CN104557966B - Method for extracting active ingredients from cambogia - Google Patents

Method for extracting active ingredients from cambogia Download PDF

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CN104557966B
CN104557966B CN201510074533.9A CN201510074533A CN104557966B CN 104557966 B CN104557966 B CN 104557966B CN 201510074533 A CN201510074533 A CN 201510074533A CN 104557966 B CN104557966 B CN 104557966B
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acid
neogambogic
gamlogic
extracted
resina garciniae
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CN104557966A (en
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白易
马亚琼
赵永强
张成亮
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Inner Mongolia Changhui Biological Technology Co ltd
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Inner Mongolia Changhui Biotechnology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D493/00Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system
    • C07D493/12Heterocyclic compounds containing oxygen atoms as the only ring hetero atoms in the condensed system in which the condensed system contains three hetero rings
    • C07D493/20Spiro-condensed systems

Abstract

The invention provides a method for efficiently extracting active ingredients from traditional Chinese medicine cambogia. The method comprises the following steps: grinding and performing reflux extraction and concentration to the cambogia, to obtain extractum A; adding ethanol and dissolving, filtering, separating a filtrate after entering simulated moving bed chromatography, to obtain a component B rich in gambogic acid and a component C rich in gambogic acid and neogambogic acid; and recovering a solvent, and performing pressure-reduced drying to obtain two specifications of products: gambogic acid with the purity of more than 95%, and a mixture of gambogic acid with the purity of 10%-20% and neogambogic acid with the purity of 30%-50%. According to the method for extracting active ingredients from cambogia, the gambogic acid and neogambogic acid in cambogia can be separated and purified by adopting the simulated moving bed chromatography, the related separation parameters are determined, the steps are simple, the purity of the product is high, and the two specifications of gambogic acid and neogambogic acid can be simultaneously obtained, and the active ingredients in the raw materials are fully extracted and separated, and the raw material resources can be saved.

Description

A kind of method for extracting effective ingredient in Resina garciniae
Technical field
The present invention relates to a kind of method for extracting effective ingredient in Chinese medicine gamboge.
Background technology
Resina garciniae is the glue flowed out after the trunk of Garcinia maingayii Resina garciniae (Garcinia hanburyi Hook f.) is hurt Shape resin, or irregular block cylindric in yellowish-brown after being dried, matter are crisp frangible, originate in Southeast Asia, and China some areas are such as There is introducing and planting on the ground such as Yunnan, Guangxi, Guangdong.Contain gamlogic acid in Resina garciniae(Gambogic acid), neogambogic acid (Neomogenic acid), allogambogic acid(Allogambogic acid)Deng Multiple components.In clinical practice of Chinese medicine, rattan Huang is mainly used in treating the diseases such as swollen ulcer drug, ulcer, eczema, tumor, stubborn dermatitis.Modern pharmacological research shows that gamlogic acid is to more Kind of tumor cell has a stronger inhibitory action, and toxic and side effects are less in the effective dosage ranges, the suppression to tumor cell With higher selectivity, and intact animal's hemopoietic system and immunologic function are not affected.There are some researches show neogambogic acid Anti-tumor activity is about 2 times of gamlogic acid, is expected to exploitation for new type antineoplastic medicine.
In prior art, in CN101781309A, disclose a kind of using gamlogic acid in supercritical extraction Chinese medicine gamboge With the method for neogambogic acid.But the method need to strictly regulate and control pressure in kettle, it is difficult to adapt to the demand of industrialized production. CN101921283A discloses one of a kind of Resina garciniae by after crushing and silica gel, kieselguhr, silica flour or polyacrylamide and mixes Load column chromatography, Jing methanol, ethyl acetate equal solvent afford the gamlogic acid extracting method of gamlogic acid primary extract.Lin Qinghua etc. Combine to prepare neogambogic acid using silica gel column chromatography with preparative liquid chromatography, with organic solvent using less, avoid it is anti- Production loss that the high cost and extremely adsorbing of cladding analysis is caused, product purity can reach the advantage of chemical reference substance prescription (Chinese medicine journal, neogambogic acid prepare liquid phase separation method, Lin Qinghua, Zhang Jian, Li Guanglei etc., Vol.42, No.3, Jun.2014, P71-72).But above two method is to be suitable only for isolating gamlogic acid or a kind of effective ingredient of neogambogic acid, Remaining active component is caused to waste.
Simulated moving bed chromatography technology is that the design philosophy of Simulation moving bed is introduced in liquid phantom preparing chromatogram, is both maintained The consumption of liquid phantom preparing chromatogram is little, separation purity is high, and temperature-changeable is the advantages of operate, and overcomes usual liquid phantom preparing chromatogram again The shortcoming that can not be operated continuously so as to which strong with separating power, equipment volume is little, and cost of investment is low, and be particularly conducive to separate Thermal sensitivity is high and the features such as difficult detached thing system.
The content of the invention
The present invention is intended to provide a kind of method that its effective ingredient efficiently can be extracted from Chinese medicine gamboge.
The method that its effective ingredient is extracted from Resina garciniae of the present invention, comprises the following steps:
(1) dry Resina garciniae is crushed, crosses 40~80 mesh sieves, plus alcohol reflux is extracted, after extracting solution concentration, obtain extractum A;
(2) in extractum A add ethanol to be dissolved, filter, filtrate is separated into simulated moving bed chromatography, obtained To component B rich in gamlogic acid and component C containing gamlogic acid, neogambogic acid;
(3) recycling design, drying under reduced pressure obtain the gamlogic acid of the gamlogic acid of purity more than 95% and purity 10%~20% with The product of two kinds of specifications of neogambogic acid mixture of purity 30%~50%.
In step (1) of the present invention, alcohol can be methanol or ethanol.
In step (2) of the present invention, the adsorbent of simulated moving bed chromatography filling is low pole macroporous adsorbent resin, Water wash zone is purified water, and strippant is 20~50% ethanol, and its consumption is 1~3 times of resin volume;Resin absorption regenerated solvent For 95% ethanol or 2~4% sodium hydrate aqueous solutions;Adsorption zone 1~2BV/h of flow velocity;Water wash zone 1~3BV/h of flow velocity;Flow desorption zone 1~3BV/h of speed;Renewing zone 2~3BV/h of flow velocity;Switching time is 600~900s;Temperature control is at 40 DEG C~60 DEG C;Pressure control System is in 0.2MPa~0.6MPa.
Further, in step (2) of the present invention, the switching time preferably 700~800s of simulated moving bed chromatography.
Further, in step (2) of the present invention, the adsorbent of simulated moving bed chromatography filling is AB-8 or DM130.
Further, in step (2) of the present invention, strippant consumption is preferably 3 times of resin volume.
Further, in step (1) of the present invention, ultrasound assisted extraction can be adopted, 30~60 kHz of frequency is extracted, is carried 30~60 DEG C of temperature is taken, extraction time is 5~20min.
Although simulated moving bed technology can apply to natural product or the separating-purifying of medicine having had in the art altogether Know, but because Simulation moving bed it is big be structurally characterized in that by the key elements such as the continuous, adverse current in chemical industry, rectification, backflow all concentrate into System, it is multiple degrees of freedom, a dynamic, be mutually related nonlinear system.Therefore, prediction, optimization and control for it It is more complicated problem, in particular for a certain natural product kind, the prediction of separation parameter is a sufficiently complex problem. Chinese medicine gamboge extraction process of effective component of the present invention, using simulated moving bed chromatography method to the gamlogic acid in Resina garciniae and new Gamlogic acid carries out separating-purifying, it is determined that related separation parameter, and step is simple, and product purity is higher, can obtain two kinds simultaneously Effective ingredient in raw material is fully extracted separation, has saved raw material resources by the gamlogic acid of specification and neogambogic acid product.
Specific embodiment
Embodiment 1
The Gamboge that 200g is dried(Resina garciniae acid content 31.28%, neogambogic acid content 12.34%)40 mesh are crossed after crushing Sieve, adds 2L absolute methanols, reflux, extract, 2h, and repeats to extract once, merges whole extracting solution, concentrates as extractum A.To extractum Add 95% ethanol to be dissolved in A, filter, filtrate is separated into simulated moving bed chromatography.Adsorbent is inhaled for AB-8 macropores Attached resin, strippant are 25% ethanol water, and its consumption is 3 times of resin volume, and water wash zone is purified water, and resin absorption is again Solvent is given birth to for 95% ethanol, adsorption zone flow velocity 2BV/h, desorption zone flow velocity 3BV/h, water wash zone flow velocity 3BV/h, renewing zone flow velocity 3BV/h, switching time is 700s, temperature 50 C, pressure 0.5MPa.Isolated component B rich in gamlogic acid and contain Resina garciniae Acid, component C of neogambogic acid.Component B and C are separately recovered into solvent, drying under reduced pressure respectively obtains Resina garciniae acid content 95.2% Product 33.5g and Resina garciniae acid content 12.3%, the product 15.8g of neogambogic acid content 47.6%.
Embodiment 2
The Gamboge that 500g is dried(Resina garciniae acid content 31.28%, neogambogic acid content 12.34%)80 mesh are crossed after crushing Sieve, adds 95% ethanol solution 5L, reflux, extract, 2h, and repeats to extract once, merges whole extracting solution, concentrates as extractum A.To Add 95% ethanol to be dissolved in extractum A, filter, filtrate is separated into simulated moving bed chromatography.Adsorbent is DM130 Macroporous adsorbent resin, strippant are 30% ethanol water, and its consumption is 3 times of resin volume, and water wash zone is purified water, resin Absorption regeneration solvent be 95% ethanol, adsorption zone flow velocity 2BV/h, desorption zone flow velocity 3BV/h, water wash zone flow velocity 3BV/h, renewing zone Flow velocity 3BV/h, switching time is 750s, temperature 50 C, pressure 0.5MPa.Isolated component B rich in gamlogic acid and contain Component C of gamlogic acid, neogambogic acid.Component B and C are separately recovered into solvent, drying under reduced pressure respectively obtains Resina garciniae acid content 95.6% product 79.7g and Resina garciniae acid content 10.7%, the product 48.5g of neogambogic acid content 38.9%.
Embodiment 3
The Gamboge that 500g is dried(Resina garciniae acid content 31.28%, neogambogic acid content 12.34%)80 mesh are crossed after crushing Sieve, adds 95% ethanol solution 5L, the ultrasound assisted extraction 20min at 50kHz, 50 DEG C, is extractum by the extracting solution for obtaining concentration A.To in extractum A, add 95% ethanol to be dissolved, filter, filtrate is separated into simulated moving bed chromatography.Adsorbent is DM130 macroporous adsorbent resins, strippant are 30% ethanol water, and its consumption is 3 times of resin volume, and water wash zone is purified water, Resin absorption regenerated solvent be 95% ethanol, adsorption zone flow velocity 2BV/h, desorption zone flow velocity 3BV/h, water wash zone flow velocity 3BV/h, then Raw area flow velocity 3BV/h, switching time is 750s, temperature 50 C, pressure 0.5MPa.Isolated component B rich in gamlogic acid and Component C containing gamlogic acid, neogambogic acid.Component B and C are separately recovered into solvent, drying under reduced pressure respectively obtains Resina garciniae acid content 96.3% product 82.8g and Resina garciniae acid content 12.4%, the product 42.2g of neogambogic acid content 45.6%.

Claims (5)

1. a kind of method that gamlogic acid and neogambogic acid are extracted from Resina garciniae, it is characterised in that comprise the following steps:
(1) dry Resina garciniae is crushed, crosses 40~80 mesh sieves, plus alcohol reflux is extracted, after extracting solution concentration, obtain extractum A;
(2) in extractum A add ethanol to be dissolved, filter, filtrate is separated into simulated moving bed chromatography, is rich in Component B of gamlogic acid and component C containing gamlogic acid, neogambogic acid;
(3) recycling design, drying under reduced pressure obtain the gamlogic acid of the gamlogic acid of purity more than 95% and purity 10%~20% with it is pure The product of two kinds of specifications of neogambogic acid mixture of degree 30%~50%, wherein in the step (2), simulated moving bed chromatography is filled out The adsorbent for filling is AB-8 macroporous adsorbent resins or DM130 macroporous adsorbent resins, and water wash zone is purified water, strippant is 20~ 50% ethanol, 1~3 times for resin volume of its consumption;Resin absorption regenerated solvent is 95% ethanol or 2~4% sodium hydroxide Aqueous solution;Adsorption zone 1~2BV/h of flow velocity;Water wash zone 1~3BV/h of flow velocity;Desorption zone 1~3BV/h of flow velocity;Renewing zone flow velocity 2~ 3BV/h;Switching time is 600~900s;Temperature control is at 40 DEG C~60 DEG C;Stress control is in 0.2MPa~0.6MPa.
2. a kind of method that gamlogic acid and neogambogic acid are extracted from Resina garciniae as claimed in claim 1, it is characterised in that:It is described In step (1), alcohol can be methanol or ethanol.
3. a kind of method that gamlogic acid and neogambogic acid are extracted from Resina garciniae as claimed in claim 1 or 2, it is characterised in that: In the step (2), the switching time of simulated moving bed chromatography is 700~800s.
4. a kind of method that gamlogic acid and neogambogic acid are extracted from Resina garciniae as claimed in claim 1 or 2, it is characterised in that: In the step (2), 3 times for resin volume of strippant consumption.
5. a kind of method that gamlogic acid and neogambogic acid are extracted from Resina garciniae as claimed in claim 1 or 2, it is characterised in that: In the step (1), using ultrasound assisted extraction, extraction 30~60kHz of frequency, 30~60 DEG C of Extracting temperature, extraction time is 5 ~20min.
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