CN102086465B - Method for preparing polypeptide active substance from enzymolysis ginkgo protein - Google Patents

Method for preparing polypeptide active substance from enzymolysis ginkgo protein Download PDF

Info

Publication number
CN102086465B
CN102086465B CN2010101120962A CN201010112096A CN102086465B CN 102086465 B CN102086465 B CN 102086465B CN 2010101120962 A CN2010101120962 A CN 2010101120962A CN 201010112096 A CN201010112096 A CN 201010112096A CN 102086465 B CN102086465 B CN 102086465B
Authority
CN
China
Prior art keywords
polypeptide
content
ginkgo
enzymolysis
powder
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.)
Active
Application number
CN2010101120962A
Other languages
Chinese (zh)
Other versions
CN102086465A (en
Inventor
王成章
陈西娟
叶建中
陈虹霞
马维新
周彬
程耀波
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.)
Chengdu Yishenrui Technology Co ltd
Jiangsu Hengtian Biotechnology Co ltd
Shanghai Di Wan Electronic Technology Co ltd
Institute of Chemical Industry of Forest Products of CAF
Original Assignee
PIZHOU XINYUAN BIOLOGICAL PRODUCTS CO Ltd
Institute of Chemical Industry of Forest Products of CAF
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 PIZHOU XINYUAN BIOLOGICAL PRODUCTS CO Ltd, Institute of Chemical Industry of Forest Products of CAF filed Critical PIZHOU XINYUAN BIOLOGICAL PRODUCTS CO Ltd
Priority to CN2010101120962A priority Critical patent/CN102086465B/en
Publication of CN102086465A publication Critical patent/CN102086465A/en
Application granted granted Critical
Publication of CN102086465B publication Critical patent/CN102086465B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Landscapes

  • Peptides Or Proteins (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)

Abstract

The invention discloses a method for preparing ginkgo polypeptide. The method comprises the following the steps of: shelling a raw material; removing seed coats and grinding seeds into thick liquid; drying; degreasing; performing enzymatic hydrolysis on degreased ginkgo powder; performing membrane separation on enzymolysis liquid; collecting trapped fluid for concentrating; fractionally precipitating polysaccharide and polypeptide by using a solvent; washing polypeptide precipitate; and performing freeze drying so as to obtain polypeptide dry powder. The molecular weight of a polypeptide active substance is between 3,000 Dalton and 10,000 Dalton, the polypeptide content is 50 to 80 percent, the moisture content is less than 5 percent, and the granularity is between 100 meshes and 200 meshes. The polypeptide contains eight types of amino acids which are essential for human bodies; simultaneously, the content of lysine is more than 7 percent, the content of histidine is more than 8 percent, the content of serine is more than 11 percent, the content of aspartic acid is more than 14 percent, and the content of glutamic acid is more than 16 percent. In particularly, the content of the aspartic acid, the glutamic acid, the serine and the lysine in the polypeptide is remarkably higher than that of the same in the ginkgo raw material, so that a new method for deep processing of ginkgo is found. The method has a simple process, is environmentally-friendly, and is suitable for industrial production.

Description

The method of preparing polypeptide active substance from enzymolysis ginkgo protein
Technical field
The present invention relates to a kind of vegetable active thing extraction and separation technology, relate in particular to a kind of method of preparing polypeptide active substance from enzymolysis ginkgo protein.
Background technology
In recent years, the progress of polypeptide protein is rapid, especially the natural polypeptides and the protein that have physiology and pharmaceutical activity, at present existing new constituent quite a lot is found, they not only play an important role on the adjusting body function, and also have activity on AIDS resisting, cancer, cardio-cerebrovascular diseases.Gingko not only contains flavones, terpene lactones, polysaccharide, trace element, grease.And contain protein more than 10%.The foreign scholar finds dynamic smart sample material rnase in gingko, and the people such as Deng Qianchun separate gingko albumin protein ((Ginkgo Albumin Protein, GAP) from gingko.GAP is take white protein as leading and have the albumen of notable biological activity; Xie Bijun has studied enzymatic hydrolysis and anti-oxidant activity, inhibition tumor promotion and the Immunologic Functions thereof of gingko albumin protein.Studies show that the activated protein before gingko peptides is than enzymolysis, its anti-oxidant activity has raising in various degree, yet also the utmost point is deep in present correlative study both domestic and external, especially the processing technology of the separation of the high efficiency extraction of activated protein and bio-transformation active polypeptide thereof.
Plant protein accounts for more than 70% of world's albumen total supply, and its nutritive value and animal protein approach, and cholesterol level is low, contains a large amount of essential amino acids, is mankind's edible protein important sources.But protein exists with macromolecular form, and the quantity of its amino acid monomer does not wherein contain the little peptide of various molecular weight less greater than 100, therefore is unfavorable for absorption of human body.The outlet of plant protein resource broadened application is to utilize biological method or soda acid chemical process to carry out processing treatment to vegetable-protein, to reduce its molecular weight, remove simultaneously antinutritional factor and toxin, improve nutritive value and functional performance, improve solubility property, make its biological value near animal protein, replace Some Animals protein, reach the purpose that takes full advantage of plant protein resource.
Proteolysis can be converted into polypeptide, at present main acid system hydrolysis and the enzymatic hydrolysis of adopting.Acid system is wayward because of hydrolysis degree, working condition is harsh, amino acid suffers damage seldom adopts; Enzymatic hydrolysis does not damage amino acid and mostly is used, but the selection of enzyme is most important.Therefore, utilize biological enzyme degrading activity albumen, the biologically active substances such as preparation active polypeptide and amino acid, after eating human body, has the effect of the cholesterol of reduction, also be conducive to the milk-acid bacteria in enteron aisle, the growth of bifidocaterium, have very high nutritive value and functional performance, this method is extensively used and is become study hotspot, especially polypeptide, the industrialized development of protein medicaments liposome are rapid, as the Berna Biotech employing Virosome of company technology, embed virus membrane antigen on the phospholipid bilayer of liposome, the preparation liposome bacterin.
Summary of the invention
The invention provides a kind of method method of preparing polypeptide active substance from enzymolysis ginkgo protein of high conversion, resulting polypeptide purity is high.
The present invention adopts following technical scheme:
A kind of method of preparing polypeptide active substance from enzymolysis ginkgo protein is comprised of following steps:
The first step, preparation degreasing gingko powder: with fresh ginkgo shelling, except the clothing skin, pull an oar into paste with hollander at lower than the temperature of 20 ℃, then with non-polar solvent or supercritical CO 2Oil and grease extracting, then at-10 ℃--50 ℃ of lyophilizes, the weight percentage that obtains moisture less than 5%, fragmentation, sieve, obtaining granularity is 100~200 purpose degreasing gingko powder;
Second step, enzymic hydrolysis degreasing gingko powder: be mixing in 1: 5~1: 15 in mass ratio with described degreasing gingko powder and deionized water, add wherein again enzyme, the interpolation quality of enzyme is 5%~20% of described degreasing gingko powder, heating is under 30~60 ℃ mixture temperature, regulates to make its pH value be in 7~10, stirring reaction 3~48h, supernatant liquor is collected in centrifugation after hydrolysis;
The 3rd step membrane sepn enzymolysis solution, molecular weight cut-off is 3000-10000 dalton polypeptide class actives, is obtaining concentrated enzymolysis solution lower than 30 ℃ of lower vacuum concentration;
The purifying of the 4th step polypeptide: be 50~90% ethanol or acetone soln and described concentrated enzymolysis solution 1-10 by volume with mass percent: 1 mix and blend, the precipitation polysaccharose substance, centrifuging makes clear liquid, then adds reagent, and described reagent is trichoroacetic acid(TCA), acetone, (NH 4) 2SO 4In any or its mixture, described reagent and described clear liquid volume ratio 1-10: 1, and mix and blend, precipitation obtains polypeptide class actives;
The preparation of the 5th step gingko polypeptide powder: the described polypeptide class actives with the 4th step obtained, be precipitated with acetone, ethanol, methanol wash successively, be deposited in-10 ℃--50 ℃ of lyophilizes obtain the gingko polypeptide powder.
In technique scheme, polypeptide class actives molecular weight is 3000-10000 dalton, and the quality percentage composition of polypeptide is 50~80%, and the quality percentage composition of contained humidity is lower than 5%, granularity 100~200 orders; Wherein in polypeptide, lysine content is greater than 7%, and Histidine is greater than 8%, and Serine is greater than 11%, and aspartic acid is greater than 14%, and L-glutamic acid is greater than 16%.
Enzyme is active papoid greater than 800,000 u/g, active bacillus alkaline protease greater than 200,000 u/g, active neutral protease greater than 150,000 u/g, active cellulase greater than 1,000,000 u/g, active one or more mixture greater than in the polygalacturonase of 800,000 u/g.
Described non-polar solvent be in normal hexane, ether, sherwood oil, No. 6 solvent oils any, with the liquid-solid ratio of degreasing gingko powder be 1-20: 1, wherein liquid measures with milliliter, solid measures with gram.Described supercritical CO 2Extracting pressure is 10-30MPa, and extraction temperature is 25-50 ℃, and extraction time is 1-4h, CO used 2Flow is 10-30L/h, and the functional quality percentage concentration is that the 1%-15% sherwood oil is as entrainment agent.
The present invention obtains following technique effect:
1. the present invention adopts the fresh gingko of lyophilize and supercritical process degreasing, and the quality of assurance gingko and protein and polypeptide are not degraded, and, spraying drying dry with traditional Vacuum Heat compared, and the content of the proteins and peptides of product improves more than 20%.Preferred 0-20 degree centigrade of the first step making beating temperature of the present invention, too low temperature is unfavorable for extracting, and too high temperature easily causes by product to increase.The 3rd preferred 0-30 degree centigrade of step vacuum concentration, too low temperature efficiency is lower, and too high temperature easily causes unstable products.
2. adopt CO in the first step of the present invention 2Amount and quality that supercritical extraction gingko powder obtains Ginkgo oil are all higher, and the Ginkgo oil yield of preparation improves 20%-35% than prior art, and especially in Ginkgo oil, insatiable hunger is closed lipid acid and brought up to more than 85%, and wherein 9,12-C 18:2Linolic acid accounts for 31.876%, 8-C 18:1Oleic acid accounts for 20.360%; 9-C 18:1Oleic acid accounts for 19.345%.
3. adopt the different techniques such as the degraded of enzyme solution low temperature, class settling, nanofiltration and lyophilize, gingko polypeptide transformation efficiency is higher than 70%, and enrichment polypeptide class actives molecular weight is 3000-10000 dalton, and content of peptides is 50~80%, and purity is high;
4. the enzymolysis model of setting up ginkgo protein matter is DH%=599.51725-229.33925 * A+16.46370 * B-12.04075 * C+2.509 * A * B+6.05250 * A * C-0.594 * B * C+7.12425 * A2-0.40213 * B2-3.35575 * C2, for the best enzymolysis process of ginkgo protein matter provides theoretical parameter;
5. the degreasing gingko polypeptide of this patent preparation, not only content of peptides is 50~80%, moisture<5%, granularity 100~200 orders, and also polypeptide contains 17 seed amino acids, the amino acid that comprises 8 kinds of needed by human, while lysine content>7%, Histidine>8%, Serine>11%, aspartic acid>14%, L-glutamic acid>16%.Especially the content of aspartic acid, L-glutamic acid, Serine and Methionin amino acid in the ginkgo protein powder, after eating human body, more easily absorbed by the body, showing as molecular weight is the daltonian small molecules of 3000-10000, and amino acid whose composition is comprehensive, and ratio is reasonable, and nutrition is abundanter.
Description of drawings
The isogram of Fig. 1 enzymolysis pH value and temperature
The response surface figure that Fig. 2 Fig. 1 is corresponding
The isogram of Fig. 3 enzymolysis pH value and concentration of substrate
The response surface figure that Fig. 4 Fig. 3 is corresponding
The isogram of Fig. 5 hydrolysis temperature and concentration of substrate
The response surface figure that Fig. 6 Fig. 5 is corresponding
Figure 71 7 seed amino acid standard substance HPLC
Fig. 8 gingko polypeptide powder amino acid HPLC
Fig. 9 supercritical extraction Ginkgo oil GC-MS
Embodiment
Following examples are more of the present invention giving an example, and should not be seen as limitation of the invention.
Embodiment 1
A kind of method of preparing polypeptide active substance from enzymolysis ginkgo protein is comprised of following steps:
The first step, preparation degreasing gingko powder: with fresh ginkgo shelling, except the clothing skin, pull an oar into paste with hollander at lower than the temperature of 20 ℃, for example temperature can be chosen for 19 ℃, 18 ℃, 14 ℃, 10 ℃, 8 ℃, 6 ℃, 5 ℃, 4 ℃ ,-2 ℃ ,-6 ℃ ,-8 ℃, then with non-polar solvent or supercritical CO 2Oil and grease extracting, then at-10 ℃--50 ℃ of lyophilizes, for example lyophilize 6-50 hour, time can be 20 hours, 40 hours, and the quick moisture determination of infrared rays, the weight percentage that obtains moisture less than 5%, fragmentation, sieve, obtaining granularity is 100~200 purpose degreasing gingko powder;
second step, enzymic hydrolysis degreasing gingko powder: be mixing in 1: 5~1: 15 in mass ratio with described degreasing gingko powder and deionized water, for example can be chosen for 1: 8, 1: 9, 1: 11, 1: 14, add wherein again enzyme, the interpolation quality of enzyme is 5%~20% of described degreasing gingko powder, for example can be chosen for 7%, 9%, 13%, 15%, 16%, 18%, heating is under 30~60 ℃ mixture temperature, for example temperature can be chosen for 35 ℃, 45 ℃, 55 ℃, adjusting makes its pH value be in 7~10, stirring reaction 3~48h, for example be chosen as 4 hours, 15 hours, 20 hours, 40 hours, centrifugation after hydrolysis, collect supernatant liquor,
The 3rd step membrane sepn enzymolysis solution, molecular weight cut-off is 3000-10000 dalton polypeptide class actives, is obtaining concentrated enzymolysis solution lower than 30 ℃ of vacuum concentration; As elect-5 ℃ as, and-2 ℃, 0 ℃, 5 ℃, 8 ℃, 12 ℃, 18 ℃, 20 ℃, 25 ℃,
The purifying of the 4th step polypeptide: be 50~90% ethanol or acetone soln and described concentrated enzymolysis solution 1-10 by volume with mass percent: 1 mix and blend, for example can be chosen for: 2: 1,4: 1,7: 1,9: 1, the precipitation polysaccharose substance, centrifuging makes clear liquid, add reagent, described reagent is trichoroacetic acid(TCA), acetone, (NH again 4) 2SO 4In any or its mixture, described reagent and described clear liquid volume ratio 1-10: 1, for example can be chosen for: 2: Isosorbide-5-Nitrae: 1,8: 1,9: 1, and mix and blend, precipitation obtains polypeptide class actives;
The preparation of the 5th step gingko polypeptide powder: the described polypeptide class actives with the 4th step obtained, be precipitated with acetone, ethanol, methanol wash successively, be deposited in-10 ℃--50 ℃ of lyophilizes, for example can be chosen for-20 ℃,-40 ℃ ,-45 ℃, obtain the gingko polypeptide powder.
In technique scheme, polypeptide class actives molecular weight is 3000-10000 dalton, and the quality percentage composition of polypeptide is 50~80%, and the quality percentage composition of contained humidity lower than 5%, is for example 3%, 2%, granularity 100~200 orders; Wherein in polypeptide, lysine content is greater than 7%, and Histidine is greater than 8%, and Serine is greater than 11%, and aspartic acid is greater than 14%, and L-glutamic acid is greater than 16%.Described content is the quality percentage composition.
in technique scheme, enzyme is active papoid greater than 800,000 u/g, for example activity is 900,000 u/g, 950,000 u/g, active bacillus alkaline protease greater than 200,000 u/g, for example activity is 350,000 u/g, for example activity is 400,000 u/g, active neutral protease greater than 150,000 u/g, for example activity is 200,000 u/g, for example activity is 300,000 u/g, active cellulase greater than 1,000,000 u/g, for example activity is 1,200,000 u/g, for example activity is 1,400,000 u/g, in active polygalacturonase greater than 800,000 u/g, 900,000 u/g for example, 1,000,000 u/g, the mixture of above-mentioned one or more, if mixture, it can be arbitrary proportion.
Described non-polar solvent be in normal hexane, ether, sherwood oil, No. 6 solvent oils any, with the liquid-solid ratio of degreasing gingko powder be 1-20: 1, wherein liquid measures with milliliter, solid measures with gram.Described supercritical CO 2Extracting pressure is 10-30MPa, and extraction temperature is 25-50 ℃, and for example 35 ℃, 40 ℃, extraction time is 1-4h, for example is chosen for 2 hours, 3 hours, and CO used 2Flow is 10-30L/h, for example is chosen for 20L/h, and the functional quality percentage concentration be the 1%-15% sherwood oil as entrainment agent, for example mass concentration is 8%, 12%.
Embodiment 2 ginkgo protein enzymolysis prepare polypeptide class actives
A kind of method of efficient preparing polypeptide active substance from enzymolysis ginkgo protein comprises the following steps: the first step prepares degreasing gingko powder: fresh gingko 100g-200g is shelled, can select 100g, 120g, 150g, 180g, 200g except the clothing skin, is 5 ℃ with hollander, 10 ℃, 12 ℃, 15 ℃, 18 ℃, pull an oar into paste under 20 ℃, then with non-polar solvent or supercritical CO 2Oil and grease extracting, at-10 ℃--50 ℃ of lyophilizes, preferably-20 ℃--40 ℃, for example be chosen for-25 ℃ ,-30 ℃,-40 ℃, preparation degreasing gingko powder, the quick moisture determination of infrared rays, moisture<5% (mass percent), broken, sieve, obtain granularity 100~200 orders, protein content 11.3% (mass percent) degreasing gingko powder;
Second step enzymic hydrolysis degreasing gingko powder: be mixing in 1: 5~1: 15 by degreasing gingko powder and deionized water quality ratio, the enzyme addition is 5%~20% of degreasing gingko powder raw material, and is preferred 5%~8%, 30~60 ℃ of temperature, preferred 40 ℃, 50 ℃, pH=7~10, preferred pH=8 and pH=9, stirring reaction time 3~48h, preferred 4-8h, supernatant liquor is collected in centrifugation after hydrolysis, and degree of hydrolysis (DH%) is greater than 70%;
The 3rd step membrane sepn enzymolysis solution:
The cellulose membrane of the centrifugal enzymolysis clear liquid that obtains of second step through 0.45 μ m filtered, select molecular weight 3,000 dalton, 5,000 dalton, 10, the filtrate of 000 dalton, 30,000 daltonian polysulfone membrane fractional separation cellulose membranes, molecular weight cut-off are 3000-10000 dalton polypeptide class actives, at vacuum concentration below 30 ℃, preferred-5 ℃--40 ℃ of vacuum freezings are to 50ml-100ml;
The purifying of the 4th step polypeptide
With 50~90% ethanol or acetone and membrane sepn polypeptide concentrated solution 1-10 by volume: 1 mix and blend, the precipitation polysaccharose substance, centrifuging makes clear liquid.Select TCA (trichoroacetic acid(TCA)), acetone, (NH 4) 2SO 4Three kinds of reagent is any or with the 1-10 by volume of array mode arbitrarily: mix and blend in 1 clear liquid that adds after centrifugal, precipitation polypeptide class actives;
The preparation of the 5th step gingko polypeptide powder
With the polypeptide class actives of the 4th step precipitation, use successively acetone, ethanol, methanol wash by solid-to-liquid ratio 1: 1-30 (g/ml), throw out is at-10 ℃--and 50 ℃ of lyophilizes obtain the gingko polypeptide powder.
In the present embodiment, enzyme is selected papoid (>80 ten thousand u/g), bacillus alkaline protease (>20 ten thousand u/g), any mixture of one or more in neutral protease (>15 ten thousand u/g), cellulase (>100 ten thousand u/g), polygalacturonase (>80 ten thousand u/g).Non-polar solvent is selected in normal hexane, ether, sherwood oil, No. 6 solvent oils any, with the liquid-solid ratio (ml/g) of degreasing gingko powder be 1-20: 1.Supercritical CO 2Extracting pressure 10-30MPa, extraction temperature 25-50 ℃, extraction time 1-4h, CO 2Flow 10-30L/h, 1%-15% sherwood oil are as entrainment agent, and in preparation gingko grease, lipid acid>85% is closed in insatiable hunger.In the present embodiment, preparation polypeptide class actives molecular weight is 3000-10000 dalton, and content of peptides is 75%, moisture<5%, granularity 100~200 orders.And polypeptide contains 17 seed amino acids, and wherein aspartic acid 14.26%, L-glutamic acid 16.89%, Serine 11.32%, Histidine 8.02%, glycine 4.56%, Threonine 5.96%, arginine 6.54%, L-Ala 7.41%, tyrosine 2.25%, Gelucystine 0.21%, α-amino-isovaleric acid 4.57%, methionine(Met) 1.92%, phenylalanine 1.97%, Isoleucine 2.27%, leucine 3.15%, Methionin 7.70%, proline(Pro) 1.01%.
Embodiment 3 ginkgo protein enzymolysis prepare polypeptide class actives
With the 100g ginkgo shelling, except the clothing skin, pull an oar into paste with hollander under 15 ℃, with normal hexane equal-volume extraction 3-5 time, eliminate grease again, water layer is at-35 ℃ of lyophilize 40h, be broken into granularity 100~200 order degreasing gingko powder after drying, the infrared rays Fast Measurement, moisture 4.45%, protein content 11.8%.
Take degreasing gingko powder 20g, add deionized water 100ml, add enzyme activity 400,000 u/g neutral protease 2g, regulate pH=8, be hydrolyzed 5h under temperature 50 C, centrifugal after hydrolysis, collect supernatant liquor.Supernatant liquor is through the cellulose membrane of 0.45 μ m, and filtrate is first through the polysulfone membrane of 10,000MW, see through liquid through the polysulfone membrane of 3,000MW, trapped fluid-40 ℃ freeze concentration is to 50ml, add 250ml70% ethanol, the precipitation Crude polysaccharides, centrifugal, it is in the TCA (trichoroacetic acid(TCA))/acetone mixed solution 200ml of 1: 9 that supernatant concentration adds volume ratio to 50ml, the precipitation polypeptide, centrifugal, throw out is washed the impurity such as most moisture content again with acetone, and insolubles makes polypeptide dry powder-25 ℃ of lyophilizes.Take the tetrapeptide standard substance as check analysis, in polypeptide dry powder, content of peptides is 70%, and wherein aspartic acid 15.6%, L-glutamic acid 17.2%, Serine 11.5%, Histidine 8.7%, glycine 3.7%, Threonine 5.9%, arginine 7.4%, L-Ala 7.8%, tyrosine 1.4%, α-amino-isovaleric acid 6.4%, Isoleucine 2.8%, leucine 3.7%, Methionin 7.8%.
Embodiment 4 ginkgo protein enzymolysis prepare polypeptide class actives
With the 200g ginkgo shelling, except the clothing skin, pull an oar into paste with hollander under 15 ℃, with ether equal-volume extraction 3-5 time, eliminate grease again, water layer is at-35 ℃ of lyophilize 40h, be broken into granularity 100~200 order degreasing gingko powder after drying, the infrared rays Fast Measurement, moisture 4.45%, protein content 11.8%.
Take degreasing gingko powder 30g, add deionized water 280ml, add enzyme activity 1,200,000 u/g papoid 3g, regulate pH=9, be hydrolyzed 6h under temperature 45 C, centrifugal after hydrolysis, collect supernatant.Supernatant liquor is through the cellulose membrane of 0.45 μ m, and filtrate is first through the polysulfone membrane of 10,000MW, see through liquid through the polysulfone membrane of 3,000MW, trapped fluid-40 ℃ freeze concentration is to 50ml, add 250ml80% acetone, the precipitation Crude polysaccharides, centrifugal, supernatant concentration is to 50ml, add 10%-15%TCA (trichoroacetic acid(TCA)) precipitation polypeptide, centrifugal, throw out is washed the impurity such as most moisture content again with acetone, and insolubles makes polypeptide dry powder-35 ℃ of lyophilizes.Take the tetrapeptide standard substance as check analysis, in polypeptide dry powder, content of peptides is 58%, and wherein aspartic acid 15.6%, L-glutamic acid 17.2%, Serine 11.5%, Histidine 8.7%, glycine 3.7%, Threonine 5.9%, arginine 7.4%, L-Ala 7.8%, tyrosine 1.4%, α-amino-isovaleric acid 6.4%, Isoleucine 2.8%, leucine 3.7%, Methionin 7.8%.
Embodiment 5 ginkgo protein enzymolysis prepare polypeptide class actives
With the 200g ginkgo shelling, except the clothing skin, pull an oar into paste with hollander under 15 ℃, with sherwood oil equal-volume extraction 3-5 time, eliminate grease again, water layer is at-35 ℃ of lyophilize 40h, be broken into granularity 100~200 order gingko powder after drying, the infrared rays Fast Measurement, moisture 4.45%, protein content 11.8%.
Take degreasing gingko powder 30g, add deionized water 280ml, add enzyme activity 250,000 u/g bacillus alkaline protease 1g, 1,000,000 u/g cellulase 1g, 800,000 u/g polygalacturonase 1g regulate pH=9, are hydrolyzed 6h under temperature 45 C, and are centrifugal after hydrolysis, collect supernatant.Supernatant liquor is through the cellulose membrane of 0.45 μ m, and filtrate is first through the polysulfone membrane of 10,000MW, see through liquid through the polysulfone membrane of 3,000MW, trapped fluid-40 ℃ freeze concentration is to 50ml, add 250ml80% acetone, the precipitation Crude polysaccharides, centrifugal, supernatant concentration is to 50ml, add 70% ammoniumsulphate soln mixed precipitation polypeptide, centrifugal, throw out is washed the impurity such as most moisture content again with acetone, and insolubles makes polypeptide dry powder-35 ℃ of lyophilizes.Take the tetrapeptide standard substance as check analysis, in polypeptide dry powder, content of peptides is 65%, and wherein aspartic acid 15.6%, L-glutamic acid 17.2%, Serine 11.5%, Histidine 8.7%, glycine 3.7%, Threonine 5.9%, arginine 7.4%, L-Ala 7.8%, tyrosine 1.4%, α-amino-isovaleric acid 6.4%, Isoleucine 2.8%, leucine 3.7%, Methionin 7.8%.
The overcritical preparation degreasing of embodiment 6 gingko powder and Ginkgo oil
With the 300g ginkgo shelling, except the clothing skin, pull an oar into paste with hollander under 15 ℃, at-35 ℃ of lyophilize 40h, be broken into granularity 100 order gingko powder after drying.Weighing gingko powder 100g puts into 1L CO 2Extract extracting pressure 10-30MPa, extraction temperature 25-50 ℃, extraction time 1-4h, CO in the supercritical extraction tank 2Flow 10-30L/h,, optimum process condition is 40 ℃ of temperature, pressure 20MPa, flow velocity 15L/h, time 3h, the Ginkgo oil yield can reach 7.11%.CO 2Gingko powder after supercritical extraction is broken into granularity 100~200 order gingko powder, infrared rays Fast Measurement, moisture 4.45%, protein content 11.8% at-35 ℃ of lyophilize 20h after drying.
The GC-MS Analysis for CO 2The Ginkgo oil chemical composition of supercritical extraction shows: in Ginkgo oil, the unsaturated fatty acids total amount can reach 85.2%, and wherein 9,12-C 18:2Linolic acid accounts for 32%, 8-C 18:1Oleic acid accounts for 21%; 9-C 18:1Oleic acid accounts for 20%.Ginkgo oil has following physical features: refractive index (n 40): 1.460~1.468; Relative density (d): 0.922~0.929; Iodine number (I) is (g/100g): 95~115; Saponification value (KOH) is (mg/g): 187~196; Unsaponifiables (g/kg) :≤15.Color and luster (Lovibond cell 133.4mm)≤Huang 70 red 4.0; Moisture and volatile matter content/(%)≤0.2; Insoluble impurities/(%)≤0.2; Acid number (KOH)/(mg/g)≤4.0; Heat test (280 ℃).
The overcritical preparation degreasing of embodiment 7 gingko powder and Ginkgo oil
The present embodiment purpose is to obtain a seed amino acid to form abundant, rational polypeptide from the gingko powder, wherein polypeptide class actives molecular weight is 3000-10000 dalton, content of peptides is 50~80%, and the contained humidity mass percent is less than 5%, granularity 100~200 orders.Polypeptide contains 8 kinds of indispensable amino acids of human body, while lysine content>7%, Histidine>8%, Serine>11%, aspartic acid>14%, L-glutamic acid>16%.Especially the content of aspartic acid, L-glutamic acid, Serine and Methionin is apparently higher than the gingko raw material, for new approach is found in the deep processing of gingko.
The method that adopts is comprised of following steps:
The first step prepares degreasing gingko powder
Fresh gingko 100g-200g is shelled, except the clothing skin, pulling an oar into paste with hollander lower than 20 ℃, then with non-polar solvent or supercritical CO 2Oil and grease extracting, at-10 ℃--50 ℃ of lyophilizes, the infrared rays Fast Measurement, moisture<5%,, granularity 100~200 orders;
Second step enzymic hydrolysis degreasing gingko powder
Be mixing in 1: 5~1: 15 by degreasing gingko powder and deionized water quality ratio, the enzyme addition is 5%~20% of degreasing gingko powder raw material, 30~60 ℃ of temperature, pH=7~10, stirring reaction time 3~48h, centrifugation after hydrolysis, collect supernatant liquor, degree of hydrolysis (DH%) is greater than 70%;
The 3rd step membrane sepn enzymolysis solution
The cellulose membrane of the centrifugal enzymolysis clear liquid that obtains of second step through 0.45 μ m filtered, select molecular weight 3,000 dalton, 5,000 dalton, 10,000 dalton, 30, the filtrate of 000 daltonian polysulfone membrane fractional separation cellulose membrane, molecular weight cut-off are 3000-10000 dalton polypeptide class actives, at vacuum concentration below 30 ℃ to 50ml-100ml;
The purifying of the 4th step polypeptide
With 50~90% ethanol or acetone and membrane sepn polypeptide concentrated solution 1-10 by volume: 1 mix and blend, the precipitation polysaccharose substance, centrifuging makes clear liquid.Select TCA (trichoroacetic acid(TCA)), acetone, (NH 4) 2SO 4Three kinds of reagent is any or with the 1-10 by volume of array mode arbitrarily: mix and blend in 1 clear liquid that adds after centrifugal, precipitation polypeptide class actives;
The preparation of the 5th step gingko polypeptide powder
With the polypeptide class actives of the 4th step precipitation, use successively acetone, ethanol, methanol wash by solid-to-liquid ratio 1: 1-30 (g/ml), throw out obtains the gingko polypeptide powder-10 ℃ of-50 ℃ of lyophilizes.
The present invention does not degrade for the quality that guarantees gingko and protein and polypeptide, with water content in the shelling of the fresh gingko of 50%-65% with except after the clothing skin, employing is lower than 20 ℃ of making beating and cryodesiccated method, at-10 ℃ extremely--50 ℃ of lyophilizes, freezing time 6-50 hour, preferably-15 ℃--40 ℃, freezing time 10-40 hour, water content<6%.If do not adopt the art of this patent to process, higher than 50%, issue the metabolism of biochemical composition due to the water content of fresh gingko in the effect of self enzyme, enzyme liberating, easy moldy metamorphism, the nutritive ingredients such as protein and grease are destroyed.The easy enzymolysis of ginkgo protein produces peculiar smell, also easily goes mouldy, and has influence on the local flavor of gingko.If adopt heated drying or Exposure to Sunlight to process, the original volatile component of gingko easily loses, and grease easily produces and becomes sour simultaneously.If 190 ℃ of-220 ℃ of lower spraying dryings, obtain water content at the powder of 10% left and right; Due to through pyroprocessing, ginkgo protein, polypeptide, the sex change of enzyme isoreactivity thing can not keep the structure of original proteins and peptides.And experiment shows protein content 11.9% in lyophilize gingko powder, greater than protein content 9.7% in spraying drying gingko powder.
Contain the fat-soluble ginkgotoxins such as hydrocyanic acid, ginkgolic acid, Hydroginkgolic acid and bilobol due to gingko, easily cause untoward reaction, affect people's neural system, Digestive tract, integumentary system and hemopoietic system.Therefore, the people of some responsive physique easily occurs irritated to ginkgotoxin, occur various types of dermatitis fash after food; After the edible gingko of somebody, the gastrointestinal discomfort symptom can appear, as situations such as nauseating, vomiting, stomachache, diarrhoea.In addition, gingko contains the grease of 4%-10%, is mainly wherein unsaturated fatty acids, and to cause that easily oyster loses rotten due to unsaturated fatty acids, and the existence of grease simultaneously affects proteolysis and becomes polypeptide.In order to remove the gingko grease, this patent adopted with non-polar solvent or supercritical CO before preparation gingko powder 2Then oil and grease extracting becomes degreasing gingko powder-10 ℃ to-50 ℃ lyophilizes.
This patent non-polar solvent is selected in normal hexane, ether, sherwood oil, No. 6 solvent oils any, with the liquid-solid ratio (ml/g) of degreasing gingko powder be 1-20: 1, preferred 10-15: 1, continuous extraction 3-6 time, residuum becomes degreasing gingko powder-10 ℃ to-50 ℃ lyophilizes.This patent adopts supercritical CO simultaneously 2Oil and grease extracting, supercritical CO 2Extracting pressure 10-30MPa, extraction temperature 25-50 ℃, extraction time 1-4h, CO 2Flow 10-30L/h, 1%-15% sherwood oil be as entrainment agent, and preparation gingko grease unsaturated fatty acid content is brought up to more than 85%, and wherein 9,12-C 18:2Linolic acid accounts for 31.876%, 8-C 18:1Oleic acid accounts for 20.360%; 9-C 18:1Oleic acid accounts for 19.345%.As table 1.
The chemical constitution of table 1 supercritical extraction gingko powder
Figure GSA00000017477300081
The present embodiment discloses the method that enzymolysis ginkgo protein matter prepares the gingko polypeptide, enzyme is selected papoid (>80 ten thousand u/g), bacillus alkaline protease (>20 ten thousand u/g), neutral protease (>15 ten thousand u/g), cellulase (>100 ten thousand u/g)), one or more any mixture in polygalacturonase (>80 ten thousand u/g), preferred neutral protease, papoid and Sumizyme MP.Degreasing gingko powder and deionized water quality ratio are mixing in 1: 5~1: 15, and the enzyme addition is 5%~20% of degreasing gingko powder raw material, 30~60 ℃ of temperature, pH=7~10, stirring reaction time 3~48h, centrifugation after hydrolysis, collect supernatant liquor, degree of hydrolysis (DH%) is greater than 65%.By investigating the impact of the factors such as hydrolysis temperature, pH value, enzyme substrates concentration, enzyme dosage, time, by Design expert experimental analysis software design, adopt Box-Behnken model (seeing Table 2), design 3 factor 3 level optimization experiments (seeing Table 3), the Surface Method that meets with a response analytical model R 2=0.8521, F value is 4.48, P value 0.0303, the model highly significant, and the optimum enzymolysis condition that obtains on this model basis is: time 4-10h, enzyme dosage 2g, pH are 9, and hydrolysis temperature is 45-50 ℃, and concentration of substrate is 2.17%.The present invention adopts formol titration to measure its amino acid nitrogen content, the degree of hydrolysis (DH%) of protein when calculating enzymolysis according to formula (1), and degree of hydrolysis (DH%) is greater than 70% with this understanding.
DH % = ( v 2 - v 1 ) × 0.1 × 14.008 TN × 100 % - - - ( 1 )
V 1-alkali-titration initial value; V 2-alkali-titration end point values; TN---total nitrogen content, mg;
Table 2Box-Behnken experimental design factor and level code value
Figure GSA00000017477300092
Adopt the Design Expert 7.1.3.1 of statistical software to carry out the multiple regression match to experimental data, model analysis shows that secondary model (Quadratic) is best fit model, and the results of analysis of variance of this model sees Table 4.
Regression diagnostics shows, coefficient of determination R-Squared=81.01%, and signal to noise ratio (Adeq-Precision)=7.498>4 illustrates that the degree of fitting of equation and confidence level are all very high, can be used for the degree of hydrolysis of pre-measured reaction.The tolerance range of C.V.% (variation coefficient of Y) expression experiment, the C.V.% value is higher, and the reliability of experiment is lower, and C.V.=14.65% in this patent contrived experiment is lower, and the illustrative experiment operation is credible.Therefore regression equation provides a model to the enzymolysis process of protein.
DH%=599.51725-229.33925 * A+16.46370 * B-12.04075 * C+2.509 * A * B+6.05250 * A * C-0.594 * B * C+7.12425 * A2-0.40213 * B2-3.35575 * C2, A-pH wherein, B-temperature, C-concentration of substrate.
Table 3 experimental design and result
Figure GSA00000017477300101
The enzymolysis clear liquid filters through the cellulose membrane of 0.45 μ m, this patent adopts the centrifugal enzymolysis clear liquid that obtains of polysulfone membrane stage treatment of different molecular weight, select molecular weight 3,000 dalton, 5,000 dalton, 10,000 dalton, 30,000 daltonian polysulfone membrane, molecular weight cut-off are 3000-10000 dalton polypeptide class actives, at vacuum concentration below 30 ℃, preferably-5 ℃--40 ℃ of vacuum freezings can keep the activity of polypeptide better to 50ml-100ml.Select 50~90% ethanol or acetone, preferred 70~80% ethanol or acetone, and membrane sepn polypeptide concentrated solution 1-10 by volume: 1 mix and blend, preferred 3-6: 1, the precipitation polysaccharose substance, centrifuging makes clear liquid.Select again TCA (trichoroacetic acid(TCA)), acetone, (NH 4) 2SO 4Three kinds of reagent is any or with the 1-10 by volume of array mode arbitrarily: mix and blend in 1 clear liquid that adds after centrifugal, precipitation polypeptide class actives; Use successively acetone, ethanol, methanol wash by solid-to-liquid ratio 1: 1-30 (g/ml), preferred solid-to-liquid ratio 1: 1-10 (g/ml) throw out is at-10 ℃--50 ℃ of lyophilizes, obtain the gingko polypeptide powder, wherein polypeptide class actives molecular weight is 3000-10000 dalton, content of peptides is 50~80%, moisture<5%, granularity 100~200 orders.
The present embodiment adopts biuret method, measures content of peptides with the drafting of tetrapeptide typical curve.Draw respectively tetrapeptide standard substance (4mg/ml) 0.0ml, 0.5ml, 1.0ml, 1.5ml, 2.0ml, 2.5ml, 3.0ml, 3.5ml, 4.0ml 4.5ml is in the 10ml volumetric flask, label adds respectively 2ml biuret reagent A, sway evenly, then add biuret reagent B, sway evenly, adding distil water is settled to scale, shake up, it was fully developed the color in standing 3 minutes, centrifugal, get supernatant, measure optical density value (OD) in the 540nm place, blank reagent (No. 1 volumetric flask) is reference.Take OD as ordinate zou, tetrapeptide standard substance concentration is X-coordinate, and the drawing standard curve carries out linear regression analysis with method of least squares, tries to achieve standard regressive method Y=aX+b.Y is absorbancy (A); X is concentration (C); A is slope; B is intercept.During sample determination, with diluted sample to proper concn,
And add biuret reagent, and processing mode is the same, and after shaking up, in 540nm place mensuration light absorption value (A), namely the y value, bring standard regressive method into, tries to achieve x, i.e. sample concentration (C).Adopt biuret method to survey its content of peptides, obtain typical curve equation Y=0.2475X+0.0004, R 2=0.9992.
The present embodiment is set up the HPLC method and is measured polypeptide amino acid, HPLC adopts 17 seed amino acid standard substance to do the external standard contrast, sets up HPLC reversed-phase system analysis of amino acid and forms, concrete operation method: get polypeptide sample 29.14mg, add 0.8ml5.7NHCl to put into the acid treatment of hydrolysis pipe, be filled with N 2Rear tube sealing is hydrolyzed 22h under 110 ℃.Open pipe is settled to 2ml after neutralization, get supernatant after centrifugal and put into volumetric flask and treat that HPLC analyzes.Analysis condition: o-phthalaldehyde(OPA) column front derivation, stationary phase ODS C 18(4.6 * 50mm, 5 μ), mobile phase A: sodium acetate soln (including 3 ‰ tetrahydrofuran (THF)s); Mobile phase B: water: methyl alcohol: acetonitrile=200: 450: 350, carry out linear gradient elution, flow velocity: 0.5ml/min, ultraviolet detection 338.1nm.HPLC collection of illustrative plates such as Fig. 4 of 17 seed amino acid standard substance, HPLC collection of illustrative plates such as Fig. 5 of polypeptide amino acid.
Table 4 secondary model analysis of variance table
Figure GSA00000017477300111
The degreasing gingko polypeptide of the present embodiment preparation, wherein polypeptide class actives molecular weight is 3000-10000 dalton, and content of peptides is 50~80%, moisture<5%, granularity 100~200 orders, and polypeptide contains 17 seed amino acids, comprises the amino acid of 8 kinds of needed by human, simultaneously lysine content>7%, Histidine>8%, Serine>11%, aspartic acid>14%, L-glutamic acid>16%.Especially the content of aspartic acid, L-glutamic acid, Serine and Methionin amino acid in the ginkgo protein powder, therefore, this patent utilizes biological enzyme degrading activity albumen, the biologically active substances such as preparation active polypeptide and amino acid, after eating human body, more easily absorbed by the body, showing as molecular weight is the daltonian small molecules of 3000-10000, and amino acid whose composition is comprehensive, and ratio is reasonable, and nutrition is abundanter.As table 5.
In table 5 gingko polypeptide and ginkgo protein matter, amino acid forms contrast
Figure GSA00000017477300121

Claims (5)

1. the method for a preparing polypeptide active substance from enzymolysis ginkgo protein is characterized in that being comprised of following steps:
The first step, preparation degreasing gingko powder: with fresh ginkgo shelling, except the clothing skin, pull an oar into paste with hollander at the temperature of 0-20 ℃, then use supercritical CO 2Oil and grease extracting, then at-10 ℃--50 ℃ of lyophilizes, fragmentation is sieved, the weight percentage that obtains moisture less than 5%, granularity is 100~200 purpose degreasing gingko powder;
Second step, enzymic hydrolysis degreasing gingko powder: be mixing in 1: 5~1: 15 in mass ratio with described degreasing gingko powder and deionized water, add wherein again enzyme, the interpolation quality of enzyme is 5%~20% of described degreasing gingko powder, heating is under 30~60 ℃ mixture temperature, regulates to make its pH value be in 7~10, stirring reaction 3~48h, supernatant liquor is collected in centrifugation after hydrolysis;
The 3rd step membrane sepn enzymolysis solution, molecular weight cut-off is 3000-10000 dalton polypeptide class actives, obtains concentrated enzymolysis solution at 0-30 ℃ of lower vacuum concentration;
The purifying of the 4th step polypeptide: be 50~90% ethanol or acetone soln and described concentrated enzymolysis solution 1-10 by volume with mass percent: 1 mix and blend, the precipitation polysaccharose substance, centrifuging makes clear liquid, then adds reagent, and described reagent is trichoroacetic acid(TCA), acetone, (NH 4) 2SO 4In any or its mixture, described reagent and described clear liquid volume ratio 1-10: 1, and mix and blend, precipitation obtains polypeptide class actives;
The preparation of the 5th step gingko polypeptide powder: the described polypeptide class actives with the 4th step obtained, be precipitated with acetone, ethanol, methanol wash successively, be deposited in-10 ℃--50 ℃ of lyophilizes obtain the gingko polypeptide powder.
2. the method for preparing polypeptide active substance from enzymolysis ginkgo protein according to claim 1, it is characterized in that, polypeptide class actives molecular weight is 3000-10000 dalton, the quality percentage composition of polypeptide is 50~80%, the quality percentage composition of contained humidity is lower than 5%, granularity 100~200 orders; Wherein in polypeptide, lysine content is greater than 7%, and Histidine is greater than 8%, and Serine is greater than 11%, and aspartic acid is greater than 14%, and L-glutamic acid is greater than 16%.
3. the method for preparing polypeptide active substance from enzymolysis ginkgo protein according to claim 1, it is characterized in that, enzyme is active papoid greater than 800,000 u/g, active bacillus alkaline protease greater than 200,000 u/g, active neutral protease greater than 150,000 u/g, active cellulase greater than 1,000,000 u/g, active one or more mixture greater than in the polygalacturonase of 800,000 u/g.
4. the method for preparing polypeptide active substance from enzymolysis ginkgo protein according to claim 1, is characterized in that, described supercritical CO 2Extracting pressure is 10-30MPa, and extraction temperature is 25-50 ℃, and extraction time is 1-4h, CO used 2Flow is 10-30L/h, and the functional quality percentage concentration is that the 1%-15% sherwood oil is as entrainment agent.
5. the method for preparing polypeptide active substance from enzymolysis ginkgo protein according to claim 1, is characterized in that, the temperature of described the first step making beating is 10 ℃-20 ℃.
CN2010101120962A 2010-02-12 2010-02-12 Method for preparing polypeptide active substance from enzymolysis ginkgo protein Active CN102086465B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010101120962A CN102086465B (en) 2010-02-12 2010-02-12 Method for preparing polypeptide active substance from enzymolysis ginkgo protein

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010101120962A CN102086465B (en) 2010-02-12 2010-02-12 Method for preparing polypeptide active substance from enzymolysis ginkgo protein

Publications (2)

Publication Number Publication Date
CN102086465A CN102086465A (en) 2011-06-08
CN102086465B true CN102086465B (en) 2013-06-19

Family

ID=44098470

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010101120962A Active CN102086465B (en) 2010-02-12 2010-02-12 Method for preparing polypeptide active substance from enzymolysis ginkgo protein

Country Status (1)

Country Link
CN (1) CN102086465B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102422976A (en) * 2011-12-20 2012-04-25 江苏伟楼生物科技有限公司 Preparation method for gingko polypeptide
CN102617716A (en) * 2012-03-23 2012-08-01 中国林业科学研究院林产化学工业研究所 Novel ginkgo protein preparation and characterization method
CN103609831B (en) * 2013-11-19 2015-07-22 徐州绿之野生物食品有限公司 Method for preparing gingko protein peptide
CN105755082A (en) * 2016-03-22 2016-07-13 中国林业科学研究院林产化学工业研究所 High static pressure and enzyme hydrolysis combined method for preparing hypoallergenic ginkgo protein powder
CN106722941A (en) * 2016-12-01 2017-05-31 苏剑锋 The preparation method of ginkgo pectase
CN109321621B (en) * 2017-08-01 2021-10-12 江苏天肽生物科技有限公司 Preparation method and new application of ginkgo polypeptide
CN107467192A (en) * 2017-08-11 2017-12-15 烟台市华昕生物医药科技有限公司 A kind of apple peptide milk tea of the active matter containing oligopeptides
CN108486201B (en) * 2018-04-18 2021-07-16 河南工程学院 Method for extracting bioactive polypeptide of ginkgo

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
.2005, *
农业工程学报&gt *
王子佳等.蛋白质分离纯化方法研究进展.《化学与生物工程》.2009,
白果油的提取及脂肪酸组成分析;邓乾春等;《中国油脂》;20071031;第77页 *
蛋白质分离纯化方法研究进展;王子佳等;《化学与生物工程》;20090831;第8-10页 *
邓乾春.白果活性蛋白的酶法水解及抗氧化活性研究.&lt *
邓乾春.白果活性蛋白的酶法水解及抗氧化活性研究.<农业工程学报>.2005,
邓乾春等.白果油的提取及脂肪酸组成分析.《中国油脂》.2007,

Also Published As

Publication number Publication date
CN102086465A (en) 2011-06-08

Similar Documents

Publication Publication Date Title
CN102086465B (en) Method for preparing polypeptide active substance from enzymolysis ginkgo protein
CN107858393B (en) Method for extracting protein polypeptide from walnut meal
CN102417546B (en) Extraction method of rose crude polysaccharide
CN104403012A (en) Extraction technology of cordyceps militaris polysaccharide and polypeptide
WO2002012159A1 (en) Process for producing oleanolic acid and/or maslinic acid
CA2834422A1 (en) Method for utilizing extraction residue of yeast extract
CN104592784B (en) The preparation method of water-soluble dark brown natural pigment in a kind of camellia seed meal
CN105063139A (en) Preparation method of sea-buckthorn seed polypeptide used for sobering up from drunkenness
CN106418111B (en) A kind of antioxidant extract and preparation method thereof from garlic stalk
CN104418944A (en) Technology for separating multiple bioactive components in maize germ
CN107011457B (en) A method of extracting preparation non-starch polysaccharide and small molecule nutrient molecule from sweet potato waste water
CN102512353A (en) Dictyophora indusiata water extract and preparation method and application thereof
CN106728257A (en) A kind of method of high efficiency extraction longan seed polyphenol
CN101229335A (en) Method for preparing total saponin extract of smilax scobinicaulis by enzyme method
CN103409487B (en) Method used for extracting maize germ active components
CN104744601A (en) Method for extracting and purifying fleurotus ferulae polysaccharide
CN108497378A (en) A kind of black fruit fructus lycii instant powder and its preparation method and application
CN105853491B (en) A method of the composition is prepared with the composition for promoting fecundity function and by raw material of maca
CN108624643B (en) Method for preparing high value-added oligopeptide by taking nannochloropsis oculata residues as raw materials
CN103355727B (en) Preparation method for solid Cordyceps militaris beverage
CN110592167A (en) Purslane polypeptide extract and preparation method thereof
KR101156775B1 (en) Anti-cancer activity of Ganoderma lucidum extract, and extractive method using basic alcohol
RU2711728C1 (en) Method for producing a complex of bioflavonoids from defatted sea-buckthorn extraction cake
CN104862364B (en) Bee pollen form cole Oligopeptide Compositions and preparation method thereof
CA2676864C (en) Extraction of phytochemicals by enzymatic hydrolysis

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: Five suojin village of Nanjing city in Jiangsu province 210042 No. 16

Patentee after: INSTITUTE OF CHEMICAL INDUSTRY OF FOREST PRODUCTS, CAF

Patentee after: JIANGSU GINATON BIOTECHNOLOGY CO.,LTD.

Address before: Five suojin village of Nanjing city in Jiangsu province 210042 No. 16

Patentee before: INSTITUTE OF CHEMICAL INDUSTRY OF FOREST PRODUCTS, CAF

Patentee before: PIZHOU XINYUAN BIOLOGICAL PRODUCTS Co.,Ltd.

CP01 Change in the name or title of a patent holder

Address after: Five suojin village of Nanjing city in Jiangsu province 210042 No. 16

Patentee after: INSTITUTE OF CHEMICAL INDUSTRY OF FOREST PRODUCTS, CAF

Patentee after: Jiangsu Hengtian Biotechnology Co.,Ltd.

Address before: Five suojin village of Nanjing city in Jiangsu province 210042 No. 16

Patentee before: INSTITUTE OF CHEMICAL INDUSTRY OF FOREST PRODUCTS, CAF

Patentee before: JIANGSU GINATON BIOTECHNOLOGY Co.,Ltd.

CP01 Change in the name or title of a patent holder
TR01 Transfer of patent right

Effective date of registration: 20210506

Address after: Room 201, No.27, Lane 123, Shenmei Road, Pudong New Area, Shanghai

Patentee after: Shanghai Di Wan Electronic Technology Co.,Ltd.

Address before: No.716, 7th floor, building 4, No.99 Guangfu Road, Wuhou District, Chengdu, Sichuan 610000

Patentee before: Chengdu yishenrui Technology Co.,Ltd.

Effective date of registration: 20210506

Address after: No.716, 7th floor, building 4, No.99 Guangfu Road, Wuhou District, Chengdu, Sichuan 610000

Patentee after: Chengdu yishenrui Technology Co.,Ltd.

Address before: Five suojin village of Nanjing city in Jiangsu province 210042 No. 16

Patentee before: INSTITUTE OF CHEMICAL INDUSTRY OF FOREST PRODUCTS, CAF

Patentee before: Jiangsu Hengtian Biotechnology Co.,Ltd.

TR01 Transfer of patent right