CN108452006A - A kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol - Google Patents

A kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol Download PDF

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CN108452006A
CN108452006A CN201810373260.1A CN201810373260A CN108452006A CN 108452006 A CN108452006 A CN 108452006A CN 201810373260 A CN201810373260 A CN 201810373260A CN 108452006 A CN108452006 A CN 108452006A
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章志成
袁玲
姚俊
孔庆娜
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Taizhou University
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    • 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)
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    • 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
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    • A61K2236/50Methods involving additional extraction steps
    • A61K2236/53Liquid-solid separation, e.g. centrifugation, sedimentation or crystallization
    • 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

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Abstract

The invention discloses a kind of methods that impulse electric field aqueous two-phase column chromatography combines extraction plant polyphenol, include the following steps:(1) plant to be extracted is carried out pre-processing to obtain material liquid;(2) using ethyl alcohol as solvent, the active material in material liquid is extracted using impulse electric field, obtains extracting solution;(3) plant polyphenol crude extract is obtained using the active constituent in aqueous two-phase extraction extracting solution after extracting solution filtering;(4) plant polyphenol crude extract revolving purifies active material in extract using column chromatography after removing alcohol;(5) it is concentrated and dried up to plant polyphenol product.The present invention is coupled a variety of advanced extracting methods, has extraction efficiency high, the high feature of extraction product purity, overcomes prior art there are technological processes long, complex process, ingredient height and the low problem of yield.

Description

A kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol
Technical field
The invention belongs to field of natural product chemistry, are related to the method for the extracting and developing and purifying of natural products, specifically It is related to a kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol.
Background technology
Plant polyphenol is a kind of polyatomic phenol secondary metabolite being widely present in plant, and type is abundant, packet Include anthocyanin, flavonols, flavones, gallic acid, protocatechuic acid etc..As plant polyphenol constituents are in inhibition of enzyme activity, antioxygen Change, radiation protection, adjusts many-sided active hair such as blood pressure and blood lipoid and raising immunity at anti-inflammatory, antibacterial, antiviral, anti-mutation It now and illustrates, plant polyphenol has increasingly extensive in fields such as agricultural, ecological environment, food additives, biological medicine, cosmetics Application.For plant polyphenol as the natural extract obtained from nature, safety receives liking for people, is referred to as For the 7th class nutrient after the 6th nutrient diet fiber.Plant polyphenol mainly from red bayberry, tealeaves, grape, persimmon, Extraction obtains in the blades of the plants such as apple, fruit, pericarp, fruit stone or pomace.Currently, the extracting method of plant polyphenol is substantially It is divided into two major classes:The straight formulation of solvent and solvent combination other technologies strengthen extraction method.
Solvent directly extracts plant polyphenol method and is divided into ethanol immersion or Hot water extraction, and the required time is longer, phenol Substance oxidation is serious, and extraction efficiency is low, and industrial production cost is high., for example, the China of Publication No. CN 105348331A Application for a patent for invention document discloses a kind of extracting method of plant polyphenol in mangrove bark comprising following steps:The first step, title Take and shred 100 parts by weight mangrove barks, and by the mangrove bark in boiling water blanching 0.5 minute~2.0 minutes;Second step, general Step 1 obtain mangrove bark with 0.2%~1.0% sodium sulfite solution impregnate 0.5~2.0 minute, then be added 0.2%~ 1.0% vitamin c solution;The mangrove bark that step 2 obtains is rinsed with water totally by third step, then according to volume ratio 1:100 ~10:It is broken with beating equipment that ultra-pure water is added in 1 ratio;Absolute ethyl alcohol is added in 4th step, the slurry walked to third, it will Gained mixed liquor is placed in 50 DEG C~70 DEG C;5th step merged the leaching liquor obtained in step 4, then with 5000r/ minutes rates Centrifugation 5 minutes is carried out to it, and supernatant is taken after centrifugation;After drying supernatant, mangrove bark polyphenol extract is made in 6th step.
Extraction efficiency and cost is reduced to improve, needs to carry out assisted extraction using other technologies means, including microwave, The technologies such as ultrasonic wave, super-pressure, overcritical.For example, at number of patent application " CN200510022420.0 ", it is entitled " to plant Technological process disclosed in the active extracting method of object polyphenols " is:Natural material is cleaned, it is dry, crush after and water Extraction chamber is added in mixing, under inert gas protection, is carried using hot dipping or microwave, ultrasonic wave householder method are extracted, through filtering Polyphenols extracting solution is obtained after cooling, and the solids of plant polyphenol is obtained after concentrated drying.Although this method flow It is shorter, but the product purity for obtaining plant polyphenol is not high, limits its scope of application.
Invention content
The present invention provides a kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol, will be a variety of advanced Extracting method coupled, have extraction efficiency high, the high feature of extraction product purity, overcoming prior art, there are works Skill long flow path, complex process, the problem low with yield of high cost.
A kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol, includes the following steps:
(1) plant to be extracted is carried out pre-processing to obtain material liquid;
(2) using ethyl alcohol as solvent, the active material in material liquid is extracted using impulse electric field, obtains extracting solution;
(3) plant polyphenol crude extract is obtained using the active constituent in aqueous two-phase extraction extracting solution after extracting solution filtering;
(4) plant polyphenol crude extract revolving purifies active material in extract using column chromatography after removing alcohol;
(5) it is concentrated and dried up to plant polyphenol product.
Aqueous two-phase system (Aqueous Two-phase Extraction) is using substance in two immiscible water phases Between distribution coefficient the method that is extracted of difference, the distribution coefficient by changing solute reaches the mesh for increasing extraction efficiency , have water content high, interfacial tension is small, there is no organic solvent residual and is easy to the advantages of engineering is amplified.
Impulse electric field has under the application scenarios of natural product extraction and microwave, the similar physical effect of ultrasound, thus Impulse electric field is combined by this project with aqueous two-phase extraction, for extracting the polyphenol substance in Waxberry fruit.Hydrophily low molecule Organic solvent-inorganic salts double-aqueous phase system (alcohol/salt system) has the stronger active ingredient of polarity in natural products good Extracting power can obtain higher distribution coefficient and the rate of recovery by the optimization to two phase aqueous extraction system.
The substance of higher degree in order to obtain needs further to purify polyphenol extract, polyphenols point Mainly there are column chromatography, molecular distillation technique, preparative high performance liquid chromatography and high-speed countercurrent chromatography etc. from purification process. Wherein, column chromatography has simple for process, and production cost is low, is easy to industrialized feature.
The present invention organically combines three kinds of technologies, mutually cooperates with, mutually promotes between each technical advantage, common to improve extraction Efficiency and product purity.
Preferably, the plant to be extracted is red bayberry or blue or green money willow.
Red bayberry (Myrica.rubra Sieb.et Zucc.) belongs to Myruca ceas red bayberry spp.ing plant, and fruit colour is bright-coloured, juice More, sweet and sour taste, nutritive value is very high, therefore is favored deeply by consumers in general, but the red bayberry maturity period is short, has focused largely on 6 The middle ten days and the last ten days moon, positive value rainy season in midsummer, listing this moment was concentrated, and storage tolerance does not transport for pole to early and middle ten days in July.In waxberry flesh Polyphenol substance rich content, thus can be considered and extract bayberry polyphenol from waxberry flesh, it is used for food antioxidant or biology Medicine.Blue or green money willow (Cylocayapalirus) also known as money tree are Juglandaceae cyclocarya plant, are collection material, greening, tea Drink health care, the rare tree species of medicinal treatment.Rich in a variety of plants such as camellia phenol, Quercetin and isoflavone aglycones in Qingqian Willow leaf Object polyphenol has hypoglycemic, reducing blood lipid, blood pressure lowering, anti-aging, antitumor action, is led in recent years in biological medicine and health care of food Domain receives increasingly extensive concern.
It is further preferred that when the plant to be extracted is red bayberry, preprocess method is:Clear water uses fruit and vegetable pulping after cleaning Machine stoning mashing, it is 70% ethanol solution that volumetric concentration, which is then added, red bayberry juice suspension is prepared into after stirring evenly, and adopt Make red bayberry juice suspension in acid up to material liquid with dilute hydrochloric acid.
It is further preferred that when the plant to be extracted is blue or green money willow, preprocess method is:Blue or green money willow cured leaf is gone to obstruct, 5~6h is dried in 60~70 DEG C of electric heating constant-temperature blowing drying box, is then crushed with micronizer, is disperseed after crossing 80 mesh sieve In the ethyl alcohol that volumetric concentration is 70%, turbid is configured to up to material liquid.
The dosage of ethyl alcohol is dispersed in 250mL ethyl alcohol with powder made of every 20g blue or green money willows cured leaf and falls into a trap.
Further, it pre-processes and is:Blue or green money willow cured leaf is gone to obstruct, is dried in 65 DEG C of electric heating constant-temperature blowing drying box Then 6h is crushed with micronizer, be dispersed in the ethyl alcohol that volumetric concentration is 70% after crossing 80 mesh sieve, be configured to turbid.
Preferably, impulse electric field extraction conditions are in step (2):Material liquid is gone into impulse electric field and extracts chamber, adjusts electricity Interpolar uses Bipolar pulse power or square-wave pulse power source away from 4~5mm, discharge power supply, and adjusting voltage makes electric field strength reach 20~30kV/cm, stopping processing after discharging 20~30 times, extracts 3~5min of total residence time in chamber, will be suspended after electric discharge Liquid removes extraction chamber, and double-layer filter cloth is used in combination to filter, and retains filtrate, that is, extracting solution.
It is further preferred that impulse electric field extraction conditions are in step (2):Material liquid is gone into impulse electric field and extracts chamber, Electrode spacing 5mm is adjusted, discharge power supply uses Bipolar pulse power or square-wave pulse power source, and adjusting voltage makes electric field strength reach To 25kV/cm, total residence time 5min in chamber is extracted in stopping processing after discharging 30 times, proposes suspension removal after electric discharge Chamber is taken, double-layer filter cloth is used in combination to filter, retains filtrate, that is, extracting solution.
Preferably, aqueous two-phase extraction condition is in step (3):
It is added the ethyl alcohol and ammonium sulfate of volumetric concentration 80% into extracting solution, lasting stirring while dilute hydrochloric acid is added dropwise to pH is 2.5~3.5, it is stood after stirring evenly, phase alcohol liquid i.e. plant polyphenol crude extract is taken after layering.
It is further preferred that amount of alcohol added and the volume ratio of extracting solution are 1:1~1:3;Ammonium sulfate is added quality and carries It is 0.2g/mL~0.4g/mL to take the volume ratio of liquid.
It is further preferred that (1 is added into extracting solution:1) ethyl alcohol of volumetric concentration 80% and ammonium sulfate (0.3g/mL Extracting solution), it is 3 persistently to stir while dilute hydrochloric acid is added dropwise to pH, and 30min is stood after stirring evenly, phase alcohol liquid is taken after layering i.e. Plant polyphenol crude extract.
Preferably, step (4) center pillar chromatography condition is:By revolving except the dilution after alcohol is in the rate of 2~3mL/min Then column uses the degassed ethanol aqueous solution of volumetric concentration 80% to elute, collects eluent.
It is further preferred that the resin in chromatographic column is pre-processed through following method:Take AB-8 Polar Adsorbent Resins, use anhydrous Ethyl alcohol or volume fraction 90% with 10~20h of pure immersion, then cleaned with deionized water, until eluate clarification and without ethyl alcohol Taste, then use NaOH aqueous solutions, deionized water and acetum to elute pillar successively, finally use distilled water flushing pillar to neutrality.
Preferably, dry using spray drying.
The present invention also provides a kind of plant polyphenols extracted such as the extracting method.
Compared with prior art, the present invention has the advantages that:
Impulse electric field extractive technique is that fluid substance applies high pressure-burst pulse repeatedly between high and low pressure electrode, to raw material Cell wall and cell membrane generate the effects such as electric polarization, electrical breakdown and electroporation, change membrane passage, form active ingredient Channel is dissolved out, while extra electric field enhances the solvability of solvent and the dissolution rate of polar molecule in raw material, formd fast Speed, it is continuous, room temperature, efficiently strengthen extraction effect, have the characteristics that extraction efficiency height, low energy consumption, the time is short, selectivity is strong.
Description of the drawings
Fig. 1 is the extraction process flow chart of bayberry polyphenol.
Fig. 2 is the extraction process flow chart of Qingqian Willow leaf polyphenol.
Specific implementation mode
The technical scheme in the embodiments of the invention will be clearly and completely described below, protection scope of the present invention It should not be limited by the examples, protection scope of the present invention is determined by claims.Based on the embodiments of the present invention, this field The every other embodiment that those of ordinary skill is obtained without creative efforts, belongs to protection of the present invention Range.
Embodiment 1:Bayberry polyphenol is extracted from waxberry flesh using the technique
Red bayberry (Myrica.rubra Sieb.et Zucc.) belongs to Myruca ceas red bayberry spp.ing plant, and fruit colour is bright-coloured, juice More, sweet and sour taste, nutritive value is very high, therefore is favored deeply by consumers in general, but the red bayberry maturity period is short, has focused largely on 6 The middle ten days and the last ten days moon, positive value rainy season in midsummer, listing this moment was concentrated, and storage tolerance does not transport for pole to early and middle ten days in July.In waxberry flesh Polyphenol substance rich content, thus can be considered and extract bayberry polyphenol from waxberry flesh, it is used for food antioxidant or biology Medicine.In conjunction with attached drawing 1, the processing step of bayberry polyphenol extraction is illustrated:
(1) pretreatment of raw material.250g red bayberries are taken to freeze fruit, 5 DEG C of defrostings in refrigerator, clear water is gone after cleaning with fruit and vegetable pulping machine Core is beaten, and 1L70% ethanol solutions are then added, red bayberry juice suspension are prepared into after stirring evenly, and the dilute salt of 4-5 drops is added Acid makes solution in acidity.
(2) bayberry polyphenol in impulse electric field extraction fruit juice.Red bayberry fruit suspension is transferred to impulse electric field and extracts chamber, is adjusted Electrode spacing 5mm is saved, discharge power supply uses Bipolar pulse power, and adjusting voltage makes electric field strength reach 25kV/cm, electric discharge 30 Secondary (each 15 of positive negative pulse stuffing) stopping is handled afterwards, extracts total residence time 5min in chamber.Suspension removal is carried after electric discharge Chamber is taken, double-layer filter cloth is used in combination to filter, retains filtrate.
(3) bayberry polyphenol in alcohol/salt double-aqueous phase system extraction extracting solution.The filtrate of collection is transferred to the large beaker of 3L In, the ethyl alcohol and 360g ammonium sulfate (ammonium sulfate concentrations are about 0.4g/mL) of 50mL 80% is then added, uninterruptedly uses blender Stirring, and dilute hydrochloric acid is added dropwise into solution, it is 3 or so to adjust pH value of solution, stands 30 minutes after stirring evenly, solution divides Layer.Wherein, bayberry polyphenol is enriched in phase alcohol liquid.
(4) column chromatography further purifies bayberry polyphenol.1. the upper phase alcoholic solution that will be enriched in bayberry polyphenol is transferred to Distilling flask volatilizes ethyl alcohol in 60 DEG C of water-bath, and 2L is diluted to the pH water for being 3 or so.2. resin pre-processes.Take the poles AB-8 Property absorption resin 150g then cleaned with deionized water with soaked in absolute ethyl alcohol 10h, until eluate clarification and without ethanol flavor, then NaOH aqueous solutions, deionized water and acetum is used to elute pillar, finally use distilled water flushing pillar to neutrality successively.3. column layer Analysis, will be enriched in the thin liquid of bayberry polyphenol, with the rate upper prop of 2.5mL/min, then be eluted with 80% degassed ethanol aqueous solution, Collect eluent.
(5) it is concentrated and dried.After being concentrated to eluent, using spray drying, bayberry polyphenol finished product is made.Through liquid chromatogram point Analysis, bayberry polyphenol is mainly cyanidin, myricetin deoxidation hexose glycosides and quercetin 3-O- glucosides etc., bayberry polyphenol Yield be 21.13mg/g.
Embodiment 2:Blue or green money willow phenol is extracted from Qingqian Willow leaf using the technique
Blue or green money willow (Cylocayapalirus) also known as money tree, be Juglandaceae cyclocarya plant, be collection material, greening, Tea-drinking health care, the rare tree species of medicinal treatment.It is organic rich in various actives such as flavones, polysaccharide, sterols in Qingqian Willow leaf Ingredient has hypoglycemic, reducing blood lipid, blood pressure lowering, anti-aging, antitumor action, in recent years in biological medicine and field of food health care Receive increasingly extensive concern.Using technological process as shown in Figure 2, polyphenols is extracted from Qingqian Willow leaf.
(1) pretreatment of raw material.20g blue or green money willow cured leafs are taken, go to obstruct, are dried in 65 DEG C of electric heating constant-temperature blowing drying box Then 6h is crushed with micronizer, cross 80 mesh sieve.Then the ethyl alcohol that 250mL volumetric concentrations are 70% is added, is configured to turbid Liquid.
(2) polyphenol substance in impulse electric field extraction Qingqian Willow leaf.Qingqian Willow leaf powder turbid is transferred to impulse electric field Chamber is extracted, electrode spacing 4mm is adjusted, discharge power supply uses square-wave pulse power source, and adjusting voltage makes electric field strength reach 20kV/ Cm, stopping processing after discharging 25 times, extracts total residence time 4min in chamber.Suspension is removed into extraction chamber after electric discharge, and It is filtered with double-layer filter cloth, retains filtrate.
(3) the Qingqian Willow leaf polyphenol in alcohol/salt double-aqueous phase system extraction extracting solution.The filtrate of collection is transferred to the big of 1L In beaker, the ethyl alcohol and 62g ammonium sulfate of 25mL 70% is then added, is uninterruptedly stirred with blender, and is added dropwise into solution dilute Hydrochloric acid, it is 3 or so to adjust pH value of solution, stands 30 minutes after stirring evenly, solution is layered.Wherein, Qingqian Willow leaf polyphenol is rich Collection is in upper phase alcohol liquid.
(4) column chromatography further purifies Qingqian Willow leaf polyphenol.1. the upper phase alcohol that will be enriched in Qingqian Willow leaf polyphenol is molten Liquid is transferred to distilling flask, and ethyl alcohol is volatilized in 60 DEG C of water-bath, and 500mL is diluted to the pH water for being 3 or so.2. resin is located in advance Reason.AB-8 Polar Adsorbent Resin 50g are taken, is that 90% ethyl alcohol impregnates 20h with volume fraction, is then cleaned with deionized water, until washing Go out liquid clarification and without ethanol flavor, then use NaOH aqueous solutions successively, deionized water and acetum elute pillar, finally use distilled water Pillar is rinsed to neutrality.3. column chromatography will be enriched in the thin liquid of bayberry polyphenol, with the rate upper prop of 2.0mL/min, then with 80% Ethanol water elution, collect eluent.
(5) it is concentrated and dried.After being concentrated to eluent, using spray drying, Qingqian Willow leaf polyphenol finished product is made.Through liquid phase color Spectrum analysis, Qingqian Willow leaf polyphenol are mainly the Flavonoid substances such as isoflavone aglycone, camellia phenol and Quercetin, and Qingqian Willow leaf polyphenol obtains Rate is 102.03mg/g.

Claims (10)

1. a kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol, which is characterized in that including walking as follows Suddenly:
(1) plant to be extracted is pre-processed, obtains material liquid;
(2) using ethyl alcohol as solvent, the active material in material liquid is extracted using impulse electric field, obtains extracting solution;
(3) plant polyphenol crude extract is obtained using the active constituent in aqueous two-phase extraction extracting solution after extracting solution filtering;
(4) plant polyphenol crude extract revolving purifies active material in extract using column chromatography after removing alcohol;
(5) it is concentrated and dried up to plant polyphenol product.
2. method according to claim 1, which is characterized in that the plant to be extracted is red bayberry or blue or green money willow.
3. method according to claim 2, which is characterized in that when the plant to be extracted is red bayberry, preprocess method is:Clearly Water is beaten after cleaning with the stoning of fruit and vegetable pulping machine, and it is 70% ethanol solution that volumetric concentration, which is then added, is prepared into after stirring evenly Red bayberry juice suspension, and make red bayberry juice suspension in acid up to material liquid using dilute hydrochloric acid.
4. method according to claim 2, which is characterized in that when the plant to be extracted is blue or green money willow, preprocess method is: Blue or green money willow cured leaf is gone to obstruct, 5~6h is dried in 60~70 DEG C of electric heating constant-temperature blowing drying box, then uses micronizer powder It is broken, it is dispersed in the ethyl alcohol that volumetric concentration is 70% after crossing 80 mesh sieve, is configured to turbid up to material liquid.
5. method according to claim 1, which is characterized in that impulse electric field extraction conditions are in step (2):Material liquid is turned Chamber is extracted to impulse electric field, adjusts 4~5mm of electrode spacing, discharge power supply uses Bipolar pulse power or square-wave pulse power source, Adjusting voltage makes electric field strength reach 20~30kV/cm, and total residence time 3 in chamber is extracted in stopping processing after discharging 20~30 times Suspension is removed extraction chamber after electric discharge, double-layer filter cloth is used in combination to filter, retains filtrate, that is, extracting solution by~5min.
6. method according to claim 1, which is characterized in that aqueous two-phase extraction condition is in step (3):
Be added the ethyl alcohol and ammonium sulfate of volumetric concentration 80% into extracting solution, lasting stirring be added dropwise simultaneously dilute hydrochloric acid to pH be 2.5 ~3.5, it is stood after stirring evenly, phase alcohol liquid i.e. plant polyphenol crude extract is taken after layering.
7. method according to claim 6, which is characterized in that amount of alcohol added and the volume ratio of extracting solution are 1:1~1:3; It is 0.2g/mL~0.4g/mL that quality and the volume ratio of extracting solution, which is added, in ammonium sulfate.
8. method according to claim 1, which is characterized in that step (4) center pillar chromatography condition is:By revolving except dilute after alcohol Liquid is released with the rate upper prop of 2~3mL/min, then uses the degassed ethanol aqueous solution of volumetric concentration 80% to elute, collects eluent.
9. method according to claim 8, which is characterized in that the resin in chromatographic column is pre-processed through following method:Take AB-8 Then Polar Adsorbent Resin is cleaned with absolute ethyl alcohol or volume fraction 90% and 10~20h of pure immersion with deionized water, until Eluate is clarified and without ethanol flavor, then uses NaOH aqueous solutions, deionized water and acetum to elute pillar successively, finally with distillation Water rinses pillar to neutrality.
10. method according to claim 1, which is characterized in that dry using spray drying.
CN201810373260.1A 2018-06-01 2018-06-01 A kind of method of impulse electric field-aqueous two-phase-column chromatography combination extraction plant polyphenol Pending CN108452006A (en)

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