JPS59106494A - Purification of phosphorylated ascorbic acid - Google Patents
Purification of phosphorylated ascorbic acidInfo
- Publication number
- JPS59106494A JPS59106494A JP21605382A JP21605382A JPS59106494A JP S59106494 A JPS59106494 A JP S59106494A JP 21605382 A JP21605382 A JP 21605382A JP 21605382 A JP21605382 A JP 21605382A JP S59106494 A JPS59106494 A JP S59106494A
- Authority
- JP
- Japan
- Prior art keywords
- ascorbic acid
- phosphorylated
- activated carbon
- filtered
- water
- 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
Links
Abstract
Description
【発明の詳細な説明】
本発明は燐酸化アスコルビン酸又はその塩類の新規な精
製方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for purifying phosphorylated ascorbic acid or its salts.
従来、アスコルビン酸は、その有する優れた生理作用に
より、医薬品、食品、化粧品その他各種の工業分野に使
用されているが、本来、熱や光に弱く、さらにその水溶
液は安定性が悪いため、分解や着色をし易いなどの欠点
がある。Conventionally, ascorbic acid has been used in pharmaceuticals, foods, cosmetics, and various other industrial fields due to its excellent physiological effects. It has drawbacks such as easy coloring.
これを改善する目的で、各種誘導体がこれまで合成され
ている。その中でも、アスコルビン酸の燐酸化エステル
やその塩類は、生体内で容易にアスコルビン酸に転換す
る特徴を有すると共に、現在提供されている他の誘導体
に較べ、水を含有する湿性製品での安定性がもつとも優
れていると云われている。Various derivatives have been synthesized for the purpose of improving this. Among these, phosphorylated esters of ascorbic acid and their salts have the characteristic of being easily converted into ascorbic acid in vivo, and are more stable in wet products containing water than other derivatives currently available. It is said that it is also excellent.
しかしながら、これらの燐酸化アスコルビン酸化合物で
あっても、例えばアスコルビン酸燐酸エステルマグネシ
ウム塩を用いる工業製品の場合、水が存在する系では、
経時的に徐々に着色が進行する傾向がある。こ\におけ
るアスコルビン酸燐酸エステルマグネ7ウム塩自体を分
析もしくは定量してもその含有量の減少は認められない
。従って、おそらくは、アスコルビン酸を出発原料とし
て合成するアスコルビン酸燐酸エステルマグネシウム塩
を製造する過程において、副反応が生じ、これに起因し
て微量の不鈍物が混在するものと考えられる。However, even with these phosphorylated ascorbic acid compounds, for example, in the case of industrial products using ascorbic acid phosphate ester magnesium salt, in a system where water is present,
Coloration tends to progress gradually over time. Even when the ascorbic acid phosphate ester magnesium salt itself is analyzed or quantified, no decrease in its content is observed. Therefore, it is considered that a side reaction occurs during the process of producing ascorbic acid phosphate magnesium salt synthesized using ascorbic acid as a starting material, and as a result of this, trace amounts of inert substances are mixed.
本発明者は、このような不純物を除き、着色のない精製
された燐酸化アスコルビン酸化合物を収率よく、経済的
に得るため、鋭意研究した結果、ついに目的とする本発
明を完成するに到ったのである。The present inventor has conducted intensive research in order to remove such impurities and obtain a purified phosphorylated ascorbic acid compound without coloring in a high yield and economically, and as a result, has finally completed the objective of the present invention. That's what happened.
すなわち、本発明は燐酸化アスコルビン酸又はその塩類
の精製方法に関するもので、その特徴とするところは、
燐酸化アスコルビン酸又はその塩類を水に溶解させ、活
性炭、ケイソウ土、酸性白土等から選択される一種又は
二種以上の担体に吸着させて脱色処理を行い、得られる
炉液に低級アルコール類あるいはケトン類のいずれか一
種又は二種以上の有機溶媒を添加せしめて生成物を沈澱
させ、これを戸遇した後、前記有機溶媒により洗浄し、
乾燥することを特徴とするものである。That is, the present invention relates to a method for purifying phosphorylated ascorbic acid or its salts, and its characteristics are as follows:
Phosphorized ascorbic acid or its salts are dissolved in water and decolorized by adsorption onto one or more carriers selected from activated carbon, diatomaceous earth, acid clay, etc., and lower alcohols or Adding one or more organic solvents of ketones to precipitate the product, allowing the product to settle, and then washing with the organic solvent,
It is characterized by drying.
次に、本発明に係る新規精製方法について、アスコルビ
ン酸燐酸エステルマグネシウム塩を例にして詳述すると
、粗製アスコルビン酸燐酸エステルマグネシウム塩を水
に溶解させて0.1〜10チ(重量類)を得、カラム法
又はパッチ法を用いて活性炭、ケイソウ土、酸性白土等
の担体好ましくは活性炭に吸着させて(水で溶出するこ
とにより)脱色処理を行い、微量の着色物質及び不純物
を除去する。この除、必要によシ担体微粉末を除去する
ため、ミルボアフィルター(ミルボア社)等で濾過処理
を行う。得られるカラム通過液もしくはパッチ処理濾過
液等の炉液に対し、メタノール、エタノール、インプロ
パツール、ブタノール、インブタノール等の低級アルコ
ール類、アセトン、ナト2ヒドロフラン等のケトン類な
どから選択される一種又は二種以上の有機溶媒を20〜
55%(容量チ)になる様に添加せしめて室温で10時
間以上又は40°Cで1時間以上、もしくは5℃で4時
間以上放置し、アスコルビン酸燐酸エステルマグネシウ
ム塩を沈澱させる。これを濾過せしめ、上記有機溶媒の
少なくとも一種好ましくはメタノール、エタノール、ア
セトン等を用いて洗浄し、次いで適宜の方法で乾燥させ
て脱水処理し、白色粉末状の精製されたアスコルビン酸
燐酸エステルマグネシウム塩を得る。Next, the novel purification method according to the present invention will be explained in detail using ascorbic acid phosphate magnesium salt as an example. Crude ascorbic acid phosphate magnesium salt is dissolved in water and 0.1 to 10 g (by weight) is dissolved in water. Then, a column method or a patch method is used to adsorb it on a carrier such as activated carbon, diatomaceous earth, acid clay, etc., preferably activated carbon, and perform a decolorization treatment (by elution with water) to remove trace amounts of colored substances and impurities. In order to remove the fine carrier powder, if necessary, filtration treatment is performed using a Milboa filter (Milboa Corporation) or the like. A type of alcohol selected from lower alcohols such as methanol, ethanol, impropatol, butanol, and imbutanol, and ketones such as acetone and nato-2-hydrofuran is applied to the obtained column-filtered liquid or patch-treated filtrate. Or two or more organic solvents for 20~
The ascorbic acid phosphate magnesium salt is precipitated by adding it to a concentration of 55% (by volume) and leaving it at room temperature for 10 hours or more, at 40°C for 1 hour or more, or at 5°C for 4 hours or more. This is filtered, washed with at least one of the above organic solvents, preferably methanol, ethanol, acetone, etc., and then dried and dehydrated by an appropriate method to obtain purified ascorbic acid phosphate magnesium salt in the form of a white powder. get.
上記以外の燐酸化アスコルビン酸化合物についてもはソ
同様の方法を用いたが、目的とすべき精製品は得られた
。The same method was used for phosphorylated ascorbic acid compounds other than those mentioned above, but the desired purified products were obtained.
本発明において重要なことは、上記精製過程における有
機溶媒の濃度が20〜55容量9g望ましくは30〜4
5容量チの範囲に維持されることでおる。55容量チを
超える場合、アスコルビン酸燐酸エステルマグネシウム
塩と共に不純物も沈澱し、目的とする精製効果が得られ
にくい。20容量チ未満では収率が著しく低下し、工業
製品として実用的でない。これらの有機溶媒の濃度は、
目的とする燐酸化アスコルビン酸化合物の種類によって
は、増減されてもよい。What is important in the present invention is that the concentration of the organic solvent in the purification process is 20-55% by volume, preferably 30-4%.
This can be achieved by maintaining the capacity within the range of 5. If the volume exceeds 55 cm, impurities will precipitate together with the ascorbic acid phosphate magnesium salt, making it difficult to obtain the desired purification effect. If it is less than 20 volumes, the yield will drop significantly and it will not be practical as an industrial product. The concentrations of these organic solvents are
The amount may be increased or decreased depending on the type of phosphorylated ascorbic acid compound targeted.
さらに必要なことは燐酸化アスコルビン酸と活性炭等の
担体(吸着剤)の重量比が1対5〜1対0.1の範囲(
好ましくは1対1〜1対0.2)に入る様にすることで
ある。1対5より担体が多いと回収率が著しく低下し、
1対0.1よす担体が少ないと精製効果が出にくい。Furthermore, it is necessary that the weight ratio of phosphorylated ascorbic acid and carrier (adsorbent) such as activated carbon be in the range of 1:5 to 1:0.1 (
Preferably, the ratio is 1:1 to 1:0.2). When the amount of carrier is more than 1:5, the recovery rate decreases significantly,
If the ratio of 1:0.1 carrier is small, it is difficult to obtain a purification effect.
次に、本発明の精製方法の実施例を示す。Next, examples of the purification method of the present invention will be shown.
実施例 1
L−アスコルビン酸−2−リン酸エステルマグネシウム
塩(未精製品)10.0.9を精製水50〇−に溶解す
る。この溶液に活性炭粉末10.0.!i’を添加し室
温にて30分間攪拌し6時間放置し活性炭に吸着させ脱
色処理する。吸引濾過により濾過し、精製水100m1
ずつで2回洗浄し、ろ液と洗液を合せる。この液を0.
22ミクロンのミリポアフィルタ−を用いて濾過する。Example 1 10.0.9 of L-ascorbic acid-2-phosphate magnesium salt (unpurified product) is dissolved in 500 of purified water. Add 10.0% of activated carbon powder to this solution. ! i' was added, stirred at room temperature for 30 minutes, and left to stand for 6 hours to be adsorbed onto activated carbon and decolorized. Filtered by suction filtration and purified water 100ml
Wash twice and combine the filtrate and washing liquid. Add this liquid to 0.
Filter using a 22 micron Millipore filter.
ろ液にメタノール5501nlを攪拌しつ\加え、室温
にて一晩放置する。生じたL−アスコルビン酸−2、−
リン酸エステルマグネシウム塩の白色沈澱を濾過しアセ
トンで洗浄脱水する。次いで風乾し、シリカゲルデシケ
ータ−中に一週間放置して目的とする精製品7.5gを
得た。(収率75チ)実施例 2
L−アスコルビン酸−2−リン酸エステルマグネシウム
塩(未精製品)20.[[’を精製水50〇−に溶解す
る。この溶液にケイソウ土(和光)1[1,Og及び活
性炭粉末10.0gを添加し、室温にて6D分間攪拌す
る。1時間放置しケイソウ土と活性炭に吸着させ脱色処
理した後吸引濾過する。戸紙上の担体を精製水100d
づつで2回洗浄する。p液と洗液を合せ、(122ミク
ロンのミリポアフィルタ−を用いて沖過する。F液にア
セトン400tnlを攪拌しつ\添加した後、40℃に
て1時間保ち、沈澱を熟成させる。次いでこれを濾過し
だ後、アセトンにて洗浄脱水し減圧乾燥して目的とする
白色の精製品16.0gを得た。Add 5501 nl of methanol to the filtrate with stirring, and leave it at room temperature overnight. The resulting L-ascorbic acid-2,-
The white precipitate of magnesium phosphate ester salt is filtered, washed with acetone and dehydrated. Then, it was air-dried and left in a silica gel desiccator for one week to obtain 7.5 g of the desired purified product. (Yield: 75 cm) Example 2 L-ascorbic acid-2-phosphate ester magnesium salt (unrefined product) 20. Dissolve [[' in 500 ml of purified water. Add 1[1,0 g of diatomaceous earth (Wako) and 10.0 g of activated carbon powder to this solution and stir for 6 D minutes at room temperature. The mixture was left for 1 hour to be adsorbed onto diatomaceous earth and activated carbon, decolorized, and then filtered with suction. 100 d of purified water on the carrier on the paper
Wash twice. The P solution and the washing solution are combined and filtered using a 122 micron Millipore filter. After adding 400 tnl of acetone to the F solution with stirring, the mixture is kept at 40°C for 1 hour to ripen the precipitate. This was filtered, washed with acetone, dehydrated, and dried under reduced pressure to obtain 16.0 g of the desired white purified product.
(収率80.0係)
実施例 6
L−アスコルビン酸−2−!Jン酸エステルマグネシウ
ム塩(未精製品)20.Clを精製水400m1に溶解
する。これを活性炭カラム(和光クロマト用活性炭50
メツシユ10.0gを水に分散し、径5αのガラスカラ
ムに充填)に注入し通過せしめて活性炭に吸着させ脱色
処理する。精製水によす溶出させ、カラム通過液の全量
が1000−になったところで溶出を終了する。0.2
2ミクロンのミリポアフィルタ−を用いてカラム通過液
を濾過し、活性炭の微粒子を除去する。涙液を攪拌しつ
\エタノール600−を加え一晩放置してL−アスコル
ビン酸−2−リン酸エステルマグネシウム塩の沈澱を生
じせしめる。次いでこれを濾過した後、エタノール(1
級)によシ洗浄し、減圧乾燥して目的とする精製品14
.7gを得た。(収率76.5係)
実施例 4
L−アスコルビン酸−2−リン酸エステルマグネシウム
塩(未精製品)30.0&を精製水500ゴを溶解する
。これを活性炭カラム(和光クロマト用活性炭50メツ
シユ20gを水に分散し、内径5crILのガラスカラ
ムに充填)に注入し通過せしめて活性炭に吸着させ脱色
処理する。精製水によシ溶出させ、カラム通過液の全量
が1000−になったところで溶出を終了する。0.2
2ミクロンのミリポアフィルタ−を用いてカラム通過液
を濾過し、活性炭の微粒子を除去する。炉液を攪拌しつ
51級アセトン650yd、を加え、5℃−4時間放置
してL−アスコルビン酸−2−リン酸マグネシウム塩を
沈澱させる。次いでこれを濾過しだ後、アセトン洗浄し
、攪拌しつ\窒素気流下で乾燥して目的とする精製品2
3.8 、li’を得た。(収率793チ)
上記の如くして得られた精製燐酸化アスコルビン酸又は
その塩類を各種水溶液に添加せしめることにより、着色
のない安定な燐酸化アスコルビン酸化合物を含有した水
溶液が提供されるものである。そして、更なる安定化の
向上を図るため、クエン酸、酒石酸、リンゴ酸等の有機
酸を一種又は二種添加してもよい。このような有機酸は
燐酸化アスコルビン酸化合物0.1〜5%(重量%)の
水溶液100部に対し、0.1〜6部が適量である。(Yield: 80.0) Example 6 L-ascorbic acid-2-! Magnesium chloride ester salt (unrefined product) 20. Dissolve Cl in 400 ml of purified water. Add this to an activated carbon column (activated carbon 50 for Wako chromatography).
10.0 g of mesh was dispersed in water, poured into a glass column (filled with a diameter of 5α), allowed to pass through, and adsorbed onto activated carbon for decolorization treatment. The column is eluted with purified water, and the elution is terminated when the total volume of the column-passing liquid reaches 1000. 0.2
The column passing liquid is filtered using a 2 micron Millipore filter to remove activated carbon particles. While stirring the lachrymal fluid, 600% of ethanol was added and allowed to stand overnight to precipitate L-ascorbic acid-2-phosphate magnesium salt. Then, after filtering it, ethanol (1
The desired purified product 14 is obtained by washing and drying under reduced pressure.
.. 7g was obtained. (Yield: 76.5%) Example 4 30.0 g of L-ascorbic acid-2-phosphate magnesium salt (unpurified product) was dissolved in 500 g of purified water. This is injected into an activated carbon column (20 g of 50 mesh of activated carbon for Wako chromatography is dispersed in water and packed into a glass column with an inner diameter of 5 crIL), allowed to pass through, and adsorbed onto the activated carbon for decolorization. The column is eluted with purified water, and the elution is terminated when the total volume of the column-passing liquid reaches 1000. 0.2
The column passing liquid is filtered using a 2 micron Millipore filter to remove activated carbon particles. While stirring the furnace liquid, 650 yd of grade 51 acetone was added, and the mixture was left at 5° C. for 4 hours to precipitate L-ascorbic acid-2-phosphate magnesium salt. Next, this is filtered, washed with acetone, stirred and dried under a nitrogen stream to obtain the desired purified product 2.
3.8, li' was obtained. (Yield: 793 cm) By adding the purified phosphorylated ascorbic acid or its salts obtained as described above to various aqueous solutions, an aqueous solution containing a stable phosphorylated ascorbic acid compound without coloration is provided. It is. In order to further improve stability, one or two organic acids such as citric acid, tartaric acid, and malic acid may be added. The appropriate amount of such an organic acid is 0.1 to 6 parts per 100 parts of an aqueous solution of 0.1 to 5% (weight %) of the phosphorylated ascorbic acid compound.
本発明の精製された燐酸化アスコルビン酸化合物と精製
未処理の燐酸化アスコルビン酸化合物について、その水
溶液の安定性試験を行った結果を下記表−1(高温安定
性)及び表−2(経時安定性)を以って示す。尚、表−
1及び表−2における試料はNa0H(1−N)とHC
’!(1−N)でpH8,0に調整したものである。The results of a stability test of aqueous solutions of the purified phosphorylated ascorbic acid compound of the present invention and the unpurified phosphorylated ascorbic acid compound are shown in Table 1 (high temperature stability) and Table 2 (temporal stability). gender). Furthermore, the table-
The samples in Table 1 and Table 2 are Na0H (1-N) and HC.
'! (1-N) to adjust the pH to 8.0.
着色の測定:試料の360 nmにおける吸光度(セル
長1cm )により着色の度合を測定した。Measurement of coloration: The degree of coloration was measured by the absorbance of the sample at 360 nm (cell length 1 cm).
データは吸光度で示した。Data were expressed as absorbance.
アスコルビン酸すン酸エステルマクネシウム塩含有量(
残存率%):アスコルビン酸リン酸エステルマグネシウ
ム塩の含有量を鉄塩比色法によシ測定し、試料作成時(
無処理)を100とした時の相対値((6)で示した。Ascorbic acid sulfate ester magnesium salt content (
Residual rate (%): The content of ascorbic acid phosphate magnesium salt was measured by the iron salt colorimetric method.
Relative value (shown as (6)) when non-treated) is set as 100.
(シス壬#、色う
未精製ははじめからかなりの着色が認められるが100
℃の処理により激しく着色し悪臭が生じていた。これに
反して精製品はほんのわずかしか着が認められず100
℃−6時間の処理でも変臭が起っていなかった。(Shisumi #, coloring unrefined coloring is recognized from the beginning, but it is 100%
Due to the treatment at ℃, it was intensely colored and had a bad odor. On the other hand, refined products have only a small amount of wear.
No odor was observed even after treatment at -6 hours.
クエン酸の添加は精製品、未精製品においてかなシの添
加効果が認められるものの、これだけでは変臭、着色を
防止出来なかった。又別の実験において、酒石酸、リン
ゴ酸等の有機酸においてもクエン酸と同様の効果がある
ことが認められた。Although the addition of citric acid was found to be effective in reducing odor and coloration in purified and unrefined products, this alone was not sufficient to prevent odor and coloration. In another experiment, it was found that organic acids such as tartaric acid and malic acid had the same effect as citric acid.
(ンス1 そ199
40℃、室温の経時試験においても精製品はほとんど又
はほんの少ししか着色せず、顕著な精製効果が認められ
た。Even in the aging test at 40°C and room temperature, the purified product was hardly or only slightly colored, and a remarkable purification effect was observed.
しかしアスコルビン酸リン酸エステルマグネシウム塩含
有量はほとんど変化せず、着色の原因は共存する少量の
不純物によるものと推定される。However, the ascorbic acid phosphate magnesium salt content hardly changed, and it is presumed that the cause of the coloring was a small amount of coexisting impurities.
又、表−6に燐酸化アスコルビン酸化合物の精製時での
溶媒濃度等の影響を示す。Furthermore, Table 6 shows the influence of solvent concentration, etc. during purification of the phosphorylated ascorbic acid compound.
エタノール濃度は低いほどfif製効果が高かった。一
般に55%(容量%)以下の溶媒濃度が精製に有効であ
った。別の実験において、メタノール、インプロパツー
ル類の低級アルコール、アセトンなどのケトン類等にも
同様の効果が認められた。但し溶媒濃度20俤(容量%
)未満では回収率が低いため工業的には実用的ではなか
った。The lower the ethanol concentration, the higher the fif production effect. In general, solvent concentrations of 55% (vol%) or less were effective for purification. In other experiments, similar effects were found with methanol, lower alcohols such as Improper Tools, and ketones such as acetone. However, the solvent concentration is 20 yen (volume%)
) is not industrially practical due to the low recovery rate.
本発明により精製される燐酸化アスコルビン酸化合物を
具体的に挙げると、L−アスコルビン[−3−1tン酸
エステル、L−アスコルビン酸−2−リン酸エステルマ
グネシウム塩、同カルシウム塩、同ナトリウム塩、L−
アスコルビン酸ビロリン酸マグネシウム塩その他各種の
化合物等である。Specifically, the phosphorylated ascorbic acid compounds purified by the present invention include L-ascorbic acid-3-1t ester, L-ascorbic acid-2-phosphoric ester magnesium salt, calcium salt, and sodium salt. ,L-
These include ascorbic acid birophosphate magnesium salt and various other compounds.
以上詳述した通υ、本発明は燐酸化アスコルビン酸又は
その塩類の新規な精製方法に関するものであり、着色の
ない安定な各種燐酸化アスコルビン酸化合物が好収率、
高純度で提供される。本発明により得られた精製燐酸化
アスコルビン酸化合物は、各種工業分野に適用され、特
に化粧品においては、化粧水等の水溶液で着色のない製
品が有利に得られるだけでなく、クリーム類、乳液類、
ゲル状物、粉体類等に使用でき、従来にない優れた品質
特性と生理活性のあるアスコルビン酸化合物が提供され
るものである。As detailed above, the present invention relates to a novel method for purifying phosphorylated ascorbic acid or its salts, which produces various stable phosphorylated ascorbic acid compounds without coloration in good yields.
Supplied in high purity. The purified phosphorylated ascorbic acid compound obtained by the present invention is applied to various industrial fields, and in particular, in cosmetics, it is useful not only for producing color-free products in aqueous solutions such as lotions, but also for creams, milky lotions, etc. ,
The present invention provides an ascorbic acid compound that can be used in gels, powders, etc., and has unprecedented quality characteristics and physiological activity.
特許出願人 ポーラ化成工業株式会社Patent applicant: POLA CHEMICAL INDUSTRIES, INC.
Claims (1)
せ、活性炭、ケイソウ土、酸性白土等から選択される一
種又は二種以上の担体に吸着させて脱色処理を行い、得
られる涙液に低級アルコール類あるいはケトン類のいず
れか一種又は二種以上の有機溶媒を添加せしめて生成物
を沈澱させ、これを涙過しだ後、前記有機溶媒により洗
浄し、乾燥することを特徴とする燐酸化アスコルビン酸
又はその塩類の精製方法。1. Dissolve phosphorylated ascorbic acid or its salts in water and adsorb it on one or more carriers selected from activated carbon, diatomaceous earth, acid clay, etc. for decolorization, and add lower alcohol to the resulting tear fluid. Phosphated ascorbin, characterized in that the product is precipitated by adding one or more organic solvents of the above-mentioned or ketones, and the product is filtered, washed with the organic solvent, and dried. Method for purifying acids or their salts.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21605382A JPS59106494A (en) | 1982-12-09 | 1982-12-09 | Purification of phosphorylated ascorbic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21605382A JPS59106494A (en) | 1982-12-09 | 1982-12-09 | Purification of phosphorylated ascorbic acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59106494A true JPS59106494A (en) | 1984-06-20 |
JPH0350758B2 JPH0350758B2 (en) | 1991-08-02 |
Family
ID=16682540
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21605382A Granted JPS59106494A (en) | 1982-12-09 | 1982-12-09 | Purification of phosphorylated ascorbic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59106494A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296410A (en) * | 1985-10-22 | 1987-05-02 | Showa Denko Kk | Bathing agent |
EP0679655A2 (en) * | 1994-04-28 | 1995-11-02 | Wako Pure Chemical Industries Ltd | Process for producing ascorbic acid derivative |
EP1059298A1 (en) * | 1999-06-07 | 2000-12-13 | F. Hoffmann-La Roche Ag | Process for purifying L-ascorbyl 2-monophosphate |
JP4812217B2 (en) * | 2000-03-03 | 2011-11-09 | サプレスタ エルエルシー | Benzofuranone stabilization of phosphate esters |
JP2012140330A (en) * | 2010-12-28 | 2012-07-26 | Tosoh Corp | Method for purifying water soluble phosphoric ester |
-
1982
- 1982-12-09 JP JP21605382A patent/JPS59106494A/en active Granted
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296410A (en) * | 1985-10-22 | 1987-05-02 | Showa Denko Kk | Bathing agent |
EP0679655A2 (en) * | 1994-04-28 | 1995-11-02 | Wako Pure Chemical Industries Ltd | Process for producing ascorbic acid derivative |
US5516919A (en) * | 1994-04-28 | 1996-05-14 | Wako Pure Chemical Industries, Ltd. | Process for producing ascorbic acid derivative |
EP0679655A3 (en) * | 1994-04-28 | 1996-05-22 | Wako Pure Chem Ind Ltd | Process for producing ascorbic acid derivative. |
EP1059298A1 (en) * | 1999-06-07 | 2000-12-13 | F. Hoffmann-La Roche Ag | Process for purifying L-ascorbyl 2-monophosphate |
JP4812217B2 (en) * | 2000-03-03 | 2011-11-09 | サプレスタ エルエルシー | Benzofuranone stabilization of phosphate esters |
JP2012140330A (en) * | 2010-12-28 | 2012-07-26 | Tosoh Corp | Method for purifying water soluble phosphoric ester |
Also Published As
Publication number | Publication date |
---|---|
JPH0350758B2 (en) | 1991-08-02 |
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