CN108310039A - A method of extraction Gypenosides - Google Patents

A method of extraction Gypenosides Download PDF

Info

Publication number
CN108310039A
CN108310039A CN201810458420.2A CN201810458420A CN108310039A CN 108310039 A CN108310039 A CN 108310039A CN 201810458420 A CN201810458420 A CN 201810458420A CN 108310039 A CN108310039 A CN 108310039A
Authority
CN
China
Prior art keywords
column
resin
ethyl alcohol
gypenosides
extraction
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.)
Pending
Application number
CN201810458420.2A
Other languages
Chinese (zh)
Inventor
刘哲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201810458420.2A priority Critical patent/CN108310039A/en
Publication of CN108310039A publication Critical patent/CN108310039A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K36/00Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
    • A61K36/18Magnoliophyta (angiosperms)
    • A61K36/185Magnoliopsida (dicotyledons)
    • A61K36/42Cucurbitaceae (Cucumber family)
    • A61K36/424Gynostemma
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2236/00Isolation or extraction methods of medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicine
    • A61K2236/30Extraction of the material
    • A61K2236/33Extraction of the material involving extraction with hydrophilic solvents, e.g. lower alcohols, esters or ketones
    • A61K2236/333Extraction of the material involving extraction with hydrophilic solvents, e.g. lower alcohols, esters or ketones using mixed solvents, e.g. 70% EtOH
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2236/00Isolation or extraction methods of medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicine
    • A61K2236/30Extraction of the material
    • A61K2236/39Complex extraction schemes, e.g. fractionation or repeated extraction steps
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2236/00Isolation or extraction methods of medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicine
    • A61K2236/50Methods involving additional extraction steps
    • A61K2236/55Liquid-liquid separation; Phase separation

Landscapes

  • Health & Medical Sciences (AREA)
  • Natural Medicines & Medicinal Plants (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Alternative & Traditional Medicine (AREA)
  • Biotechnology (AREA)
  • Botany (AREA)
  • Medical Informatics (AREA)
  • Medicinal Chemistry (AREA)
  • Microbiology (AREA)
  • Mycology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Steroid Compounds (AREA)

Abstract

The invention discloses a kind of convenient, system, the methods of integrated extraction Gypenosides, and described method includes following steps:1st step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;2nd step:Gynostemma pentaphyllum powder is put and is extracted in ethanol, filtrate is obtained;3rd step:The upper resin column of filtrate is adsorbed, until resin is saturated;The saponin(e adsorbed in the resin column is desorbed using ethyl alcohol, obtains ethyl alcohol stripping liquid;The ethyl alcohol stripping liquid is distilled, ethyl alcohol is recycled, solid drying obtains Gypenosides powder;4th step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, it is made to restore original composition and performance.This method have medicinal material pre-treatment, extraction, column chromatography, resin regeneration difference free of discontinuities separation engagement process, separative efficiency is high, separation process is stable, is convenient for Quality Control, and the Gypenosides of destination number can be obtained by the control of portion link.

Description

A method of extraction Gypenosides
Technical field
The present invention relates to active ingredients from traditional Chinese medicinal extractive technique fields, and in particular to a kind of side of extraction Gypenosides Method.
Background technology
Gypenosides, have the effects that reducing blood lipid, improve myocardial ischemia-anoxemia, cerebral ischemia is protected, anti-oxidant.Nourishing heart Invigorating the spleen, QI invigorating and blood, eliminating phlegm stagnation resolvation are suitable for hyperlipidemia, see had palpitation shortness of breath, limb uncomfortable in chest fiber crops, dizziness and headache, forgetful ear The hearts Spleen-Qi Deficiencies such as ring, unconsciously sweat and tire or abdominal fullness and distention, phlegm hinder blood stasis person.
The pharmacological action of Gypenosides:Drug composition mainly has Gypenosides.Have reducing blood lipid, platelet aggregation-against, It is the effects that damage, anti-aging of resisting myocardial ischemia, specific as follows:
1. reducing blood lipid:Serum lipids in rats is induced with high glucose and high fat feed, gives Gypenosides treatment (7 days), as a result Treatment group's serum cholesterol, triacylglycerol content are significantly reduced than control group;Its curative effect and dosage are in a linear relationship.Experiment in vitro Show that Gypenosides can inhibit adipocyte and be decomposed to form free fatty, inhibit in adipocyte intake glucose synthesis Property aliphatic acid.In addition, the medicine reduce blood fat simultaneously, also can antiatherosclerosis, make arterial wall plaque formed reduce, damage Mitigate.
2. resist myocardial ischemia damage:Results of Animal shows that Gypenosides can not only reduce myocardial infarction model Enclose, and can fight Post-ischemic Reperfusion damage (make cardiac muscle cell's marshalling, it is clear in structure, mitochondrial swelling mitigate, Vacuole is reduced, and cell chromosome is uniform).
3. platelet aggregation-against:Experiment in vitro prove Gypenosides obviously inhibit platelet aggregation (collagen, ADP, arachidonic acid) induction platelet aggregation;The visible blood platelet of Ultrastructural observation is in dispersed, and surface is smooth, no puppet Foot-shape is at intracellular granular is more and clear.
4. the influence of pair haemodynamics:To dog intravenous injection Gypenosides (1mg/kg), it is seen that angiocarpy is in excitement Effect, systolic pressure and diastolic pressure are shown in raising (systolic pressure, which increases, is more than diastolic pressure), and effect maintains 30 minutes or more;Changes in heart rate Unobvious.In addition myocardial contraction and diastolic performance can be improved, minute output is made to increase, myocardium blood circulation improves.Escalated dose To angiocarpy, in inhibiting effect, (blood pressure reduces intravenous (20mg/kg), and heart rate is slack-off, and myocardial contraction and diastolic performance reduce, and make defeated Output is reduced).
5. enhancing sexual function acts on:Herb Gynostemmae Pentaphylli extract gavage can make the testis and prostate, female mice of male mice Uterus weight is significantly increased compared with the control group, illustrates that gynostemma pentaphylla has male, the effect of female hormone sample.
6. enhancing muscle power and antifatigue effect:(1) Gypenosides, water extract are experiments have shown that can extend mouse swimming time And pole-climbing time and loading swimming time.Continuous 14 days of the Herb Gynostemmae Pentaphylli extract gavage of larger dose can make to swim for a long time big Mouse keeps, compared with elevated blood glucose levels, reducing muscle glycogen loss, this may be the antifatigue major reason of gynostemma pentaphylla;(2) gynostemma pentaphylla can Mouse is improved to the time-to-live under the higher environment of tolerance and temperature of normobaric hypoxia.
7. enhancing immunization gynostemma pentaphylla can increase normal mouse spleen and thymic weight;Gypenoside can also fight ring Mouse spleen and thymic weight caused by phosphamide decline.And Phagocytosis By The Peritoneal Macrophages In Mice can be enhanced.
8. anti-free radical effects:(1) gypenoside can be substantially reduced naturally-aged and experiment aging rats liver With plasma adherence (LPO) content.Clinical research reports that LPO values obviously increase in old man's patients with coronary heart disease blood, take It is substantially reduced with LPO values after compound gynostemma pentaphylla preparation, is restored to the level of healthy male the elderly;(2) Gypenosides can make Malonaldehyde (MDA) is reduced in exhausted movemeat mouse core nephridial tissue, superoxide dismutase compound mutase (SOD) activity in nephridial tissue It increases, SOD/MDA ratios are opposite to be increased, and has the function that protect heart nephridial tissue that radical damage is immunized.With gynostemma pentaphylla alcohol extract It feeds mouse and not only improves Mouse Liver SOD activity, while also enhancement of SOD is heat-resisting, acid resistance, plays the role of protecting SOD.
9. life test --- " cell-activating effect ":Gynostemma pentaphylla and its compound preparation can extend mouse average life span and Maximum life span.According to another report, gynostemma pentaphylla extends the biological cell proliferation of composition and passes on, in the culture solution containing total glycosides 200mg/ml, The fibroblast of the in vitro normal diploid of human fetal is set to breed to 59 generations, and control group only reached for 51 generations and just stops growing, and prolonged Long 15.7%;Receive the Skin Cell cultured in vitro of syndrome patient to Xiong Er, control group was only multiplied for 22 generations, and gynostemma pentaphylla group extends to In 27 generations, extended 22%, therefore have the title of cell-activating agent.
The extraction process of original Gypenosides is handled before medicinal material, is extracted, there is larger defect in column chromatography, tool Body is shown as:Of high cost, low output, total glycosides type lack and then curative effect are caused to decline.
Invention content
The purpose of the present invention is to provide a kind of methods of extraction Gypenosides, to solve existing Gypenosides The problem of extraction process is of high cost, low output, total glycosides type lack and then curative effect caused to decline.
To achieve the above object, the technical scheme is that:
A method of extraction Gypenosides, described method includes following steps:
(1) step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;
(2) step:The gynostemma pentaphyllum powder that (1) step obtains is put and is extracted in ethanol, filtrate is obtained;
(3) step:The upper resin column of the filtrate is adsorbed, after resin saturation, stops filtrate upper prop;Using ethyl alcohol solution The saponin(e adsorbed in the resin column is inhaled, ethyl alcohol stripping liquid is obtained;The ethyl alcohol stripping liquid is distilled, ethyl alcohol, solid are recycled Drying obtains water-soluble and liposoluble ingredient Gypenosides powder (A powder);The resin column by being sequentially connected in series from top to bottom D101 large pore resin absorption columns, the first cationic resin column, resin anion (R.A.) column and the second cationic resin column composition;
(4) step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, the resin is made to restore original Composition and performance.
As a preferred solution, the D101 large pore resin absorption columns being sequentially connected in series from top to bottom, first sun from The column volume ratio of sub- resin column, resin anion (R.A.) column and the second cationic resin column is 1:1:3:1.
As a preferred solution, first cationic resin column is sulfonic group cation exchange column;It is described it is cloudy from Sub- resin column is strong-base anion-exchange resin column;Second cationic resin column is sulfonic group cation exchange column.
D101 macroporous absorbent resins are a kind of polymer absorbants with the synthesis of porous spongy structure artificial, by tree Van der Waals force between fat skeleton and the molecule (adsorbate) adsorbed carries out physical absorption by the huge specific surface area of resin And achieve the purpose that the water-soluble poor organic macromolecule of separation and Extraction from aqueous solution.Medium-height grass is extracted using macroporous absorbent resin Pharmaceutically active ingredient such as soaping agents, flavonoids, alkaloids, have easy to operate, cost is relatively low, resin can Reusability etc. it is excellent Point is suitable for industrial-scale production.
Sulfonic group cation exchange column is to be bonded a kind of novel sulfonic acids base sun in the inertia Silica Surface of high-purity Ion exchange ligand.This unique bonding structure is a kind of polymerization capsule structure of stabilization, than common polymer ions Exchange column column imitates higher, and has better mechanical strength and reproducibility.Grain size 5um, aperture 300A, specific surface area 50m2/g。
Resin anion (R.A.) column is strong-base anion-exchange resin, styrene/divinylbenzene copolymer chlorion type ratio 1.04 to 1.10 are weighed, single-size, (chlorine type) containing wet ratio 45 to 55%.
As a preferred solution, described (4) step includes the following steps:
(4.1) step:Dose volume score is 3%-7% acidity alcohol solutions;Acid is hydrogen chloride, and alcohol is ethyl alcohol;
(4.2) step:Measure the sodium hydroxide solution that dose volume score is 2%-6%;
(4.3) step:By the acidity alcohol solution upper prop, by column group series system followed by each column;When acid alcohol is molten After liquid is all added, pure water is sequentially added, keeps identical flow velocity, acid alcohol is all replaced, until column group end efflux PH When=0.67-7, stop into pure water;
(4.4) step:D101 macroporous resin columns, the first cationic resin column and the second cationic resin column are closed, is opened Resin anion (R.A.) column;Sodium hydroxide addition resin anion (R.A.) column is allowed to make the transition;After whole lye are into column, replaced using pure water Lye in column, until column bottom efflux PH=6.5~7 are stopped;
(4.5) step:According to column group series sequence, the ethyl alcohol for being 80%-95% with volume fraction is followed by the first sun Ion exchange resin column, resin anion (R.A.) column and the second cationic resin column, dosage 4-8BV close column group.
As a preferred solution, in (4.3) step, flow velocity of the acidity alcohol solution in column is 0.5-1.5BV/ h;In (4.4) step, flow velocity of the lye in column is 0.5-1.5BV/h;In (4.5) step, volume fraction 80%- Flow velocity of 95% ethyl alcohol in each column is 1.5-2.5BV/h.
As a preferred solution, described (4) step further includes (4.6) step:Remaining saponin(e in reclaiming liquid, The acidity alcohol solution flowed out in (4.3) step and the lye flowed out in (4.4) step are neutralized, ethyl alcohol is recycled, remaining solid dries Dry, cycle applications are in (2) step.
As a preferred solution, in (3) step, flow velocity of the filtrate in resin column is 1.5-2.5BV/h; The filtrate treating capacity of the resin column is 25~30BV;The dosage for desorbing the ethyl alcohol of absorption saponin(e in resin column is 3-7BV, flow velocity For 1.5-2.5BV/h.
As a preferred solution, the volume fraction of the ethyl alcohol employed in (2) step and (3) step is 60-85%.
As a preferred solution, described (2) step includes the following steps:
(2.1) step:Gynostemma pentaphyllum powder is packed into pot for solvent extraction, the ethyl alcohol that volume fraction is 60-85%, dipping is added;Leaching After 4-8 hours sufficient, liquid is discharged, filters, obtains liquid;The ethyl alcohol that volume fraction is 60-85%, leaching is added in second time dipping Stain 3-7 hours, filtering, obtains liquid;Merge secondary liquid, it is spare;
(2.2) step:It is separately added into the ethyl alcohol that volume fraction is 60-85% and carries out third time and the 4th time dipping, respectively Dipping 3-7 hours;Liquid merges after coarse filtration, and cycle applications are in (2) step;
(2.3) step:The residual ethanol in the dregs of a decoction is recycled, the dregs of a decoction (B powder) are continued to employ.The B powder is:Except gynostemma pentaphyllum total The part mucopolysaccharide and cellulose of indissolubility outside glucoside, trace element and the cellulose absorption influenced by isothermal compressibility Substance.
As a preferred solution, in (1) step, the particle size of the gynostemma pentaphyllum powder is 2-10 mesh.
The invention has the advantages that:
The present invention provides a kind of convenient, system, the method for integrated extraction Gypenosides, this method has medicinal material The separation engagement process of the difference free of discontinuities of saponin(e recycling is remained in pre-treatment, extraction, column chromatography, resin regeneration, regenerated liquid, point From efficient, separation process is stable, is convenient for Quality Control, the gynostemma pentaphyllum total of destination number can be obtained by the control of portion link Glucoside.
The present invention is using currently advanced reverse resin regeneration, extractive technique.Conventional method is spent ion exchange resin It goes to adsorb useless ingredient, useful ingredient is obtained in distillate.And the present invention is useful using ion exchange resin absorption The ingredient Gypenosides of liposoluble ingredient (water-soluble and), be then rinsed again with ethyl alcohol.
The present invention uses very safe D101 large pore resin absorption columns in biological medicine, sulfonic group cation exchange column and strong Alkalescence anion-exchange resin will not cause Gypenosides to be denaturalized, and very short time is by Gypenosides and other compositions Separation, substantially increases the purity of Gypenosides, reduces loss late.
Present invention employs classification to extract processing method, the full product utilization of overall process.Form A powder, water-soluble and liposoluble at The Gypenosides divided.B powder, the part mucopolysaccharide and cellulose of the indissolubility in addition to Gypenosides, trace element, with And the cellulose adsorbent influenced by isothermal compressibility.Totally 2 kinds of analytical products.
Acid alcohol preparation method, 4% Alkali liquid compounding method are applied in the method for extraction Gypenosides by the present invention.It is first First, the small-molecule substances component such as water soluble, a large amount of saponins of fat solubility, mucopolysaccharide, fat corpuscles, albumen corpusculum contains largely Beneficial.Secondly, in industrializing the compound production for preparing extraction Gypenosides preparation, due to experienced a series of life Production. art process, molecules align character has changed, and becomes to lose activity, so the also property of carrying out brokenly and renaturation technology Afterwards, it just can get and original source, the Gypenosides of biologically active high-purity.The above-mentioned preparation side that the present invention uses Decree Gypenosides keep the pharmaceutical activity of very high degree, make domestic Gypenosides industrialization development, industrialized production at To be possible, while also ensuring the high activity and high-quality of Gypenosides.
Specific implementation mode
The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention..
Embodiment 1
The present invention provides a kind of methods of extraction Gypenosides, and described method includes following steps:
(1) step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;The particle size of the gynostemma pentaphyllum powder is 2-10 mesh.
(2) step:The gynostemma pentaphyllum powder that (1) step obtains is put and is extracted in ethanol, filtrate is obtained;
Described (2) step includes the following steps:
(2.1) step:Gynostemma pentaphyllum powder is packed into pot for solvent extraction, the ethyl alcohol that volume fraction is 80% is added, dipping;Leaching foot 6 After hour, liquid is discharged, filters, obtains liquid;The ethyl alcohol that volume fraction is 80% is added in second time dipping, impregnates 5 hours, Filtering, obtains liquid;Merge secondary liquid, it is spare;
(2.2) step:It is separately added into the ethyl alcohol that volume fraction is 80% and carries out third time and the 4th time dipping, impregnate respectively 5 hours;Liquid merges after coarse filtration, and cycle applications are in (2) step;
(2.3) step:The residual ethanol in the dregs of a decoction is recycled, the dregs of a decoction (B powder) are continued to employ.The B powder is:Except gynostemma pentaphyllum total The part mucopolysaccharide and cellulose of indissolubility outside glucoside, trace element and the cellulose absorption influenced by isothermal compressibility Substance.
(3) step:The upper resin column of the filtrate is adsorbed, after resin saturation, stops filtrate upper prop;Using ethyl alcohol solution The saponin(e adsorbed in the resin column is inhaled, ethyl alcohol stripping liquid is obtained;The ethyl alcohol stripping liquid is distilled, ethyl alcohol, solid are recycled Drying obtains water-soluble and liposoluble ingredient Gypenosides powder (A powder);Flow velocity of the filtrate in resin column is 2BV/ h;The filtrate treating capacity of the resin column is 27BV;The dosage for desorbing the ethyl alcohol of absorption saponin(e in resin column is 5BV, and flow velocity is 2BV/h。
The resin column is by D101 large pore resin absorption columns, the first cationic resin column, the moon for being sequentially connected in series from top to bottom Ion exchange resin column and the second cationic resin column composition;
The D101 large pore resin absorption columns being sequentially connected in series from top to bottom, the first cationic resin column, resin anion (R.A.) The column volume ratio of column and the second cationic resin column is 1:1:3:1.
First cationic resin column is sulfonic group cation exchange column;The resin anion (R.A.) column be strong basicity the moon from Sub-exchange resin column;Second cationic resin column is sulfonic group cation exchange column.
(4) step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, the resin is made to restore original Composition and performance.
Described (4) step includes the following steps:
(4.1) step:Dose volume score is 5% acidity alcohol solution;Acid is hydrogen chloride, and alcohol is ethyl alcohol;
(4.2) step:Measure the sodium hydroxide solution that dose volume score is 4%;
(4.3) step:By the acidity alcohol solution upper prop, by column group series system followed by each column;When acid alcohol is molten After liquid is all added, pure water is sequentially added, keeps identical flow velocity, acid alcohol is all replaced, until column group end efflux PH When=0.67-7, stop into pure water;Flow velocity of the acidity alcohol solution in column is 1BV/h;
(4.4) step:D101 macroporous resin columns, the first cationic resin column and the second cationic resin column are closed, is opened Resin anion (R.A.) column;Sodium hydroxide addition resin anion (R.A.) column is allowed to make the transition;After whole lye are into column, replaced using pure water Lye in column, until column bottom efflux PH=6.5~7 are stopped;Flow velocity of the lye in column is 1BV/h;
(4.5) step:According to column group series sequence, the ethyl alcohol for being 95% with volume fraction is set followed by the first cation Fat column, resin anion (R.A.) column and the second cationic resin column, dosage 6BV close column group.The ethyl alcohol that volume fraction is 95% is each Flow velocity in column is 2BV/h.
Described (4) step further includes (4.6) step:Remaining saponin(e in reclaiming liquid, by what is flowed out in (4.3) step The lye flowed out in acidity alcohol solution and (4.4) step neutralizes, and recycles ethyl alcohol, remaining solid drying, cycle applications are in (2) Step.
Embodiment 2
The present invention provides a kind of methods of extraction Gypenosides, and described method includes following steps:
(1) step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;The particle size of the gynostemma pentaphyllum powder is 2-10 mesh.
(2) step:The gynostemma pentaphyllum powder that (1) step obtains is put and is extracted in ethanol, filtrate is obtained;
Described (2) step includes the following steps:
(2.1) step:Gynostemma pentaphyllum powder is packed into pot for solvent extraction, the ethyl alcohol that volume fraction is 60% is added, dipping;Leaching foot 4 After hour, liquid is discharged, filters, obtains liquid;The ethyl alcohol that volume fraction is 60% is added in second time dipping, impregnates 3 hours, Filtering, obtains liquid;Merge secondary liquid, it is spare;
(2.2) step:It is separately added into the ethyl alcohol that volume fraction is 60% and carries out third time and the 4th time dipping, impregnate respectively 3 hours;Liquid merges after coarse filtration, and cycle applications are in (2) step;
(2.3) step:The residual ethanol in the dregs of a decoction is recycled, the dregs of a decoction (B powder) are continued to employ.The B powder is:Except gynostemma pentaphyllum total The part mucopolysaccharide and cellulose of indissolubility outside glucoside, trace element and the cellulose absorption influenced by isothermal compressibility Substance.
(3) step:The upper resin column of the filtrate is adsorbed, after resin saturation, stops filtrate upper prop;Using ethyl alcohol solution The saponin(e adsorbed in the resin column is inhaled, ethyl alcohol stripping liquid is obtained;The ethyl alcohol stripping liquid is distilled, ethyl alcohol, solid are recycled Drying obtains water-soluble and liposoluble ingredient Gypenosides powder (A powder);Flow velocity of the filtrate in resin column be 1.5BV/h;The filtrate treating capacity of the resin column is 25BV;The dosage for desorbing the ethyl alcohol of absorption saponin(e in resin column is 3BV, stream Speed is 1.5BV/h.
The resin column is by D101 large pore resin absorption columns, the first cationic resin column, the moon for being sequentially connected in series from top to bottom Ion exchange resin column and the second cationic resin column composition;
The D101 large pore resin absorption columns being sequentially connected in series from top to bottom, the first cationic resin column, resin anion (R.A.) The column volume ratio of column and the second cationic resin column is 1:1:3:1.
First cationic resin column is sulfonic group cation exchange column;The resin anion (R.A.) column be strong basicity the moon from Sub-exchange resin column;Second cationic resin column is sulfonic group cation exchange column.
(4) step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, the resin is made to restore original Composition and performance.
Described (4) step includes the following steps:
(4.1) step:Dose volume score is 3% acidity alcohol solution;Acid is hydrogen chloride, and alcohol is ethyl alcohol;
(4.2) step:Measure the sodium hydroxide solution that dose volume score is 2%;
(4.3) step:By the acidity alcohol solution upper prop, by column group series system followed by each column;When acid alcohol is molten After liquid is all added, pure water is sequentially added, keeps identical flow velocity, acid alcohol is all replaced, until column group end efflux PH When=0.67-7, stop into pure water;Flow velocity of the acidity alcohol solution in column is 0.5BV/h;
(4.4) step:D101 macroporous resin columns, the first cationic resin column and the second cationic resin column are closed, is opened Resin anion (R.A.) column;Sodium hydroxide addition resin anion (R.A.) column is allowed to make the transition;After whole lye are into column, replaced using pure water Lye in column, until column bottom efflux PH=6.5~7 are stopped;Flow velocity of the lye in column is 0.5BV/h;
(4.5) step:According to column group series sequence, the ethyl alcohol for being 80% with volume fraction is set followed by the first cation Fat column, resin anion (R.A.) column and the second cationic resin column, dosage 4BV close column group.The ethyl alcohol that volume fraction is 80% is each Flow velocity in column is 1.5BV/h.
Described (4) step further includes (4.6) step:Remaining saponin(e in reclaiming liquid, by what is flowed out in (4.3) step The lye flowed out in acidity alcohol solution and (4.4) step neutralizes, and recycles ethyl alcohol, remaining solid drying, cycle applications are in (2) Step.
Embodiment 3
The present invention provides a kind of methods of extraction Gypenosides, and described method includes following steps:
(1) step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;The particle size of the gynostemma pentaphyllum powder is 2-10 mesh.
(2) step:The gynostemma pentaphyllum powder that (1) step obtains is put and is extracted in ethanol, filtrate is obtained;
Described (2) step includes the following steps:
(2.1) step:Gynostemma pentaphyllum powder is packed into pot for solvent extraction, the ethyl alcohol that volume fraction is 85% is added, dipping;Leaching foot 8 After hour, liquid is discharged, filters, obtains liquid;The ethyl alcohol that volume fraction is 85% is added in second time dipping, impregnates 7 hours, Filtering, obtains liquid;Merge secondary liquid, it is spare;
(2.2) step:It is separately added into the ethyl alcohol that volume fraction is 85% and carries out third time and the 4th time dipping, impregnate respectively 7 hours;Liquid merges after coarse filtration, and cycle applications are in (2) step;
(2.3) step:The residual ethanol in the dregs of a decoction is recycled, the dregs of a decoction (B powder) are continued to employ.The B powder is:Except gynostemma pentaphyllum total The part mucopolysaccharide and cellulose of indissolubility outside glucoside, trace element and the cellulose absorption influenced by isothermal compressibility Substance.
(3) step:The upper resin column of the filtrate is adsorbed, after resin saturation, stops filtrate upper prop;Using ethyl alcohol solution The saponin(e adsorbed in the resin column is inhaled, ethyl alcohol stripping liquid is obtained;The ethyl alcohol stripping liquid is distilled, ethyl alcohol, solid are recycled Drying obtains water-soluble and liposoluble ingredient Gypenosides powder (A powder);Flow velocity of the filtrate in resin column be 2.5BV/h;The filtrate treating capacity of the resin column is 30BV;The dosage for desorbing the ethyl alcohol of absorption saponin(e in resin column is 7BV, stream Speed is 2.5BV/h.
The resin column is by D101 large pore resin absorption columns, the first cationic resin column, the moon for being sequentially connected in series from top to bottom Ion exchange resin column and the second cationic resin column composition;
The D101 large pore resin absorption columns being sequentially connected in series from top to bottom, the first cationic resin column, resin anion (R.A.) The column volume ratio of column and the second cationic resin column is 1:1:3:1.
First cationic resin column is sulfonic group cation exchange column;The resin anion (R.A.) column be strong basicity the moon from Sub-exchange resin column;Second cationic resin column is sulfonic group cation exchange column.
(4) step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, the resin is made to restore original Composition and performance.
Described (4) step includes the following steps:
(4.1) step:Dose volume score is 7% acidity alcohol solution;Acid is hydrogen chloride, and alcohol is ethyl alcohol;
(4.2) step:Measure the sodium hydroxide solution that dose volume score is 6%;
(4.3) step:By the acidity alcohol solution upper prop, by column group series system followed by each column;When acid alcohol is molten After liquid is all added, pure water is sequentially added, keeps identical flow velocity, acid alcohol is all replaced, until column group end efflux PH When=0.67-7, stop into pure water;Flow velocity of the acidity alcohol solution in column is 1.5BV/h;
(4.4) step:D101 macroporous resin columns, the first cationic resin column and the second cationic resin column are closed, is opened Resin anion (R.A.) column;Sodium hydroxide addition resin anion (R.A.) column is allowed to make the transition;After whole lye are into column, replaced using pure water Lye in column, until column bottom efflux PH=6.5~7 are stopped;Flow velocity of the lye in column is 1.5BV/h;
(4.5) step:According to column group series sequence, the ethyl alcohol for being 95% with volume fraction is set followed by the first cation Fat column, resin anion (R.A.) column and the second cationic resin column, dosage 8BV close column group.The ethyl alcohol that volume fraction is 95% is each Flow velocity in column is 2.5BV/h.
Described (4) step further includes (4.6) step:Remaining saponin(e in reclaiming liquid, by what is flowed out in (4.3) step The lye flowed out in acidity alcohol solution and (4.4) step neutralizes, and recycles ethyl alcohol, remaining solid drying, cycle applications are in (2) Step.
Although above having used general explanation and specific embodiment, the present invention is described in detail, at this On the basis of invention, it can be made some modifications or improvements, this will be apparent to those skilled in the art.Therefore, These modifications or improvements without departing from theon the basis of the spirit of the present invention belong to the scope of protection of present invention.

Claims (9)

1. a kind of method of extraction Gypenosides, which is characterized in that described method includes following steps:
(1) step:Gynostemma pentaphyllum is crushed, gynostemma pentaphyllum powder is obtained;
(2) step:The gynostemma pentaphyllum powder that (1) step obtains is put and is extracted in ethanol, filtrate is obtained;
(3) step:The upper resin column of the filtrate is adsorbed, after resin saturation, stops filtrate upper prop;Institute is desorbed using ethyl alcohol The saponin(e adsorbed in resin column is stated, ethyl alcohol stripping liquid is obtained;The ethyl alcohol stripping liquid is distilled, ethyl alcohol is recycled, solid is dried, Obtain water-soluble and liposoluble ingredient Gypenosides powder;
The resin column is by the D101 large pore resin absorption columns, the first cationic resin column, the anion that are sequentially connected in series from top to bottom Resin column and the second cationic resin column composition;
(4) step:It is removed using the Impurity elution that resin regeneration solution is adsorbed resin, the resin is made to restore original group At and performance.
2. the method for extraction Gypenosides according to claim 1, which is characterized in that described to be sequentially connected in series from top to bottom D101 large pore resin absorption columns, the first cationic resin column, resin anion (R.A.) column and the second cationic resin column column volume Ratio is 1:1:3:1.
3. the method for extraction Gypenosides according to claim 1, which is characterized in that first cationic resin column For sulfonic group cation exchange column;The resin anion (R.A.) column is strong-base anion-exchange resin column;Second cation Resin column is sulfonic group cation exchange column.
4. the method for extraction Gypenosides according to claim 1, which is characterized in that described (4) step includes as follows Step:
(4.1) step:Dose volume score is 3%-7% acidity alcohol solutions;
(4.2) step:Measure the sodium hydroxide solution that dose volume score is 2%-6%;
(4.3) step:By the acidity alcohol solution upper prop, by column group series system followed by each column;When acidity alcohol solution is complete After portion is added, pure water is sequentially added, keeps identical flow velocity, acid alcohol is all replaced, until column group end efflux PH= When 0.67-7, stop into pure water;
(4.4) step:Close D101 macroporous resin columns, the first cationic resin column and the second cationic resin column, open it is cloudy from Sub- resin column;Sodium hydroxide addition resin anion (R.A.) column is allowed to make the transition;After whole lye are into column, using in pure water column precipitator Lye, until column bottom efflux PH=6.5~7 are stopped;
(4.5) step:According to column group series sequence, the ethyl alcohol for being 80%-95% with volume fraction is followed by the first cation Resin column, resin anion (R.A.) column and the second cationic resin column, dosage 4-8BV close column group.
5. the method for extraction Gypenosides according to claim 4, which is characterized in that in (4.3) step, the acidity Flow velocity of the alcoholic solution in column is 0.5-1.5BV/h;In (4.4) step, flow velocity of the lye in column is 0.5-1.5BV/ h;In (4.5) step, the flow velocity of ethyl alcohol that volume fraction is 80%-95% in each column is 1.5-2.5BV/h.
6. the method for extraction Gypenosides according to claim 4, which is characterized in that described (4) step further includes the (4.6) step:The acidity alcohol solution flowed out in (4.3) step and the lye flowed out in (4.4) step are neutralized, ethyl alcohol is recycled, is remained Remaining solid drying, cycle applications are in (2) step.
7. the method for extraction Gypenosides according to claim 1, which is characterized in that in (3) step, the filtrate Flow velocity in resin column is 1.5-2.5BV/h;The filtrate treating capacity of the resin column is 25~30BV;Desorb resin column interior suction The dosage of the ethyl alcohol of attached saponin(e is 3-7BV, flow velocity 1.5-2.5BV/h.
8. the method for extraction Gypenosides according to claim 1, which is characterized in that
Described (2) step includes the following steps:
(2.1) step:Gynostemma pentaphyllum powder is packed into pot for solvent extraction, the ethyl alcohol that volume fraction is 60-85%, dipping is added;Soak foot 4-8 After hour, liquid is discharged, filters, obtains liquid;The ethyl alcohol that volume fraction is 60-85% is added in second time dipping, impregnates 3-7 Hour, filtering obtains liquid;Merge secondary liquid, it is spare;
(2.2) step:It is separately added into the ethyl alcohol that volume fraction is 60-85% and carries out third time and the 4th time dipping, impregnate respectively 3-7 hours;Liquid merges after coarse filtration, and cycle applications are in (2) step;
(2.3) step:The residual ethanol in the dregs of a decoction is recycled, the dregs of a decoction are continued to employ.
9. the method for extraction Gypenosides according to claim 1, which is characterized in that institute in (2) step and (3) step The volume fraction of the ethyl alcohol used is 60-85%.
CN201810458420.2A 2018-05-14 2018-05-14 A method of extraction Gypenosides Pending CN108310039A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810458420.2A CN108310039A (en) 2018-05-14 2018-05-14 A method of extraction Gypenosides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810458420.2A CN108310039A (en) 2018-05-14 2018-05-14 A method of extraction Gypenosides

Publications (1)

Publication Number Publication Date
CN108310039A true CN108310039A (en) 2018-07-24

Family

ID=62895906

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810458420.2A Pending CN108310039A (en) 2018-05-14 2018-05-14 A method of extraction Gypenosides

Country Status (1)

Country Link
CN (1) CN108310039A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103520256A (en) * 2013-10-15 2014-01-22 曹远东 Preparation method of high-purity gynostemma pentaphylla total saponin for veterinary drug
CN104774238A (en) * 2015-04-03 2015-07-15 泉州市奈斯材料科技有限公司 Method for refining soapnut saponin by using ion exchange resin method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103520256A (en) * 2013-10-15 2014-01-22 曹远东 Preparation method of high-purity gynostemma pentaphylla total saponin for veterinary drug
CN104774238A (en) * 2015-04-03 2015-07-15 泉州市奈斯材料科技有限公司 Method for refining soapnut saponin by using ion exchange resin method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
孔玉琼等: "绞股蓝总皂苷中单体皂苷的分离纯化", 《大连工业大学学报》 *

Similar Documents

Publication Publication Date Title
CN102552396B (en) Salvia miltiorrhiza Bunge var alba total phenolic acid extract, preparation method and application
CN1459448A (en) Preparation method of red sageroot total phenolic acid and its use
CN102895294B (en) Astragalus mongholicus injection and preparation method thereof
CN100500196C (en) Method for preparing paris polyphylla total saponin
CN104804060A (en) Preparing method of sodium aescinate, external use preparation comprising same and application thereof
WO2018133563A1 (en) Panax plant extract and pharmaceutical composition and use thereof
CN105294811A (en) Method for preparing ganoderma lucidum karst triterpenic acid and ganoderma lucidum karst polysaccharide with Nyingchi ganoderma lucidum karst as material
CN107412430A (en) A kind of radix scrophulariae water extract and its application
CN101283999B (en) Medicinal composition mainly for curing cardiovascular and cerebrovascular diseases and preparation method thereof
CN101006984B (en) An injection preparation containing salvianolic acid A and extract of panax natoginseng, and its preparation method and application
CN100384429C (en) Capsule for treating cardiac and cerebral vascular diseases and its preparing method and application
CN101597314B (en) Preparation method of ginsenoside Rg1
CN107095893B (en) Extraction method and application of active substances of panax pseudoginseng
CN108310039A (en) A method of extraction Gypenosides
CN101190906B (en) Method for preparing carthamin yellow carthamus B and application thereof
CN101292987B (en) Pharmaceutical combination
CN101647858B (en) Preparation method of water-soluble extract of red sage root
CN101293009A (en) Pharmaceutical composition
CN108403750A (en) A method of extraction Gypenosides
CN100584345C (en) Distillage of Ardisia chinensis Benth of possessing function of antivirus, extraction method and application
CN103919759B (en) A kind of containing danshensu sodium, the pharmaceutical composition of salvia miltiorrhiza tanshinoate F and preparation thereof
CN102716231B (en) A kind of Chinese medicine composition and application thereof for the treatment of brain injury and cerebral edema
CN104352529A (en) Preparation and detection methods of anti-liver fibrosis active cockroach extract
CN102086223B (en) Method for preparing ginsenoside Rg1
WO2023125719A1 (en) Veronica undulata extract as well as preparation method therefor and use thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20180724