JPS5842855B2 - Isolation method for pyruvate - Google Patents
Isolation method for pyruvateInfo
- Publication number
- JPS5842855B2 JPS5842855B2 JP399279A JP399279A JPS5842855B2 JP S5842855 B2 JPS5842855 B2 JP S5842855B2 JP 399279 A JP399279 A JP 399279A JP 399279 A JP399279 A JP 399279A JP S5842855 B2 JPS5842855 B2 JP S5842855B2
- Authority
- JP
- Japan
- Prior art keywords
- pyruvate
- aqueous solution
- lactate
- present
- precipitate
- 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
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は、ピルビン酸塩を含有する水溶液からピルビン
酸塩を固体の形で単離する方法、より詳細には、乳酸塩
の接触酸化によって製造したピルビン酸塩水溶液から、
ピルビン酸塩を単離する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention describes a method for isolating pyruvate in solid form from an aqueous solution containing pyruvate, more particularly from an aqueous pyruvate solution prepared by catalytic oxidation of lactate. ,
The present invention relates to a method for isolating pyruvate.
ピルビン酸塩は、熱安定性が悪く、ピルビン酸塩を含有
する水溶液を単に蒸発乾固するのみでは、熱分解等によ
り脱炭酸を起こし酢酸塩が副生したり、重合物が生成し
たりするため、高純度のピルビン酸塩を得ることは困難
である。Pyruvate has poor thermal stability, and simply evaporating an aqueous solution containing pyruvate to dryness will result in decarboxylation due to thermal decomposition, etc., resulting in acetate by-products or polymers. Therefore, it is difficult to obtain highly pure pyruvate.
高純度品を得るには、従来は、減圧下に低温で水を除去
するが、または凍結乾燥等の方法が用いられていたため
に、単離に要する費用も大きく、工業的に安価にピルビ
ン酸塩の固体を得るのは困難であった。Conventionally, to obtain a high-purity product, water was removed at low temperature under reduced pressure, or methods such as freeze-drying were used, which resulted in high costs for isolation. It was difficult to obtain salt solids.
本発明の目的とするところは、ピルビン酸塩を含有する
水溶液、特に乳酸塩の接触酸化によって得たピルビン酸
塩含有水溶液から、固体状のピルビン酸塩を取得する方
法を提供することにある。An object of the present invention is to provide a method for obtaining solid pyruvate from an aqueous pyruvate-containing solution, in particular a pyruvate-containing aqueous solution obtained by catalytic oxidation of lactate.
本発明者は、ピルビン酸塩を含有する水溶液から固体状
のピルビン酸塩を単離する方法を種々研究した結果、ピ
ルビン酸塩含有水溶液とイソプロピルアルコール(以下
、イソプロパツールと略記する)とを混合すると、ピル
ビン酸塩の固体が析出することを見い出し本発明を完成
するに至った。As a result of various studies on methods for isolating solid pyruvate from an aqueous solution containing pyruvate, the present inventor discovered that a method for isolating solid pyruvate from an aqueous solution containing pyruvate and isopropyl alcohol (hereinafter abbreviated as isopropanol) It was discovered that solid pyruvate precipitates when mixed, leading to the completion of the present invention.
すなわち、本発明の要旨とするところは、イソフロパノ
ールとピルビン酸塩含有水溶液とを混合し、ピルビン酸
塩固体を析出せしめ、これを沢過分離するところにある
。That is, the gist of the present invention is to mix isofuropanol and a pyruvate-containing aqueous solution, precipitate pyruvate solids, and then filter and separate the solids.
本発明の方法によれば、容易にピルビン酸塩を含有する
水溶液から固体状のピルビン酸塩を工業的に有利に取得
することができる。According to the method of the present invention, solid pyruvate can be easily and industrially advantageously obtained from an aqueous solution containing pyruvate.
本発明の方法を適用するピルビン酸塩を含有する水溶液
は、通常、下記のような方法により製造される。The aqueous solution containing pyruvate to which the method of the present invention is applied is usually produced by the following method.
乳酸塩を含有する水溶液に触媒の存在下、空気を吹込み
、乳酸塩を酸化脱水素してピルビン酸塩とする。Air is blown into an aqueous solution containing lactate in the presence of a catalyst to oxidize and dehydrogenate the lactate to form pyruvate.
この方法で製造したピルビン酸塩の水溶液から触媒を分
離した後、イソプロパツールを添加しピルビン酸塩を沈
澱として析出せしめる。After separating the catalyst from the aqueous solution of pyruvate produced by this method, isopropanol is added to precipitate the pyruvate.
ピルビン酸塩含有水溶液と混合してピルビン酸塩沈澱と
して析出せしめる溶剤はインプロパツールであり、イン
プロパツール以外の低級アルコール、たとえば、メタノ
ール、エタノールまたはブタノールなどを用いてピルビ
ン酸塩含有水溶液から、ピルビン酸塩を沈澱として析出
させることは、収率が極めて低く、実用的でない。The solvent that is mixed with the pyruvate-containing aqueous solution to precipitate pyruvate is Impropatool, which is mixed with the pyruvate-containing aqueous solution using a lower alcohol other than Impropatool, such as methanol, ethanol, or butanol, from the pyruvate-containing aqueous solution. Precipitating pyruvate as a precipitate has an extremely low yield and is not practical.
乳酸塩水溶液中で接触酸化脱水素することによって製造
したピルビン酸塩含有水溶液には、通常、副生成物とし
て、微量の酢酸塩と未反応の乳酸塩が含有される。A pyruvate-containing aqueous solution produced by catalytic oxidative dehydrogenation in an aqueous lactate solution usually contains trace amounts of acetate and unreacted lactate as byproducts.
このようなピルビン酸塩含有水溶液からピルビン酸塩を
、酢酸塩および未反応乳酸塩と分離し、ピルビン酸塩の
みを経済的に取得するのは困難であった。It has been difficult to economically obtain only pyruvate by separating pyruvate from acetate and unreacted lactate from such a pyruvate-containing aqueous solution.
すなわち、本発明の方法であるインプロパツールによる
沈澱析出法によれば、酢酸塩および乳酸塩はインプロパ
ツールに比較的良く溶解するために、ピルビン酸塩から
酢酸塩および乳酸塩を分離することも同時に行なうこと
ができる点も本発明の方法の優れた特徴の一つである。That is, according to the method of the present invention, which is a precipitation method using Improper Tool, acetate and lactate can be separated from pyruvate because acetate and lactate dissolve relatively well in Improper Tool. One of the excellent features of the method of the present invention is that it can be carried out simultaneously.
したがって、乳酸塩水溶液の接触酸化脱水素によって製
造したピルビン酸塩含有水溶液に本発明の方法を適用す
ることによって、副生成物である酢酸塩および未反応の
乳酸塩の分離を同時に行ないながら固体状のピルビン酸
塩を単離取得することができる優れた特徴を有する。Therefore, by applying the method of the present invention to a pyruvate-containing aqueous solution produced by catalytic oxidative dehydrogenation of an aqueous lactate solution, acetate, which is a byproduct, and unreacted lactate can be simultaneously separated and solidified. It has the excellent characteristics that pyruvate can be isolated and obtained.
以上のように、本発明の方法を適用するピルビン酸塩含
有水溶液は、酸化反応を終了後の反応液から触媒を分離
することにより得られるが、該水溶液が著しく着色して
いる場合には、該水溶液を、たとえば、活性炭処理など
、適当に脱色処理することが好ましい。As described above, the pyruvate-containing aqueous solution to which the method of the present invention is applied can be obtained by separating the catalyst from the reaction solution after the oxidation reaction has been completed, but if the aqueous solution is significantly colored, It is preferable to subject the aqueous solution to an appropriate decolorization treatment, such as activated carbon treatment.
脱色処理を実施せずにインプロパツールを添加すると、
析出した沈澱が着色し、着色沈澱の脱色は困難な場合が
多い。When Improper Tool is added without decolorization,
The deposited precipitate is colored, and it is often difficult to decolorize the colored precipitate.
本発明の方法を適用するピルビン酸塩水溶液の濃度は、
通常、20〜70wt%の範囲であるが、とくに30〜
50wt%の範囲が好ましい。The concentration of the pyruvate aqueous solution to which the method of the present invention is applied is:
Usually, it is in the range of 20 to 70 wt%, but especially 30 to 70 wt%.
A range of 50 wt% is preferred.
本発明の方法に用いられるイソプロパツールは、高純度
のアルコールである必要はなく、含水量でも十分使用す
ることができる。The isopropanol used in the method of the present invention does not need to be a highly pure alcohol, and can be used even if it has a water content.
含水量は、20〜30%であってもさしつかえない。The water content may be 20 to 30%.
したがって、本発明の方法に用いたイソプロパツールと
水との混合廃溶液に、簡単な蒸留操作を行なって、イソ
プロパツール88%、水12%の共沸混合液を回収し、
繰返し使用でき、このイソプロパツールは回収再使用す
るために特別な抽出蒸留を行なう必要もない。Therefore, the mixed waste solution of isopropanol and water used in the method of the present invention is subjected to a simple distillation operation to recover an azeotropic mixture of 88% isopropanol and 12% water.
It can be used repeatedly, and the isopropanol does not require special extractive distillation for recovery and reuse.
インプロパツールの使用量は、ピルビン酸塩含有水溶液
1容に対し、2〜10容、とくに4〜6容を使用するの
が好ましい。The amount of Impropatool to be used is preferably 2 to 10 volumes, particularly 4 to 6 volumes, per 1 volume of the pyruvate-containing aqueous solution.
イソプロパツールとピルビン酸塩含有水溶液を、前記の
比率で混合し、攪拌すれば白色のピルビン酸塩の沈澱が
析出する。When isopropanol and a pyruvate-containing aqueous solution are mixed in the above ratio and stirred, a white pyruvate precipitate is precipitated.
この沈澱は数時間以上放置熟成してから沢別分離する。This precipitate is left to ripen for several hours or more and then separated into sawasetsu.
沢別分離した沈澱は、室温ないし70℃で風乾するか、
減圧乾燥することにより製品とする。The precipitate separated by Sawabetsu is air-dried at room temperature to 70°C, or
The product is obtained by drying under reduced pressure.
以下実施例により本発明を説明する。The present invention will be explained below with reference to Examples.
実施例 1
乳酸ナトリウムの10%水溶液200グ、白金を2wt
%および、炭酸鉛3wt%を担持した活性炭粉末触媒4
グを気泡塔式の反応器に仕込み反応温度70℃で常圧空
気を吹込み、1時間30分反応を行なった。Example 1 200 g of 10% aqueous solution of sodium lactate, 2 wt of platinum
% and activated carbon powder catalyst supporting 3 wt% of lead carbonate 4
The mixture was charged into a bubble column type reactor, and normal pressure air was blown into the reactor at a reaction temperature of 70° C., and the reaction was carried out for 1 hour and 30 minutes.
反応終了後、触媒を沢別した反応液を高速液体クロマト
グラフィーにより分析したところ、乳酸ナトリウムの転
化率90%、ピルビン酸ソーダの選択率85%、酢酸ソ
ーダの選択率5%であった。After the reaction was completed, the reaction solution from which the catalyst had been removed was analyzed by high performance liquid chromatography, and the conversion rate of sodium lactate was 90%, the selectivity of sodium pyruvate was 85%, and the selectivity of sodium acetate was 5%.
この反応液を減圧下に5Ofまで濃縮し、イソプロパツ
ール100fを加え攪拌し、白色の沈澱を析出させた。This reaction solution was concentrated to 5Of under reduced pressure, and 10Of of isopropanol was added and stirred to precipitate a white precipitate.
白色沈澱を沢別し、減圧下45℃で乾燥し、ピルビン酸
ナトリウムの白色粉末13.7?を取得した。The white precipitate was separated and dried at 45°C under reduced pressure to obtain a white powder of sodium pyruvate 13.7? obtained.
得られた粉末を重水溶媒に溶かし、NMRスペクトルを
測定したところ、乳酸ナトリウムおよび酢酸ナトリウム
の含有量は微少であり、高純度のピルビン酸ナトリウム
が取得できた。When the obtained powder was dissolved in a heavy water solvent and the NMR spectrum was measured, the content of sodium lactate and sodium acetate was minute, and highly pure sodium pyruvate was obtained.
Claims (1)
れるピルビン酸塩含有水溶液からピルビン酸を単離する
に際し、該ピルビン酸塩含有水溶液とイソプロピルアル
コールとを混合し、ピルビン酸塩の固体を析出させるこ
とを特徴とするピルビン酸塩の単離方法。1. When isolating pyruvic acid from a pyruvate-containing aqueous solution obtained by oxidizing lactate in an aqueous solution with an oxygen-containing gas, the pyruvate-containing aqueous solution and isopropyl alcohol are mixed to separate the solid pyruvate. A method for isolating pyruvate, the method comprising precipitation.
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP399279A JPS5842855B2 (en) | 1979-01-19 | 1979-01-19 | Isolation method for pyruvate |
US06/028,695 US4242525A (en) | 1978-04-17 | 1979-04-10 | Process for producing salts of pyruvic acid |
CH339579A CH641140A5 (en) | 1978-04-17 | 1979-04-10 | METHOD FOR PRODUCING A SALT OF PYRUVINIC ACIDS. |
GB7912999A GB2018773B (en) | 1978-04-17 | 1979-04-12 | Process for producing salts of pyruvic acid |
CA325,454A CA1101882A (en) | 1978-04-17 | 1979-04-12 | Process for producing salts of pyruvic acid |
IT21888/79A IT1120113B (en) | 1978-04-17 | 1979-04-13 | PROCESS TO PRODUCE SALTS OF PYRUVIC ACID |
DE2915395A DE2915395C2 (en) | 1978-04-17 | 1979-04-14 | Process for the preparation of a salt of pyruvic acid |
FR7909654A FR2423472A1 (en) | 1978-04-17 | 1979-04-17 | PROCESS FOR PREPARING SALTS OF PYRUVIC ACID |
NLAANVRAGE7902985,A NL184516C (en) | 1978-04-17 | 1979-04-17 | PROCESS FOR THE PREPARATION OF SALTS OF PYROVINIC ACID. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP399279A JPS5842855B2 (en) | 1979-01-19 | 1979-01-19 | Isolation method for pyruvate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5598132A JPS5598132A (en) | 1980-07-25 |
JPS5842855B2 true JPS5842855B2 (en) | 1983-09-22 |
Family
ID=11572506
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP399279A Expired JPS5842855B2 (en) | 1978-04-17 | 1979-01-19 | Isolation method for pyruvate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5842855B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017007965A (en) * | 2015-06-18 | 2017-01-12 | ノーベルファーマ株式会社 | Method for producing sodium pyruvate |
-
1979
- 1979-01-19 JP JP399279A patent/JPS5842855B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5598132A (en) | 1980-07-25 |
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