2, preferably 1.5 with sulfuric acid to remove the residual prussic acid at <=50 deg.C under reduced pressure to afford the aimed substance.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、グリコロニトリルの改良された製造方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an improved method for producing glycolonitrile.

グリコロニトリルはヒダントイン類の製造中間体として
有用な化合物である。
Glycolonitrile is a compound useful as an intermediate in the production of hydantoins.

(従来の技術) ホルマリンに塩基性触媒の存在下、青酸を反応させてグ
リコロニトリルを製造する一般的な方法は既によく知ら
れている。
(Prior Art) A general method for producing glycolonitrile by reacting formalin with hydrocyanic acid in the presence of a basic catalyst is already well known.

しかしながら、これらの公知方法は、副生物の生成を抑
制し、目的生成物の着色を防止し、且つ高純度の製品を
高収率で製造するには未だ満足できるものではない。
However, these known methods are still unsatisfactory in suppressing the formation of by-products, preventing coloring of the target product, and producing high-purity products in high yields.

(発明が解決しようとする問題点) 本発明の課題は、このような従来技術の問題点を解決し
、副生物の生成を抑制しながら反応を進め、着色がなく
、高純度のグリコロニトリルを高収率で製造する方法を
提供することである。
(Problems to be Solved by the Invention) The object of the present invention is to solve the problems of the prior art, proceed with the reaction while suppressing the production of by-products, and produce highly pure glycolonitrile without coloring. It is an object of the present invention to provide a method for producing with high yield.

(問題点を解決するための手段) 本発明者等は、上記課題解決のために鋭意検討を行った
。その結果、上記課題解決のためには、ホルマリンと青
酸およびグリコロニトリルが、安定に保持され、かつ反
応が円滑に進行する条件の選定が極めて重要であること
を見出した。
(Means for Solving the Problems) The present inventors have conducted extensive studies to solve the above problems. As a result, in order to solve the above problem, it was found that it is extremely important to select conditions under which formalin, hydrocyanic acid, and glycolonitrile are stably maintained and the reaction proceeds smoothly.

すなわち、反応中の反応液のpi(、反応温度、反応後
の反応液のpi(、反応液の後処理条件、製品の保存条
件等を厳しく制御することにより上記課題を解決しうろ
ことを見出し、本発明を完成した。
In other words, it was discovered that the above problems could be solved by strictly controlling the pi of the reaction solution during the reaction, the reaction temperature, the pi of the reaction solution after the reaction, the post-treatment conditions of the reaction solution, the storage conditions of the product, etc. , completed the invention.

すなわち、本発明は、触媒量の酢酸ナトリウムを溶解し
たホルマリン液にほぼ等モルの青酸を液温15〜30℃
で、必要ならば、酢酸または酢酸ナトリウムを添加しな
がらpt+を4.8〜6.0に保って滴下し同条件下で
反応を行った後、硫酸で反応液のpnを2以下に調製し
、次いで50℃以下、減圧下に残留青酸を除去すること
を特徴とするグリコロニトリルの製造方法である。
That is, in the present invention, approximately equimolar hydrocyanic acid is added to a formalin solution in which a catalytic amount of sodium acetate is dissolved at a liquid temperature of 15 to 30°C.
Then, if necessary, add acetic acid or sodium acetate while keeping pt+ at 4.8 to 6.0, add dropwise and react under the same conditions, and then adjust the pn of the reaction solution to 2 or less with sulfuric acid. , followed by removing residual hydrocyanic acid at 50° C. or lower under reduced pressure.

本発明の方法において、触媒量の酢酸ナトリウムを熔解
したホルマリン液とは、ホルマリンに酢酸ナトリウムの
結晶、もしくは酢酸ナトリウムの水溶液を加え、ホルマ
リン中に酢酸ナトリウムを溶解させたものである。
In the method of the present invention, the formalin solution in which a catalytic amount of sodium acetate is dissolved is one in which sodium acetate crystals or an aqueous solution of sodium acetate are added to formalin to dissolve sodium acetate in formalin.

ここで、本発明に用いられるホルマリンは特に制限はな
く、通常市販のホルマリン、パラホルムアルデヒドを水
に溶解させたものなどが挙げられる。
Here, the formalin used in the present invention is not particularly limited, and examples thereof include commercially available formalin and paraformaldehyde dissolved in water.

このようなホルマリン液に溶解させる酢酸ナトリウムは
触媒量でよい。通常、0.005〜%の範囲、好ましく
は0.01〜1%の範囲である。
A catalytic amount of sodium acetate may be dissolved in such a formalin solution. Usually, it is in the range of 0.005-%, preferably in the range of 0.01-1%.

この酢酸ナトリウムを溶解したホルマリン液に添加する
青酸の量は、ホルマリンに対して1.0〜1.05モル
倍程度で良い。
The amount of hydrocyanic acid added to the formalin solution in which sodium acetate is dissolved may be about 1.0 to 1.05 times the mole of formalin.

青酸の添加温度は、15〜30℃の範囲に保つことが必
要である。15℃未満ではホルマリンとの反応速度が遅
くなり、反応系に蓄積した青酸が一時に反応してその制
御が困難になる恐れがある。また、30℃を越えると反
応液のpHが徐々に上昇し生成したグリコロニトリルが
分解し着色の原因となることがある。
It is necessary to maintain the addition temperature of hydrocyanic acid in the range of 15 to 30°C. If it is below 15°C, the reaction rate with formalin will be slow, and there is a risk that hydrocyanic acid accumulated in the reaction system will react all at once, making it difficult to control. Moreover, if the temperature exceeds 30° C., the pH of the reaction solution will gradually increase, and the generated glycolonitrile may decompose and cause coloring.

青酸の滴下中は、ホルマリン液のpl+を4.8〜6.
0に保って行う。青酸の滴下により反応が進行し反応液
のpi(が変動するので、必要に応じて、酢酸または酢
酸ナトリウムを添加し、反応液のpl+を4.8〜6.
0に保ちながら、青酸の滴下および反応を行うのが好ま
しい。反応液のpnが低くなり過ぎると反応速度が遅く
なり、また高すぎると、重合反応が起こり製品が着1色
してくる場合がある。
During the dropping of hydrocyanic acid, the pl+ of the formalin solution was set at 4.8 to 6.
Keep it at 0. As the reaction progresses with the dropwise addition of hydrocyanic acid, the pi of the reaction solution changes, so if necessary, acetic acid or sodium acetate is added to adjust the pl+ of the reaction solution to 4.8 to 6.
It is preferable to drop hydrocyanic acid and carry out the reaction while maintaining the temperature at 0. If the pn of the reaction solution is too low, the reaction rate will be slow, and if it is too high, a polymerization reaction may occur and the product may become colored one color.

反応時間は、上記反応条件の制御が十分に行われていれ
ば、その影響は小さい。反応の完了に合わせて適宜決定
すればよい。
The influence of the reaction time is small if the reaction conditions are sufficiently controlled. It may be determined as appropriate depending on the completion of the reaction.

反応終了後、反応液のpl+を酸を用いて2以下、好ま
しくは1.5程度に調整する。この調整は、通常、硫酸
で行うのが好ましい。
After the reaction is completed, the pl+ of the reaction solution is adjusted to 2 or less, preferably about 1.5 using an acid. This adjustment is usually preferably carried out with sulfuric acid.

調整した後、ついで減圧下、50℃以下の温度で反応液
中に残存する青酸を除去する。
After the adjustment, hydrocyanic acid remaining in the reaction solution is then removed under reduced pressure at a temperature of 50° C. or lower.

この際、反応液の温度が50℃を越えると、グリコロニ
トリルの分解が生じる恐れがある。
At this time, if the temperature of the reaction solution exceeds 50°C, there is a risk that glycolonitrile will be decomposed.

除去された青酸はホルマリン液に吸収させ、つぎのグリ
コロニトリルの製造に使用することができる。
The removed hydrocyanic acid can be absorbed into a formalin solution and used in the next production of glycolonitrile.

以上のようにして、グリコロニトリルを得る。Glycolonitrile is obtained as described above.

得られたグリコロニトリルは、p)11.5程度の水溶
液の形態で、20℃以下で安定に保存することができる
The obtained glycolonitrile can be stably stored at 20° C. or lower in the form of an aqueous solution with a p) of about 11.5.

(効果) 本発明の方法によれば、高純度のグリコロニトリルをほ
ぼ定量的に製造することが可能である。
(Effects) According to the method of the present invention, it is possible to produce highly pure glycolonitrile almost quantitatively.

(実施例) 以下、実施例により本発明の方法を具体的に説明する。(Example) Hereinafter, the method of the present invention will be specifically explained with reference to Examples.

実施例1 37重量%ホルマリン液1100gに酢酸ナトリウム0
.8gを水4mlに溶解して加えたのち、液温15℃、
p114..9〜5.7に保って、98重量%青酸37
4gを加え、同条件で12時間反応を行った。
Example 1 1100g of 37% by weight formalin solution with 0 sodium acetate
.. After dissolving 8g in 4ml of water and adding it, the liquid temperature was 15℃,
p114. .. 98% by weight hydrocyanic acid 37
4 g was added and the reaction was carried out under the same conditions for 12 hours.

反応後25重量%硫酸3.78でPH1,5に調整し、
次いで50℃、50mmHgで残留青酸を除去した。
After the reaction, the pH was adjusted to 1.5 with 25% sulfuric acid 3.78,
Then, residual hydrocyanic acid was removed at 50° C. and 50 mmHg.

青酸を除去した反応液は、無色透明でグリコロニトリル
 51.4重量%を含む水溶液1475gであり、ホル
ムアルデヒドに対するグリコロニトリルの収率は98%
であった。
The reaction solution from which hydrocyanic acid was removed was 1475 g of a colorless and transparent aqueous solution containing 51.4% by weight of glycolonitrile, and the yield of glycolonitrile based on formaldehyde was 98%.
Met.

なお、除去した青酸は次のグリコロニトリルの製造に問
題なく使用することができた。
Note that the removed hydrocyanic acid could be used in the subsequent production of glycolonitrile without any problem.

実施例2 87重量%パラホルムアルデヒド509gに水591g
、酢酸ナトリウム1.5gを加え、溶解後、液温25°
C1pH4,8〜5.8に保って、98重量%青酸37
4gを加え、同条件で5時間反応を行った。
Example 2 591 g of water in 509 g of 87% by weight paraformaldehyde
, add 1.5 g of sodium acetate, and after dissolving, reduce the liquid temperature to 25°.
C1 Maintain pH 4.8-5.8, add 98 wt% hydrocyanic acid 37
4 g was added and the reaction was carried out under the same conditions for 5 hours.

反応後25重量%硫酸4.0gでPH1,5に調整し、
次いで50℃、50mmHgで残留青酸を除去した。
After the reaction, the pH was adjusted to 1.5 with 4.0 g of 25% sulfuric acid,
Then, residual hydrocyanic acid was removed at 50° C. and 50 mmHg.

青酸を除去した反応液は、無色透明でグリコロニトリル
 51.6重量%を含む水溶液1470gであり、ホル
ムアルデヒドに対するグリコロニトリルの収率は98%
であった。
The reaction solution from which hydrocyanic acid was removed was 1470 g of a colorless and transparent aqueous solution containing 51.6% by weight of glycolonitrile, and the yield of glycolonitrile based on formaldehyde was 98%.
Met.

比較例1 37重量%ホルマリン1100gに酢酸ナトリウム0.
8gを水4mlに溶解して加えた後、液温40℃、pH
5,5に保って、98重量%青酸の滴下を開始した。
Comparative Example 1 1100 g of 37% by weight formalin and 0.0 g of sodium acetate.
After dissolving 8g in 4ml of water and adding it, the liquid temperature was 40℃ and the pH was
While maintaining the temperature at 5.5, dropwise addition of 98% by weight hydrocyanic acid was started.

滴下途中、急激な温度の上昇に伴い反応液は黒色となり
分解した。
During the dropwise addition, the reaction solution turned black and decomposed due to a sudden rise in temperature.

比較例2 37重量%ホルマリン1100gに2N水酸化ナトリウ
ム水溶液5IIllを加え、液温15℃にて、98重量
%青酸374gを加え、同条件で12時間反応を行った
Comparative Example 2 5IIll of 2N aqueous sodium hydroxide solution was added to 1100g of 37% by weight formalin, and 374g of 98% by weight hydrocyanic acid was added at a liquid temperature of 15°C, and the reaction was carried out under the same conditions for 12 hours.

この間、pHは9.4〜7.0であり、反応液は黄色に
着色していた。ホルムアルデヒドに対するグリコロニト
リルの収率は96%であった。
During this time, the pH was 9.4 to 7.0, and the reaction solution was colored yellow. The yield of glycolonitrile based on formaldehyde was 96%.

比較例3 実施例1と全く同様に青酸との反応を行い、25重量%
硫酸にてpnを1.5に調整した。
Comparative Example 3 A reaction with hydrocyanic acid was carried out in exactly the same manner as in Example 1, and 25% by weight
The pn was adjusted to 1.5 with sulfuric acid.

ついで、70℃、150mmHgで残留青酸の除去を開
始したところ、反応液は黒色となり分解した。
Then, when removal of residual hydrocyanic acid was started at 70° C. and 150 mmHg, the reaction solution turned black and decomposed.

特許出願人  三井東圧化学株式会社 手続主甫正書(自発) 昭和62年3月30日Patent applicant: Mitsui Toatsu Chemical Co., Ltd. Procedural master's letter (spontaneous) March 30, 1986

Claims (1)

【特許請求の範囲】[Claims] (1)触媒量の酢酸ナトリウムを溶解したホルマリン液
に青酸を液温15〜30℃で、必要ならば、酢酸または
酢酸ナトリウムを添加しながらpHを4.8〜6.0に
保って滴下し同条件下で反応を行った後、硫酸で反応液
のpHを2以下に調製し、次いで50℃以下、減圧下に
残留青酸を除去することを特徴とするグリコロニトリル
の製造方法
(1) Hydrocyanic acid is added dropwise to a formalin solution containing a catalytic amount of sodium acetate at a temperature of 15 to 30°C, and if necessary, adding acetic acid or sodium acetate while maintaining the pH at 4.8 to 6.0. A method for producing glycolonitrile, which comprises carrying out the reaction under the same conditions, adjusting the pH of the reaction solution to 2 or less with sulfuric acid, and then removing residual hydrocyanic acid at 50°C or less under reduced pressure.
JP61110837A 1986-05-16 1986-05-16 Method for producing glycolonitrile Expired - Lifetime JPH0730004B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61110837A JPH0730004B2 (en) 1986-05-16 1986-05-16 Method for producing glycolonitrile

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61110837A JPH0730004B2 (en) 1986-05-16 1986-05-16 Method for producing glycolonitrile

Publications (2)

Publication Number Publication Date
JPS62267257A true JPS62267257A (en) 1987-11-19
JPH0730004B2 JPH0730004B2 (en) 1995-04-05

Family

ID=14545920

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61110837A Expired - Lifetime JPH0730004B2 (en) 1986-05-16 1986-05-16 Method for producing glycolonitrile

Country Status (1)

Country Link
JP (1) JPH0730004B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006126626A1 (en) 2005-05-27 2006-11-30 Asahi Kasei Chemicals Corporation Method for producing glycolic acid
JP2008525467A (en) * 2004-12-22 2008-07-17 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Process for the synthesis of glycolonitrile
WO2011158758A1 (en) * 2010-06-17 2011-12-22 旭化成ケミカルズ株式会社 Process for producing cyanohydrin

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2305170A1 (en) * 1973-02-02 1974-08-08 Sueddeutsche Kalkstickstoff Stable conc glycolonitrile solns. prodn. - by two-stage reaction of hydrocyanic acid and formalin followed by cation-exchange treatment
JPS51100027A (en) * 1975-02-25 1976-09-03 Mitsubishi Chem Ind GURIKORONITORIRUNOSEIZOHO
JPS5368725A (en) * 1976-11-29 1978-06-19 Showa Denko Kk Preparation of glycollonitrile

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2305170A1 (en) * 1973-02-02 1974-08-08 Sueddeutsche Kalkstickstoff Stable conc glycolonitrile solns. prodn. - by two-stage reaction of hydrocyanic acid and formalin followed by cation-exchange treatment
JPS51100027A (en) * 1975-02-25 1976-09-03 Mitsubishi Chem Ind GURIKORONITORIRUNOSEIZOHO
JPS5368725A (en) * 1976-11-29 1978-06-19 Showa Denko Kk Preparation of glycollonitrile

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008525467A (en) * 2004-12-22 2008-07-17 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Process for the synthesis of glycolonitrile
WO2006126626A1 (en) 2005-05-27 2006-11-30 Asahi Kasei Chemicals Corporation Method for producing glycolic acid
EP2361900A2 (en) 2005-05-27 2011-08-31 Asahi Kasei Chemicals Corporation Method for producing glycolic acid
US8106238B2 (en) 2005-05-27 2012-01-31 Asahi Kasei Chemicals Corporation Method for producing glycolic acid
US8956837B2 (en) 2005-05-27 2015-02-17 Asahi Kasei Chemicals Corporation Method for producing glycolic acid
WO2011158758A1 (en) * 2010-06-17 2011-12-22 旭化成ケミカルズ株式会社 Process for producing cyanohydrin

Also Published As

Publication number Publication date
JPH0730004B2 (en) 1995-04-05

Similar Documents

Publication Publication Date Title
JP4499706B2 (en) Method for producing methionine and its salt
EP0208948B1 (en) A method for optical resolution of phenylacetic acid derivative
JP4426104B2 (en) Process for producing hydroxymethylthiobutyric acid
JPH0313238B2 (en)
JPS62267257A (en) Production of glycolonitrile
JP4792754B2 (en) Method for removing ammonia from a solution containing an ammonium salt
JPS5839155B2 (en) Production method of thiourea dioxide
JP3011493B2 (en) Method for producing 4-alkyl-3-thiosemicarbazide
CN109369447A (en) Improved method of preparation technology of 3- (2, 2, 2-trimethylhydrazinium) propionate dihydrate
JPH0244472B2 (en)
JPH029874A (en) Production of alpha-aminoacetonitrile hydrochlorides
US20100094040A1 (en) Process for preparing alkali metal or alkaline earth metal tricyanomethanides
JPH0510332B2 (en)
KR100877134B1 (en) Process for preparation of Acamprosate Calcium
JP2003506428A (en) Betaine manufacturing method
JP3927835B2 (en) Process for producing iodinated aromatic compound diacetate
JPH0219365A (en) Production of inorganic acid salt of disulfide type siamine derivative
JP3908794B2 (en) Process for producing N-substituted unsaturated amides
JPH06135923A (en) Production of glycolonitrile
JP4212821B2 (en) Method for producing high-purity 4,4&#39;-dihydroxydiphenylsulfone monoether or a derivative thereof
KR800001550B1 (en) Preparing process for 5-(4-hyroxy phenyl)hydantoins
JPH1180072A (en) Production of highly pure lower saturated aliphatic carboxylic acid hydroxylamine
JPS584707B2 (en) Method for producing optically active phenylglycines
JPH04221354A (en) Production of tert. butyl hydrazine
JPH04173765A (en) Production of 1,3-phenylenedioxydiacetic acid