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Methods for purifying proanthocyanidin oligomers

一种原花色素、低聚物的技术,应用在有机化学等方向,能够解决不适合工业分离方法等问题

Inactive Publication Date: 2004-05-26
ASAHI GRP HLDG LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, these methods are not suitable as industrial separation methods for large-scale purification due to safety and economical factors

Method used

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  • Methods for purifying proanthocyanidin oligomers
  • Methods for purifying proanthocyanidin oligomers
  • Methods for purifying proanthocyanidin oligomers

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0077] Example 1 Purification by solid-liquid extraction (A)

[0078] 300 ml of methyl acetate was added to 30 g of the proanthocyanidin fraction obtained in Reference Example 1, and then solid-liquid extraction was performed at room temperature for 1 hour. The extraction was carried out twice in total, and the extracts from the two extractions were combined and filtered. Next, the extracted residue was washed with a small amount of methyl acetate. The methyl acetate extracts and washings were combined and concentrated under reduced pressure. A small amount of distilled water was added thereto, followed by concentration again under reduced pressure, and the extracted components were dissolved in an aqueous solution. The resulting aqueous solution was freeze-dried to obtain 17.5 g of a powdery methyl acetate extract. Then, the extraction residue was dried to obtain 12.5 g of a powdery non-extract after extraction with methyl acetate. The contents of dimeric and trimeric pro...

Embodiment 2

[0081] Example 2 Purification by Solid-Liquid Extraction (B)

[0082] Methyl acetate and different solvents were mixed in a volume ratio of 9:1 (when mixing with methyl acetate:hexane, the ratio was 9:5), thus preparing a solvent for solid-liquid extraction. Among the various solvents used are methyl acetate-miscible organic solvents: methanol, ethanol, propanol, butanol, ethyl formate, ethyl acetate, acetone, acetonitrile, tetrahydrofuran, hexane or acetic acid. 10 ml of a solvent for extraction was added to 1 g of each proanthocyanidin fraction obtained in Reference Example 1, and the mixture was subjected to solid-liquid extraction at room temperature for 1 hour (single extraction). After removing solid components from the extract by centrifugal filtration, a certain amount of the extract was diluted 100-fold with distilled water (0.01→1 ml). The contents of PB1, PB2 and PC1 were then measured by the reversed-phase liquid chromatography described in Reference Example 2. A...

Embodiment 3

[0084] Example 3 Purification by Solid-Liquid Extraction (C)

[0085] Methyl acetate and ethyl acetate were mixed at the volume ratios listed in Table 3, followed by solid-liquid extraction. 10 ml of solvents for extraction having different volume ratios were added to 1 g of each proanthocyanidin fraction obtained in Reference Example 1, followed by solid-liquid extraction at 30° C. for 1.5 hours. This step was repeated three times. These extracts were combined, concentrated under reduced pressure, and freeze-dried, whereby a powdery product (extract) was obtained. The contents of PB1, PB2 and PC1 in the powder product were measured by reversed-phase liquid chromatography described in Reference Example 2. Table 3 has listed the result with the solvent extraction of different volume ratios, comprises the total yield (%) of solid content yield (%), PB1, PB2 and the total yield of PC1 and the total yield of PC1, PB2 and PC1 respectively purity.

[0086] solvent for e...

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Abstract

The present invention relates to a process for purifying dimeric to pentameric proanthocyanidin oligomers which comprises extracting the proanthocyanidin oligomers from raw materials containing the proanthocyanidin oligomers or crude purification products therefrom by solid-liquid extraction using methyl acetate as a liquid phase; a process for purifying dimeric to pentameric proanthocyanidin oligomers which comprises pretreating with an enzyme for hydrolysis raw materials containing the proanthocyanidin oligomers, crude purification products therefrom, or a solution containing one of these; and a process for purifying dimeric to pentameric proanthocyanidin oligomers with a uniform polymerization degree which comprises separating and purifying the proanthocyanidin oligomers by polymerization degree from raw materials containing the proanthocyanidin oligomers or crude purification products therefrom by normal phase silica gel liquid chromatography using as a mobile phase a single solvent or a mixed solvent of two or more solvents selected from the group consisting of an ester solvent, a ketone solvent, a hydrocarbon solvent, an ether solvent and an alcohol solvent.

Description

technical field [0001] The present invention relates to a method for efficiently purifying high-purity proanthocyanidin oligomers. This oligomer has different biological activities, including anti-tumor, anti-inflammatory, anti-aging, anti-oxidation, anti-allergic, antibacterial, and hair growth activities, etc., and can be effectively applied in food, cosmetics, drugs, etc. Background technique [0002] Generally, it is known that proanthocyanidin is a kind of bioprotective substance of advanced plants, and it is the generic name of a class of polymers. 4β→8·2β0→7 and other bond-forming dimers or polymers exist. These oligomers are also called condensed tannins ("E.Steinegger·R.Hnsel, Pharmacognosy [Vol. 1], Approach to Chemistry and Pharmacology" (translated by Shuji Itokawa et al., Hirokawa Publishing Company), 204-208 (1977) ; Porter L.J., Flavans and Proanthocyanidins, In: Harborne J.B. (ed.), "the Flavonoids, Advances in ResearchScience 1986", Cha...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D311/60C07D311/62
CPCC07D311/62C07D311/60
Inventor 本多伸吉高桥知也神村彩子松冈贵子神田智正柳田显郎稗田一男
Owner ASAHI GRP HLDG LTD