CS252039B1 - A method of isolating fl-escin from horse chestnut seeds - Google Patents
A method of isolating fl-escin from horse chestnut seeds Download PDFInfo
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- CS252039B1 CS252039B1 CS858794A CS879485A CS252039B1 CS 252039 B1 CS252039 B1 CS 252039B1 CS 858794 A CS858794 A CS 858794A CS 879485 A CS879485 A CS 879485A CS 252039 B1 CS252039 B1 CS 252039B1
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Abstract
Účelom je zlepšenie izolácie (3-escínu zo semien pagaštana koňského. Uvedený účel sa dosiahne tým, že sa semená extrahujú zmesou vody a alkoholu s počtom uhlíkov Ci až C3, extrakt sa pri teplote 40 až 80 °C zahustí, k zahuštěnému extraktu sa pri teplote 50 až 60 °C přidá kyselina do pH 2,8 až 1,6 a roztok sa odstaví na kryštalizáciu.The purpose is to improve the isolation of (3-escin from horse chestnut seeds. The stated purpose is achieved by extracting the seeds with a mixture of water and alcohol with a carbon number of Ci to C3, the extract is concentrated at a temperature of 40 to 80 °C, an acid is added to the concentrated extract at a temperature of 50 to 60 °C to a pH of 2.8 to 1.6 and the solution is set aside for crystallization.
Description
Vynález sa týká sposobu izolácie ^-escínu zo semien pagaštana koňského.The present invention relates to a process for the isolation of β-escin from horse chestnut seeds.
/J-Escín, používaný ako surovina pre výrobu farmaceutických prípravkov používaných napr. pri bečení posttraumatických a pooperačných edémov, sa izoluje zo semien pagaštana koňského (Aesculus hippocastanum L.j extrakciou alkoholmi, resp. zmesou alkoholov s vodou (pat. NDR 11178, pat. NSR 25 30 941), z extraktu sa (3-escín vyzráža cholesterolom (pat. NSR 1125 117), alebo sa extrakt preleje cez iónomenič v H cykle (pat. NSR 25 30 941], alebo sa okysli kyselinou do pH 1,5 až 2,0 (pat. NDR 11178), potom sa zahustí a ^f-escín sa vyzráža vodou. Ďalšie postupy využívajú extrakciu pomletých vysušených gaštanových semien vyššími alifatickými alkoholmi (pat. francúzsky 77 24 689, pat. španielsky 455 693), alebo ternárnymi zmesami ako metanol — chloroform — voda (pat. NSR 23 39 760). Je známy postup extrakcie semien pagaštana koňského vodným amoniakom, v extrakte sa upraví pH a ,3-escín sa extrahuje izopropanolom (pat. ZSSR 483 982). Pri ďalšom postupe (Cs. AO č. 227 627) sa semená extrahujú zmesou metanol — voda, extrakt sa zahustí pri teplote 20 až 40 °C, ochladí sa na teplotu 10 až 25 °C, přidá sa silná minerálna kyselina do pH 1,0, okyslený roztok sa zahřeje na teplotu 40 až 60 °C a vylúčený escín sa izoluje. Nevýhodou tohoto postupu je, že před přidáváním kyseliny sa extrakt ochladí a potom znovu zahřeje, čo je energeticky nevýhodné. Ďalšou nevýhodou je, že sa přidává silná minerálna kyselina do pH 1,0.[Beta] -Ecin, used as a raw material for the manufacture of pharmaceutical preparations used e.g. whilst post-traumatic and postoperative edema is bleached, it is isolated from the seeds of the horse-chestnut (Aesculus hippocastanum LI by extraction with alcohols or a mixture of alcohols with water (pat. GDR 11178, pat. NSR 1125 117), or the extract is passed through an ion exchanger in an H cycle (U.S. Pat. No. 25 30 941), or acidified to pH 1.5 to 2.0 (U.S. Pat. No. 11178), then concentrated and concentrated. f-escin is precipitated with water Other processes utilize the extraction of ground dried chestnut seeds with higher aliphatic alcohols (French Pat. No. 24 24 689, Spanish Pat. No. 455 693), or ternary mixtures such as methanol-chloroform-water (Pat. There is known a process for extracting equine grapevine seeds with aqueous ammonia, adjusting the pH in the extract and extracting the 3-escin with isopropanol (U.S. Pat. No. 483,982). water, extract is concentrated It is cooled to 10-25 ° C, strong mineral acid is added to pH 1.0, the acidified solution is heated to 40-60 ° C and the precipitated escin is isolated. The disadvantage of this procedure is that before the addition of the acid, the extract is cooled and then reheated, which is an energy disadvantage. Another disadvantage is that strong mineral acid is added to a pH of 1.0.
(S-Escín sa v prírodnom materiáli nachádza vo formě vodorozpustnej sodnej soli, z ktorej ho třeba uvolnit’ prídavkom kyseliny. Vo vodnom roztoku pri pH 4,2 je poměr disociovanej a nedisociovanej formy escínu v pomere 1: 1, to značí, že pre zrážanie je potřebné dosiahnuť pH nižšiu ako< je hodnota 4,2. /J-Escín je však glykozid, ktorý sa v kyslých roztokoch rozkládá. Rýchlosť rozkladu je úměrná znižovaniu pH a zvyšovaniu teploty. Právě z tohoto dovodu okyslenie extraktu do pH 1,0 viedlo k čiastočnému rozkladu produktu, ktorý sa pre dosiahnutie požadovaných parametrov musel rekryštalizovat z metanolu.(S-Escin is present in the natural material in the form of a water-soluble sodium salt from which it must be liberated by the addition of acid. In aqueous solution at pH 4.2, the ratio of dissociated and undissociated form of escin is 1: 1. precipitation is necessary to reach a pH lower than <4.2, but J-Escin is a glycoside which decomposes in acidic solutions, and the rate of decomposition is proportional to the decrease in pH and the temperature rise. resulted in a partial decomposition of the product which had to be recrystallized from methanol to achieve the desired parameters.
Nevýhody tohoto postupu sa odstránili postupom podta vynálezu, pri ktorom sa semená pagaštana koňského extrahujú zmesou vody a alkoholu s počtom uhlíkov Ci až C3, extrakt sa zahustí pri teplote 40 až 80 °C na 1/2 až 1/5 povodného objemu, přidá sa kyselina do pH 2,8 až 1,6 pri teplote 5!0 až 60 °C a roztok sa odstaví na kryštalizáciu. Výhodou tohoto postupu je, že zahusťovanie extraktu sa vykoná pri neutrálnom pH, kedy rozklad esterovej i glykozidlckej vazby je minimálny; pre uvofnenie escínu z jeho sodnej soli stačí upravit pH na hodnotu niže 2,8 a teda sa spotřebuje menšie množstvo kyseliny, pri nižšom stupni rozkladu glykozidickej vazby. Udržiavanie teploty na 50 až 60 °C je potřebné, aby produkt sa vylúčil vo vhodnej kryštalickej formě. Podfa tohoto postupu sa získal /3-escín bez ďalšej kryštalizácie takých parametrov, ako pri predošlom postupe s dodatečnou purifikáciou. Ďalšou výhodou je jednoduchšie spracovanie kryštalizačných lúhov úpravou pH, oddělením solí a zahuštěním — tento produkt možno použit napr. v kozmetických prípravkoch.The disadvantages of this process are eliminated by the process according to the invention, in which the horse chestnut seeds are extracted with a mixture of water and an alcohol having a carbon number of C1 to C3, the extract is concentrated at 40 to 80 ° C to 1/2 to 1/5 of the flood volume. acid to pH 2.8 to 1.6 at 5 ° C ! 0 to 60 ° C, and the solution is allowed to crystallize. The advantage of this procedure is that the concentration of the extract is carried out at neutral pH, with both ester and glycosidic bond decomposition being minimal; in order to release escin from its sodium salt, it is sufficient to adjust the pH to a value of less than 2.8, thus consuming less acid, with a lower degree of glycosidic bond decomposition. Maintaining the temperature at 50 to 60 ° C is required for the product to precipitate in a suitable crystalline form. According to this procedure, β-escin was obtained without further crystallization of such parameters as in the previous post-purification procedure. Another advantage is easier treatment of the crystallization liquors by adjusting the pH, separating the salts and concentrating - this product can be used e.g. in cosmetics.
Bližšie podrobnosti sposobu podta vynálezu sú zřejmé z príkladov prevedenia.Further details of the method of the invention are apparent from the examples.
Příklad 1Example 1
100 kg vysušených pomletých semien pagaštana koňského sa mieša 1 h v zmesi etanol — voda (1 000 1, poměr 1 : 1 j, suspenzia sa filtruje, filtrát sa vákuovo zahustí pri teplote 60 až 70 °C na výsledný objem 400 1, pri teplote 60 °C sa přidá kyselina fosforečná (2 mol/1) doi výsledného pH roztoku 2,4 a roztok sa odstaví na kryštalizáciu. Týmto postupom sa získalo 2,7 kg produktu, ktorý bez ďalšej rekryštalizácie vykazoval následovně parametre:100 kg of dried milled horse-chestnut seeds are stirred for 1 h in ethanol-water (1000 l, 1: 1 ratio), the suspension is filtered, the filtrate is concentrated under vacuum at 60 to 70 ° C to a final volume of 400 l at 60 ° C, phosphoric acid (2 mol / l) was added to a final pH of 2.4, and the solution was set aside to crystallize to give 2.7 kg of product, which had the following parameters without further recrystallization:
teplota tánia: 220 až 230 °C (rozkl.j [«]d20 —26,8 + 1 ° (c 5, metanol), množstvo vody 10,2 %, množstvo /?-escínu v sušině 99,6 %. Příklad 2 kg vysušených pomletých gaštanových semien sa 1 h mieša v 600 1 zmesi etanol — voda (6:4), suspenzia sa přefiltruje, filtrát sa pri teplote 60 až 70 °C vákuovo zahustí na objem 150 1, koncentrát sa okysli prídavkom kyseliny sírovej (5 mol/1) doi pH 1,8 a pri teplote 60 až 65 °C sa odstaví ku kryštalizácii.Melting point: 220 DEG-230 DEG C. (decomposition [.alpha.] D @ 20 = -26.8 DEG. + -. 1 DEG (c. 5, methanol); water: 10.2%; EXAMPLE 2 kg of dried ground chestnut seeds is stirred for 1 hour in 600 l of ethanol-water (6: 4), the suspension is filtered, the filtrate is concentrated to a volume of 150 l at 60-70 [deg.] C, the concentrate is acidified (5 mol / l) to pH 1.8 and at 60-65 ° C is set aside to crystallize.
Týmto postupom sa získalo 1,5 kg produktu, množstvo vody 11,3 °/o, množstvo β-escínu v sušině 99,7 °/o.This procedure yielded 1.5 kg of product, an amount of water of 11.3% / o, an amount of β-escin in dry matter of 99.7% / o.
P r i k 1 a d 3Example 1 and d 3
100 kg vysušených pomletých gaštanových semien sa mieša 1,5 h v 1 200 1 zmesi metanol — voda (55:45), suspenzia sa přefiltruje, filtrát sa pri teplote 40 až 60 °C za vákua zahustí na objem 600 1, zahuštěný roztok sa okysli kyselinou mravčou (koncentrovanou ) na pH. 2,8 a odstaví sa ku kryštabzácii.100 kg of dried ground chestnut seeds are stirred for 1.5 hours in 1 200 l of methanol-water (55:45), the suspension is filtered, the filtrate is concentrated to a volume of 600 l at 40-60 ° C under vacuum, and the concentrated solution is acidified formic acid (concentrated) to pH. 2.8 and set aside for crystallization.
Týmto postupom sa vyrobilo 1,9 kg produktu, množstvo vody 10,6 %, množstvo β-escínu v sušině 98,9 %.This procedure produced 1.9 kg of product, an amount of water of 10.6%, an amount of β-escin in the dry matter of 98.9%.
Claims (2)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS858794A CS252039B1 (en) | 1985-12-03 | 1985-12-03 | A method of isolating fl-escin from horse chestnut seeds |
| CS224488A CS268598B3 (en) | 1985-12-03 | 1988-04-01 | Method of aqueous-alkanolic solution preparation with betaescine content |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS858794A CS252039B1 (en) | 1985-12-03 | 1985-12-03 | A method of isolating fl-escin from horse chestnut seeds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS879485A1 CS879485A1 (en) | 1986-11-13 |
| CS252039B1 true CS252039B1 (en) | 1987-08-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS858794A CS252039B1 (en) | 1985-12-03 | 1985-12-03 | A method of isolating fl-escin from horse chestnut seeds |
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| Country | Link |
|---|---|
| CS (1) | CS252039B1 (en) |
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1985
- 1985-12-03 CS CS858794A patent/CS252039B1/en unknown
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| Publication number | Publication date |
|---|---|
| CS879485A1 (en) | 1986-11-13 |
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