JPH0796537B2 - Method for purifying 3- (3,4-dihydroxyphenyl) serine - Google Patents
Method for purifying 3- (3,4-dihydroxyphenyl) serineInfo
- Publication number
- JPH0796537B2 JPH0796537B2 JP62177757A JP17775787A JPH0796537B2 JP H0796537 B2 JPH0796537 B2 JP H0796537B2 JP 62177757 A JP62177757 A JP 62177757A JP 17775787 A JP17775787 A JP 17775787A JP H0796537 B2 JPH0796537 B2 JP H0796537B2
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- Japan
- Prior art keywords
- dops
- dihydroxyphenyl
- serine
- crude
- 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.)
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は工業的に有利な3−(3,4−ジヒドロキシフェ
ニル)セリン(以下、DOPSと略称する。)の精製方法に
関する。TECHNICAL FIELD The present invention relates to an industrially advantageous method for purifying 3- (3,4-dihydroxyphenyl) serine (hereinafter abbreviated as DOPS).
DOPSの精製法としては、特開昭51−32540号公報に示さ
れる如く、粗製DOPSを水に加熱還流下溶解し、冷却後に
析出する結晶をろ取することによって精製DOPSを得ると
云う、いわゆる再結晶精製法が知られていた。As a method for purifying DOPS, as shown in JP-A-51-32540, it is said that crude DOPS is dissolved in water under heating under reflux, and purified DOPS is obtained by filtering crystals that precipitate after cooling, so-called. Recrystallization purification methods were known.
上記の技術では、次の如き問題が未解決であった。例え
ば、L−3−(3,4−ジヒドロキシフェニル)セリン
(以下、L−DOPSと略称する。)の場合には、以下の如
くであった。The above-mentioned technique has not solved the following problems. For example, in the case of L-3- (3,4-dihydroxyphenyl) serine (hereinafter abbreviated as L-DOPS), it was as follows.
L−DOPSは水溶液中での熱安定性が悪い為、加熱還流
溶解時に劣化する。従って、加熱時間が延長すればL−
DOPSの分解が進行し、含量が低下する。Since L-DOPS has poor thermal stability in an aqueous solution, it deteriorates when dissolved under heating under reflux. Therefore, if the heating time is extended, L-
Decomposition of DOPS progresses and the content decreases.
以下に、水溶液中でのL−DOPSの熱安定性を示す。The thermal stability of L-DOPS in an aqueous solution is shown below.
粗製L−DOPSに対し、約60倍量の水を必要とするた
め、容積効率が悪い。 Since it requires about 60 times as much water as crude L-DOPS, it has poor volumetric efficiency.
L−DOPSの精製収率は約80%と低く、回収率が悪い。The purification yield of L-DOPS is as low as about 80%, and the recovery rate is poor.
以上の問題点は、工業的製造の見地からは、いずれも大
きな欠点であり、特に、における溶液中での熱安定性
が悪いと云うことは、大量製造時に、加熱溶解に要する
時間の延長による大巾な収率低下の原因となることが予
想される。The above problems are all major drawbacks from the viewpoint of industrial production, and in particular, the fact that the thermal stability in a solution in is poor is due to the extension of the time required for heating and dissolution during mass production. It is expected to cause a large decrease in yield.
従って、上記製造法は工業的製造法としては問題が多
く、DOPSの精製法としては、より有効な方法の開発が求
められていた。Therefore, the above production method has many problems as an industrial production method, and it has been required to develop a more effective method as a purification method of DOPS.
本発明者らは、かかる状況下、DOPSの工業的精製法とし
て、より有利な方法を鋭意検討した結果加熱再結晶化す
ることなく、適当な溶媒にDOPSを鉱酸塩として一度溶解
し塩基で中和することによりDOPSを結晶として析出させ
て、容易に精製DOPSを得る精製法を見出し、本発明を完
成した。Under such circumstances, as an industrial purification method for DOPS, the present inventors have earnestly studied a more advantageous method, and as a result, do not recrystallize by heating, and once dissolve DOPS as a mineral acid salt in an appropriate solvent to form a base. The present invention has been completed by finding a purification method for easily obtaining purified DOPS by precipitating DOPS as crystals by neutralization.
以下本発明方法について詳細に説明する。The method of the present invention will be described in detail below.
粗DOPSを水あるいは、50%(W/W)以上の水を含むメタ
ノールに懸濁した後、鉱酸を加え、粗DOPSを鉱酸塩とし
て溶解させる。水あるいは、50%(W/W)以上の水を含
むメタノールの量としては粗DOPSに対し6〜30倍重量用
いることができ、塩酸、硫酸、リン酸、硝酸等の鉱酸を
粗DOPSに対し、1.0〜2.0当量用いることができる。粗DO
PSを溶解させる温度は室温付近で充分であるが、0℃付
近まで冷却するか、あるいは50℃付近迄加熱しても良
い。すみやかに溶解させ、かつDOPSの分解を防ぐ点から
15〜30℃にて溶解させる事が好ましい。必要に応じて、
DOPSの空気酸化を防ぐ目的で、アスコルビン酸、亜硫酸
ナトリウム、亜硫酸水素ナトリウム、2,6−ビス(1,1−
ジメチル−エチル)−4−メチルフェノール(BHT)等
の抗酸化剤を粗DOPSに対し、0.1〜5%重量を加えても
良い。After suspending the crude DOPS in water or methanol containing 50% (W / W) or more of water, a mineral acid is added to dissolve the crude DOPS as a mineral acid salt. The amount of water or methanol containing 50% (W / W) or more of water can be 6 to 30 times as much as the weight of crude DOPS, and mineral acids such as hydrochloric acid, sulfuric acid, phosphoric acid, and nitric acid can be used as crude DOPS. On the other hand, 1.0 to 2.0 equivalents can be used. Coarse DO
Room temperature is sufficient for dissolving PS, but it may be cooled to around 0 ° C or heated up to around 50 ° C. From the point of dissolving quickly and preventing the decomposition of DOPS
It is preferable to dissolve at 15 to 30 ° C. If necessary,
For the purpose of preventing air oxidation of DOPS, ascorbic acid, sodium sulfite, sodium bisulfite, 2,6-bis (1,1-
An antioxidant such as dimethyl-ethyl) -4-methylphenol (BHT) may be added in an amount of 0.1 to 5% by weight based on the crude DOPS.
DOPSの鉱酸塩の水溶液または含水メタノール溶液は、鉱
酸を含む水または含水メタノールに粗DOPSを加えて調整
することもできる。An aqueous solution of a mineral acid salt of DOPS or a water-containing methanol solution can also be prepared by adding crude DOPS to water containing a mineral acid or water-containing methanol.
こうして得られたDOPSの鉱酸塩溶液は塩基を加え中和す
る事により精製DOPSの析出が行われるが、その前に必要
に応じ不溶物の除去の濾過操作あるいは、脱色あるいは
不純物の吸着を目的に0.5〜10%重量の活性炭を加えた
後の濾過操作を加えることもできる。中和に用いる塩基
としては水酸化ナトリウム、水酸化カリウム、炭酸ナト
リウム、炭酸水素ナトリウム、炭酸カリウム等、通常用
いられる無機塩基又はトリエチルアミン、ジエチルアミ
ン、モノメチルアミン等の有機アミン、あるいはアンモ
ニア等を挙げることができる。中和点としてはDOPSの等
電点付近に調整すれば良いが実際上はpH3〜8にて実施
することができ、得られる精製DOPSの収率、品質の点か
らはpH4.0〜6.0が特に好ましい。中和温度としては室温
付近で行えば良いが必須の条件ではなく0〜50℃にて実
施できる。収率を上げる目的からは中和後0℃付近まで
冷却してから析出した精製DOPSをろ取する事が好まし
い。ろ取して得られたDOPSは冷却した水にて洗浄した
後、乾燥することにより高品質の精製DOPSを収率良く得
ることができる。なお、本発明に使用される粗DOPSとし
てはL−DOPSのスレオ体、あるいはエリスロ体、DL−DO
PSのスレオ体、あるいはエリスロ体、D−DOPSのスレオ
体あるいはエリスロ体のいずれを用いてもよく、好適な
ものとしてはL−DOPSのスレオ体を挙げることができ
る。The DOPS mineral acid salt solution thus obtained is subjected to a filtration operation to remove insoluble matter or decolorization or adsorption of impurities before the precipitation of purified DOPS by neutralizing by adding a base. It is also possible to add a filtration operation after adding 0.5 to 10% by weight of activated carbon. Examples of the base used for neutralization include sodium hydroxide, potassium hydroxide, sodium carbonate, sodium hydrogen carbonate, potassium carbonate and the like, commonly used inorganic bases or organic amines such as triethylamine, diethylamine and monomethylamine, and ammonia and the like. it can. The neutralization point may be adjusted near the isoelectric point of DOPS, but in practice it can be carried out at pH 3 to 8, and in terms of yield and quality of purified DOPS obtained, pH 4.0 to 6.0 is recommended. Particularly preferred. The neutralization temperature may be around room temperature, but it is not an essential condition and it can be carried out at 0 to 50 ° C. For the purpose of increasing the yield, it is preferred to cool the purified DOPS after neutralization to around 0 ° C., and then collect the precipitated purified DOPS by filtration. The DOPS obtained by filtration is washed with cooled water and then dried to obtain high-quality purified DOPS with a good yield. The crude DOPS used in the present invention includes L-DOPS threo, erythro, and DL-DO.
Any of a threo body of PS, an erythro body, a threo body of D-DOPS or an erythro body may be used, and a preferable example thereof is a threo body of L-DOPS.
本発明方法は、従来知られていた水再結晶法と比較し、 精製操作が低温又は、室温付近で実施できる為、熱に
よるDOPSの劣化を避けることができる。Compared with the conventionally known water recrystallization method, the method of the present invention can avoid deterioration of DOPS due to heat because the refining operation can be carried out at a low temperature or near room temperature.
精製工程における容積効率が向上し、従来法と比較
し、2〜10倍改善された。The volumetric efficiency in the refining process was improved and was improved by 2 to 10 times as compared with the conventional method.
精製収率が大巾に向上した。The purification yield is greatly improved.
等の利点を有する工業的かつ有用なDOPSの精製法であ
る。It is an industrial and useful DOPS refining method having advantages such as the following.
つぎに本発明を実施例・参考例により説明するが本発明
はこれらに限定されるものではない。Next, the present invention will be described with reference to examples and reference examples, but the present invention is not limited thereto.
尚実施例・参考例中の純収率は下の式により算出したも
のである。The net yields in Examples and Reference Examples are calculated by the following formula.
純度(%)=高速液体クロマトグラフを用いた、絶体検
量線法による定量値。 Purity (%) = quantitative value by absolute calibration curve method using high performance liquid chromatograph.
実施例1 粗L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン100g(純度94.2%)、水1230g、L−アスコルビン
酸1.0gの混合液中に室温攪拌下36%塩酸71.7gを加え溶
解した。溶解を確認した後カルボラフィン5.0gを加え、
15分間攪拌した後ろ過し水135gで洗浄した。このろ液に
27%水酸化ナトリウム水溶液43.6gを滴下し、さらに27
%水酸化ナトリウム水溶液61.3gを1時間要して滴下し
た。さらに27%水酸化ナトリウム水溶液3.6gにてpH5.20
に調節した。その後、1時間室温にて攪拌した後pH4.8
〜5.3であることを確認して0〜5℃に冷却し、その温
度で2時間攪拌した。析出した結晶をろ取し、冷却した
0.05%L−アスコルビン酸水溶液145gで3回洗浄後、さ
らにアセトン115gで2回洗浄し、その後、乾燥する事に
よって精L−スレオ−3−(3,4−ジヒドロキシフェニ
ル)セリン89.0g(純度99.9%)、〔α〕D−39.6゜
(C=0.5,0.1N塩酸)を得た。(純収率94.4%)。Example 1 To a mixed solution of 100 g of crude L-threo-3- (3,4-dihydroxyphenyl) serine (purity 94.2%), 1230 g of water and 1.0 g of L-ascorbic acid was added 36% hydrochloric acid 71.7 g with stirring at room temperature. Dissolved. After confirming dissolution, add 5.0 g of carborafine,
After stirring for 15 minutes, the mixture was filtered and washed with 135 g of water. In this filtrate
Add 43.6 g of 27% sodium hydroxide aqueous solution, and add 27
% Aqueous sodium hydroxide solution (61.3 g) was added dropwise over 1 hour. Further, pH is 5.20 with 3.6 g of 27% sodium hydroxide aqueous solution.
Adjusted to. Then, after stirring at room temperature for 1 hour, pH 4.8
After confirming that it was ˜5.3, it was cooled to 0˜5 ° C. and stirred at that temperature for 2 hours. The precipitated crystals were collected by filtration and cooled
After washing 3 times with 145 g of 0.05% L-ascorbic acid aqueous solution, further washing twice with 115 g of acetone, and then drying, 89.0 g of pure L-threo-3- (3,4-dihydroxyphenyl) serine (purity 99.9) %), [Α] D −39.6 ° (C = 0.5, 0.1N hydrochloric acid). (Net yield 94.4%).
実施例2 粗L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン10.0g(純度94.2%)、50%含水メタノール268g、
L−アスコルビン酸0.1gの混合液中に室温攪拌下36%塩
酸4.52gを加え溶解した。溶解を確認した後カルボラフ
ィン0.5gを加え、15分間攪拌した後ろ過し、水13.5gで
洗浄した。このろ液にトリエチルアミン4.51gを3時間
要して滴下pH5.23に調整した。その後1時間室温にて攪
拌した後pH4.8〜5.3であることを確認して0〜5℃に冷
却し、その温度で2時間攪拌した。析出した結晶をろ取
し、冷却水14.5gで3回洗浄後、さらにアセトン11.5gで
2回洗浄し、その後、乾燥する事によって精L−スレオ
−3−(3,4−ジヒドロキシフェニル)セリン8.96g(純
度99.5%)、〔α〕D−39.1゜(C=0.5,0.1N塩酸)を
得た。(純収率94.6%)。Example 2 Crude L-threo-3- (3,4-dihydroxyphenyl) serine 10.0 g (purity 94.2%), 50% hydrous methanol 268 g,
While stirring at room temperature, 4.52 g of 36% hydrochloric acid was added and dissolved in a mixed solution of 0.1 g of L-ascorbic acid. After confirming the dissolution, 0.5 g of carborafine was added, stirred for 15 minutes, filtered, and washed with 13.5 g of water. 4.51 g of triethylamine was added to this filtrate over 3 hours, and the pH was adjusted to 5.23. After stirring at room temperature for 1 hour, it was confirmed that pH was 4.8 to 5.3, cooled to 0 to 5 ° C, and stirred at that temperature for 2 hours. The precipitated crystals were collected by filtration, washed 3 times with 14.5 g of cooling water, further washed twice with 11.5 g of acetone, and then dried to obtain purified L-threo-3- (3,4-dihydroxyphenyl) serine. 8.96 g (purity 99.5%) and [α] D- 39.1 ° (C = 0.5, 0.1N hydrochloric acid) were obtained. (Net yield 94.6%).
実施例3 粗L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン10g(純度94.2%)、水70g、L−アスコルビン酸0.
1gの混合液中に室温攪拌下36%塩酸7.17gを加え溶解し
た。溶解を確認した後不溶解物をろ去して水13.5gで洗
浄した。このろ液に27%水酸化ナトリウム水溶液10.86g
を1時間要して滴下しpH5.05に調整した。その後1時間
室温にて攪拌して0〜5℃に冷却し、その温度で2時間
攪拌した。析出した結晶をろ取し、冷却水14.5gで3回
洗浄後、さらにアセトン11.5gで2回洗浄し、その後、
乾燥する事によって精L−スレオ−3−(3,4−ジヒド
ロキシフェニル)セリン9.01g(純度99.6%)、〔α〕
D−39.5゜(C=0.5,0.1N塩酸)を得た。(純収率95.7
%)。Example 3 Crude L-threo-3- (3,4-dihydroxyphenyl) serine 10 g (purity 94.2%), water 70 g, L-ascorbic acid 0.
7.17 g of 36% hydrochloric acid was added to and dissolved in 1 g of the mixed solution at room temperature with stirring. After confirming dissolution, the insoluble material was filtered off and washed with 13.5 g of water. 27% sodium hydroxide aqueous solution 10.86g in this filtrate
Was added dropwise over 1 hour to adjust the pH to 5.05. Then, the mixture was stirred at room temperature for 1 hour, cooled to 0 to 5 ° C, and stirred at that temperature for 2 hours. The precipitated crystals were collected by filtration, washed with 14.5 g of cooling water three times, and further washed with 11.5 g of acetone twice, and then,
By drying, the purified L-threo-3- (3,4-dihydroxyphenyl) serine 9.01 g (purity 99.6%), [α]
D- 39.5 ° (C = 0.5, 0.1N hydrochloric acid) was obtained. (Net yield 95.7
%).
実施例4 粗L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン10g(純度94.2%)、水100gの混合物中に室温攪拌
下濃硫酸5.43gを加え溶解した。溶解を確認した後カル
ボラフィン0.5gを加え15分間攪拌した後濾過し、水13.5
gで洗浄した。このろ液に10%水酸化カリウム水溶液31.
10gを1時間要して滴下pH5.01に調整した。その後1時
間室温にて攪拌した後pH4.8〜5.3であることを確認して
0〜5℃に冷却し、その温度で2時間攪拌した。析出し
た結晶をろ取し、冷却水14.5gで3回洗浄後、さらにア
セトン11.5gで2回洗浄し、その後乾燥する事によって
精L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン8.80g(純度99.9%)、〔α〕D−39.7゜(C=0.
5,0.1N塩酸)を得た。(純収率93.3%)。Example 4 To a mixture of 10 g of crude L-threo-3- (3,4-dihydroxyphenyl) serine (purity 94.2%) and 100 g of water, 5.43 g of concentrated sulfuric acid was added and dissolved under stirring at room temperature. After confirming dissolution, add 0.5 g of carborafine, stir for 15 minutes, and then filter with water 13.5
washed with g. 10% aqueous potassium hydroxide solution 31.
The dropping pH was adjusted to 5.01 in 10 g of 1 hour. After stirring at room temperature for 1 hour, it was confirmed that pH was 4.8 to 5.3, cooled to 0 to 5 ° C, and stirred at that temperature for 2 hours. The precipitated crystals were collected by filtration, washed 3 times with 14.5 g of cooling water, further washed twice with 11.5 g of acetone, and then dried to obtain purified L-threo-3- (3,4-dihydroxyphenyl) serine 8.80. g (purity 99.9%), [α] D −39.7 ° (C = 0.
5,0.1 N hydrochloric acid) was obtained. (Net yield 93.3%).
実施例5〜15 実施例1と同様の操作方法により、粗L−DOPS10g(純
度94.2%)を用い表−1に記載した鉱酸、塩基、溶媒の
組合せ、及び使用量にて実施した。さらに得られた精−
L−DOPSの結果も同表に記載した。Examples 5 to 15 By the same operation method as in Example 1, 10 g of crude L-DOPS (purity: 94.2%) was used, and the combination of the mineral acid, the base and the solvent shown in Table 1 and the used amount were used. Further obtained spirit
The results of L-DOPS are also shown in the table.
参考例 粗L−スレオ−3−(3,4−ジヒドロキシフェニル)セ
リン10.0g(純度94.2%)水600g、L−アスコルビン酸
0.1gの混合液を100℃に加熱した。加熱還流下溶解した
ところで熱時濾過した後、熱水6gで2回洗浄した。ろ液
は徐冷、攪拌し0〜5℃で2時間攪拌して析出した結晶
をろ取し、冷却水14.5gで3回洗浄後乾燥する事によっ
て精L−スレオ−3−(3,4−ジヒドロキシフェニル)
セリン7.54g(純度99.8%)〔α〕D−39.5゜(C=0.
5,0.1N塩酸)を得た。(純収率79.9%)。 Reference Example Crude L-threo-3- (3,4-dihydroxyphenyl) serine 10.0 g (purity 94.2%) water 600 g, L-ascorbic acid
0.1 g of the mixture was heated to 100 ° C. When dissolved under heating under reflux, the solution was filtered while hot, and then washed twice with 6 g of hot water. The filtrate is gradually cooled, stirred and stirred at 0 to 5 ° C for 2 hours, and the precipitated crystals are collected by filtration, washed with 14.5 g of cooling water three times, and then dried to obtain purified L-threo-3- (3,4). -Dihydroxyphenyl)
Serine 7.54 g (purity 99.8%) [α] D- 39.5 ° (C = 0.
5,0.1 N hydrochloric acid) was obtained. (Net yield 79.9%).
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭58−216146(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-58-216146 (JP, A)
Claims (6)
(W/W)以上の水を含むメタノールからなる粗3−(3,4
−ジヒドロキシフェニル)セリンの溶液を、塩基を用い
て中和することにより、精製された3−(3,4−ジヒド
ロキシフェニル)セリンを析出させることを特徴とする
3−(3,4−ジヒドロキシフェニル)セリンの精製方
法。1. Water or 50% containing 1 or more equivalents of mineral acid.
Crude 3- (3,4) consisting of methanol containing more than (W / W) water
A solution of -dihydroxyphenyl) serine is neutralized with a base to precipitate purified 3- (3,4-dihydroxyphenyl) serine, and 3- (3,4-dihydroxyphenyl) is characterized. ) A method for purifying serine.
ェニル)セリンに対して1〜2当量である特許請求の範
囲第1項記載の精製方法。2. The purification method according to claim 1, wherein the amount of the mineral acid is 1 to 2 equivalents relative to the crude 3- (3,4-dihydroxyphenyl) serine.
ノールの量が粗3−(3,4−ジヒドロキシフェニル)セ
リンに対して6〜30重量倍である特許請求の範囲第1項
または第2項記載の精製方法。3. The amount of water or methanol containing 50% (W / W) or more of water is 6 to 30 times by weight the amount of crude 3- (3,4-dihydroxyphenyl) serine. The purification method according to item 1 or 2.
リンとして粗L−3−(3,4−ジヒドロキシフェニル)
セリンまたは粗DL−3−(3,4−ジヒドロキシフェニ
ル)セリンを用いる特許請求の範囲第1項、第2項また
は第3項記載の精製方法。4. Crude L-3- (3,4-dihydroxyphenyl) as crude 3- (3,4-dihydroxyphenyl) serine
The purification method according to claim 1, 2, or 3, wherein serine or crude DL-3- (3,4-dihydroxyphenyl) serine is used.
請求の範囲第1項記載の精製法。5. The purification method according to claim 1, wherein sulfuric acid or hydrochloric acid is used as the mineral acid.
リウム、ジエチルアミンまたはトリエチルアミンを用い
る特許請求の範囲第1項記載の精製法。6. The purification method according to claim 1, wherein sodium hydroxide, potassium hydroxide, diethylamine or triethylamine is used as the base.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62177757A JPH0796537B2 (en) | 1987-07-16 | 1987-07-16 | Method for purifying 3- (3,4-dihydroxyphenyl) serine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62177757A JPH0796537B2 (en) | 1987-07-16 | 1987-07-16 | Method for purifying 3- (3,4-dihydroxyphenyl) serine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6422849A JPS6422849A (en) | 1989-01-25 |
| JPH0796537B2 true JPH0796537B2 (en) | 1995-10-18 |
Family
ID=16036594
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62177757A Expired - Lifetime JPH0796537B2 (en) | 1987-07-16 | 1987-07-16 | Method for purifying 3- (3,4-dihydroxyphenyl) serine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0796537B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002080435A (en) * | 2000-06-26 | 2002-03-19 | Kanegafuchi Chem Ind Co Ltd | Method for producing 3-amino-2-hydroxypropionic acid derivative |
| CN103086906B (en) * | 2011-11-03 | 2015-04-01 | 重庆圣华曦药业股份有限公司 | Droxidopa crystal and preparation method thereof |
| CN113307741B (en) * | 2020-02-26 | 2024-05-14 | 东莞市东阳光仿制药研发有限公司 | Preparation method of droxidopa |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58216146A (en) * | 1982-06-09 | 1983-12-15 | Sumitomo Chem Co Ltd | Preparation of optical active-threo-3-(3,4- dihydroxyphenyl)serine |
-
1987
- 1987-07-16 JP JP62177757A patent/JPH0796537B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6422849A (en) | 1989-01-25 |
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