CN105941819A - Extraction method of maca crude proteins - Google Patents
Extraction method of maca crude proteins Download PDFInfo
- Publication number
- CN105941819A CN105941819A CN201610270797.6A CN201610270797A CN105941819A CN 105941819 A CN105941819 A CN 105941819A CN 201610270797 A CN201610270797 A CN 201610270797A CN 105941819 A CN105941819 A CN 105941819A
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- CN
- China
- Prior art keywords
- meyenii walp
- lepidinm meyenii
- crude protein
- extraction
- extracting method
- 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.)
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- 238000000605 extraction Methods 0.000 title claims abstract description 36
- 235000019750 Crude protein Nutrition 0.000 title claims abstract description 27
- 240000000759 Lepidium meyenii Species 0.000 title abstract description 8
- 235000000421 Lepidium meyenii Nutrition 0.000 title abstract description 7
- 235000012902 lepidium meyenii Nutrition 0.000 title abstract description 6
- 238000000034 method Methods 0.000 claims abstract description 28
- 238000000227 grinding Methods 0.000 claims abstract description 11
- 239000000284 extract Substances 0.000 claims abstract description 10
- 239000003513 alkali Substances 0.000 claims abstract description 9
- 239000002253 acid Substances 0.000 claims abstract description 7
- 239000002994 raw material Substances 0.000 claims abstract description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 238000005119 centrifugation Methods 0.000 claims description 14
- 239000000843 powder Substances 0.000 claims description 13
- 241000219780 Pueraria Species 0.000 claims description 12
- 239000012670 alkaline solution Substances 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000000706 filtrate Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 235000013336 milk Nutrition 0.000 claims description 5
- 239000008267 milk Substances 0.000 claims description 5
- 210000004080 milk Anatomy 0.000 claims description 5
- 150000003839 salts Chemical class 0.000 claims description 5
- 230000003068 static effect Effects 0.000 claims description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- 235000013305 food Nutrition 0.000 claims description 3
- 102000004169 proteins and genes Human genes 0.000 abstract description 11
- 108090000623 proteins and genes Proteins 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 210000002421 cell wall Anatomy 0.000 abstract description 2
- 238000009792 diffusion process Methods 0.000 abstract description 2
- 230000003834 intracellular effect Effects 0.000 abstract description 2
- 238000003672 processing method Methods 0.000 abstract description 2
- 238000004090 dissolution Methods 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 238000000751 protein extraction Methods 0.000 abstract 1
- 238000002137 ultrasound extraction Methods 0.000 abstract 1
- 235000018102 proteins Nutrition 0.000 description 9
- 239000000243 solution Substances 0.000 description 7
- 241000196324 Embryophyta Species 0.000 description 3
- 150000001336 alkenes Chemical class 0.000 description 3
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 2
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 2
- 235000003140 Panax quinquefolius Nutrition 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 235000008434 ginseng Nutrition 0.000 description 2
- 125000004383 glucosinolate group Chemical group 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 239000004475 Arginine Substances 0.000 description 1
- 241000219193 Brassicaceae Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- CKLJMWTZIZZHCS-REOHCLBHSA-N L-aspartic acid Chemical compound OC(=O)[C@@H](N)CC(O)=O CKLJMWTZIZZHCS-REOHCLBHSA-N 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- 239000004472 Lysine Substances 0.000 description 1
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229930182558 Sterol Natural products 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- DTOSIQBPPRVQHS-PDBXOOCHSA-N alpha-linolenic acid Chemical compound CC\C=C/C\C=C/C\C=C/CCCCCCCC(O)=O DTOSIQBPPRVQHS-PDBXOOCHSA-N 0.000 description 1
- 235000020661 alpha-linolenic acid Nutrition 0.000 description 1
- 235000001014 amino acid Nutrition 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 description 1
- 235000003704 aspartic acid Nutrition 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- OQFSQFPPLPISGP-UHFFFAOYSA-N beta-carboxyaspartic acid Natural products OC(=O)C(N)C(C(O)=O)C(O)=O OQFSQFPPLPISGP-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 235000019197 fats Nutrition 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013922 glutamic acid Nutrition 0.000 description 1
- 239000004220 glutamic acid Substances 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 229960004488 linolenic acid Drugs 0.000 description 1
- KQQKGWQCNNTQJW-UHFFFAOYSA-N linolenic acid Natural products CC=CCCC=CCC=CCCCCCCCC(O)=O KQQKGWQCNNTQJW-UHFFFAOYSA-N 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000006166 lysate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- OCSIXVSXYFNTQS-UHFFFAOYSA-N n-benzyloctanamide Chemical compound CCCCCCCC(=O)NCC1=CC=CC=C1 OCSIXVSXYFNTQS-UHFFFAOYSA-N 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000001814 protein method Methods 0.000 description 1
- 230000036299 sexual function Effects 0.000 description 1
- 150000003432 sterols Chemical class 0.000 description 1
- 235000003702 sterols Nutrition 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
- A23J1/006—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from vegetable materials
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Biochemistry (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Peptides Or Proteins (AREA)
Abstract
The present invention relates to a processing method of maca and particularly relates to an extraction method of maca crude proteins. The extraction method comprises the following steps: ultrafine grinding, alkali dissolving, ultrasonic extracting, centrifugal separating and filtering. In order to overcome the disadvantages that a traditional alkali dissolving and acid precipitating method is long in extraction time and relatively high in extraction temperature, seriously destroys proteins, and is large in energy consumption, the ultrasonic extraction technology is introduced in the method, and the ultrasonic wave is applied to the medium, so that strong tensile stress appears in an extract to form a negative pressure, which forces the raw material cell walls to be ruptured instantly, accelerates dissolution and diffusion efficiencies of the intracellular proteins in the extract, and thereby can effectively shorten the extraction time and increase the extraction rate. The method has the advantages of being simple in operation, easy to control, low in cost, good in extraction effect, large-scale in production, etc. By using the method, the maca crude protein extraction rate is 10%-14%.
Description
Technical field
The processing method that the present invention relates to Lepidinm meyenii Walp, the extracting method of a kind of Lepidinm meyenii Walp crude protein.
Background technology
Lepidinm meyenii Walp is Cruciferae separate row Vegetable spp annual herb plant, originates in Peru more than height above sea level 3500m
Mountain area, Andean, can be without fertilizer, anoxia, day and night temperature greatly, normally give birth under the most ice-bound unique environments
Long." Maca " is that the English of plant Lepidium meyenii is commonly called as, and Lepidinm meyenii Walp is in nutritional labeling and increasing simultaneously
Strong energy, effect aspect of endurance can match in excellence or beauty with Radix Ginseng, are commonly referred to as the most again " PeruvianGinseng
(Peru's Radix Ginseng) ".
Fresh Lepidinm meyenii Walp (MACA) moisture content 10.4%, protein 10.2%, fat 2.2%, carbohydrate
59%, fiber 8.5%, ash 4.9%.Containing the aminoacid of abundant needed by human, such as: arginine (9.94%),
Aspartic acid (9.17%), glutamic acid (15.6%) and lysine (54.5%) etc..Lepidinm meyenii Walp (MACA)
Fatty acid in the content of unsaturated fatty acid account for 52.7% (its Linoleic acid 18.5%, linolenic acid 8.87%),
Containing glucosinolate (glucosinolates) sterol and potassium, calcium, ferrum etc..Lepidinm meyenii Walp (MACA) lipid portion
Position, containing Lepidinm meyenii Walp alkene (maceaene) and macamide (mecamide), also includes N-benzyl caprylamide, N-
Benzyl-16-hydroxyl-9-oxidation-10E, 12E, 14E-pungent certain herbaceous plants with big flowers three acrylamide, N-benzyl-16 hydroxyl-9,16-
Dioxy-10E, 12E, 14E-pungent certain herbaceous plants with big flowers three acrylamide and other 17 Lepidinm meyenii Walp alkene and the homologue of macamide.
Lepidinm meyenii Walp alkene and macamide be considered as in Lepidinm meyenii Walp (MACA) extract tool promote sexual function active substance it
One.
In presently disclosed document material, also do not have a kind of to extract the method for crude protein in Lepidinm meyenii Walp, invent one
Fine maca deep processing is very important by the extracting method planting Lepidinm meyenii Walp crude protein.
Summary of the invention
The problem that it is an object of the invention to exist for above-mentioned technology, it is provided that the extraction side of a kind of Lepidinm meyenii Walp crude protein
Method.
For achieving the above object, the technical solution used in the present invention is: the extracting method of a kind of Lepidinm meyenii Walp crude protein,
Step includes:
(1) superfine grinding: Lepidinm meyenii Walp raw material dries after cleaning, and carries out superfine grinding after section, prepares pueraria root powder；
(2) alkali is molten: the alkaline solution adding its weight 10～50 times of weight in pueraria root powder extracts, and utilizes
This alkaline solution regulation pH of mixed maintains 7.5～11.5；
(3) supersound extraction: mixed liquor adds supersound extraction tank and extracts 20～100min；
(4) centrifugation: remix liquid after supersound extraction and be centrifuged separating 15～20min；
(5) filter: filter after centrifugation, collect filtrate, add salt acid for adjusting pH extremely neutrality,
After static 15min, recentrifuge separates, and curdled milk is Lepidinm meyenii Walp crude protein.
Further, in step (1), the fineness of described pueraria root powder is 10～20 mesh.
Further, in step (2), described alkaline solution is NaOH, and concentration is 1mol/L.
Further, in step (3), described supersound extraction power is 260W～660W, described supersound extraction
Temperature 50～70 degree.
Further, in step (4), described centrifugation centrifuge speed is 3400r/min.
Further, in step (5), described centrifugation centrifuge speed is 3400r/min.
Further, in step (5), the mass concentration adding hydrochloric acid is 1mol/L.
The present invention also provides for a kind of Lepidinm meyenii Walp crude protein prepared by said method.
The present invention also provides for the application in food of a kind of Lepidinm meyenii Walp crude protein prepared by method, the thick egg of preparation
Can be used for athlete or the egg albumen powder of body-building food in vain.
The ultimate principle of the present invention is to use alkali extraction-acid precipitation, utilizes most protein isoelectric point, IP at acid model
Enclosing, when protein is in alkaline environment, most protein can be dissolved out from cell, works as lysate
When regulation pH value is to isoelectric points of proteins, due to the destruction of outer layer charge, can gather between protein molecule
Close precipitation, thus separate out from solution.
The method have the benefit that: in the present invention, for overcoming tradition alkali extraction-acid precipitation extraction time
The defects such as length, Extracting temperature is higher, serious to protein breakdown, energy resource consumption is big, introduce ultrasound wave and carry
Taking technique, by ul-trasonic irradiation in medium so that extracting solution is internal occurs that powerful tension is formed negative
Pressure, forces raw material cell wall moment to rupture, and accelerates intracellular protein dissolving in extracting solution and diffusion effect
Rate, thus can effectively shorten extraction time, improve extraction efficiency；The inventive method has simple to operate,
Easily controllable, with low cost, extraction effect is preferable, and the feature such as can be mass-produced, and utilizes side of the present invention
Method, the extraction ratio of Lepidinm meyenii Walp crude protein is 10%～14%.
Detailed description of the invention
Below in conjunction with the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Ground describes, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole realities
Execute example.Based on the embodiment in the present invention, those of ordinary skill in the art are not before making creative work
Put the every other embodiment obtained, broadly fall into the scope of protection of the invention.
Embodiment 1
A kind of extracting method of Lepidinm meyenii Walp crude protein, step includes:
(1) superfine grinding: selected Lepidinm meyenii Walp raw material 100kg dries after cleaning, and carries out superfine grinding after section,
Prepared fineness is the pueraria root powder of 10 mesh；
(2) alkali is molten: adds NaOH solution 1000kg that concentration is 1mol/L in pueraria root powder and dissolves, and profit
7.5 are maintained by this alkaline solution regulation pH of mixed；
(3) supersound extraction: mixed liquor adds supersound extraction tank and extracts 20min, and supersound extraction power is 660W,
Extracting temperature 70 degree；
(4) centrifugation: remixing liquid after supersound extraction and be centrifuged separating 15min, centrifuge speed is
3400r/min；
(5) filter: filter after centrifugation, collect filtrate, add salt acid for adjusting pH extremely neutrality,
After static 15min, recentrifuge separates, and centrifuge speed is 3400r/min, and curdled milk is Lepidinm meyenii Walp crude protein
12kg。
Embodiment 2
A kind of extracting method of Lepidinm meyenii Walp crude protein, step includes:
(1) superfine grinding: Lepidinm meyenii Walp raw material 50kg dries after cleaning, and carries out superfine grinding after section, prepares
Fineness is the pueraria root powder of 20 mesh；
(2) alkali is molten: adds NaOH solution 1200kg that concentration is 1mol/L in pueraria root powder and dissolves,
And utilize this alkaline solution regulation pH of mixed to maintain 9.5；
(3) supersound extraction: mixed liquor adds supersound extraction tank and extracts 60min, and supersound extraction power is 460W,
Extracting temperature 60 degree；
(4) centrifugation: remixing liquid after supersound extraction and be centrifuged separating 17min, centrifuge speed is
3400r/min；
(5) filter: filter after centrifugation, collect filtrate, add salt acid for adjusting pH extremely neutrality,
After static 15min, recentrifuge separates, and centrifuge speed is 3400r/min, and curdled milk is Lepidinm meyenii Walp albumen
6.5kg。
Embodiment 3
A kind of extracting method of Lepidinm meyenii Walp crude protein, step includes:
(1) superfine grinding: Lepidinm meyenii Walp raw material 200kg dries after cleaning, and carries out superfine grinding after section, prepares
Fineness is the pueraria root powder of 20 mesh；
(2) alkali is molten: adds NaOH solution 10000kg that concentration is 1mol/L in pueraria root powder and dissolves,
And utilize this alkaline solution regulation pH of mixed to maintain 11.5；
(3) supersound extraction: mixed liquor adds supersound extraction tank and extracts 100min, and extraction power is 660W,
Temperature 70 degree；
(4) centrifugation: remixing liquid after supersound extraction and be centrifuged separating 20min, centrifuge speed is
3400r/min；
(5) filter: filter after centrifugation, collect filtrate, add salt acid for adjusting pH extremely neutrality,
After static 15min, recentrifuge separates, and centrifuge speed is 3400r/min, and curdled milk is Lepidinm meyenii Walp protein 25 kg.
Those skilled in the art of the present technique are appreciated that unless otherwise defined, all terms used herein (bag
Include technical term and scientific terminology) have and being commonly understood by of the those of ordinary skill in art of the present invention
Identical meaning.Should also be understood that those terms defined in such as general dictionary should be understood that
There is the meaning consistent with the meaning in the context of prior art, and unless defined as here, no
Meeting idealization or the most formal implication are explained.
One of ordinary skill in the art will appreciate that: the parts in device in embodiment can be according to embodiment
Describe in the device being distributed in embodiment, it is also possible to carry out respective change and be disposed other than one of the present embodiment
Or in multiple device.The parts of above-described embodiment can merge into parts, it is also possible to is further split into
Multiple subassemblies.
It should be noted last that: above example only in order to illustrative not limiting technical scheme,
Although being described in detail the present invention with reference to above-described embodiment, those of ordinary skill in the art should manage
Solve: still the present invention can be modified or equivalent, without departing from the spirit and scope of the present invention
Any modification or partial replacement, it all should be contained in the middle of scope of the presently claimed invention.
Claims (9)
1. the extracting method of a Lepidinm meyenii Walp crude protein, it is characterised in that step includes:
(1) superfine grinding: Lepidinm meyenii Walp raw material dries after cleaning, and carries out superfine grinding after section, prepares pueraria root powder；
(2) alkali is molten: the alkaline solution adding its weight 10～50 times of weight in pueraria root powder extracts, and utilizes
This alkaline solution regulation pH of mixed maintains 7.5～11.5；
(3) supersound extraction: mixed liquor adds supersound extraction tank and extracts 20～100min；
(4) centrifugation: remix liquid after supersound extraction and be centrifuged separating 15～20min；
(5) filter: filter after centrifugation, collect filtrate, add salt acid for adjusting pH extremely neutrality,
After static 15min, recentrifuge separates, and curdled milk is Lepidinm meyenii Walp crude protein.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (1)
In, the fineness of described pueraria root powder is 10～20 mesh.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (2)
In, described alkaline solution is NaOH, and concentration is 1mol/L.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (3)
In, described supersound extraction power is 260W～660W, the temperature 50 of described supersound extraction～70 degree.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (4)
In, described centrifugation centrifuge speed is 3400r/min.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (5)
In, described centrifugation centrifuge speed is 3400r/min.
The extracting method of Lepidinm meyenii Walp crude protein the most according to claim 1, it is characterised in that step (5)
In, the mass concentration adding hydrochloric acid is 1mol/L.
8. the Lepidinm meyenii Walp crude protein prepared by method described in any one of claim 1-7.
The Lepidinm meyenii Walp crude protein that the most according to claim 8, prepared by method application in food.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610270797.6A CN105941819A (en) | 2016-04-27 | 2016-04-27 | Extraction method of maca crude proteins |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610270797.6A CN105941819A (en) | 2016-04-27 | 2016-04-27 | Extraction method of maca crude proteins |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105941819A true CN105941819A (en) | 2016-09-21 |
Family
ID=56916701
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610270797.6A Pending CN105941819A (en) | 2016-04-27 | 2016-04-27 | Extraction method of maca crude proteins |
Country Status (1)
| Country | Link |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103275012A (en) * | 2013-06-08 | 2013-09-04 | 中国科学院过程工程研究所 | Preparation method and application of Maca alkaloid |
| CN103918965A (en) * | 2013-01-15 | 2014-07-16 | 北京同仁堂健康药业股份有限公司 | Physical fatigue alleviating beverage |
| CN104688796A (en) * | 2015-02-04 | 2015-06-10 | 广东长兴生物科技股份有限公司 | Method for extracting maca bioactive components based on ultrasonic wave |
| CN105192723A (en) * | 2015-07-01 | 2015-12-30 | 中国科学院过程工程研究所 | Maca dietary fiber as well as preparation method and application thereof |
-
2016
- 2016-04-27 CN CN201610270797.6A patent/CN105941819A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103918965A (en) * | 2013-01-15 | 2014-07-16 | 北京同仁堂健康药业股份有限公司 | Physical fatigue alleviating beverage |
| CN103275012A (en) * | 2013-06-08 | 2013-09-04 | 中国科学院过程工程研究所 | Preparation method and application of Maca alkaloid |
| CN104688796A (en) * | 2015-02-04 | 2015-06-10 | 广东长兴生物科技股份有限公司 | Method for extracting maca bioactive components based on ultrasonic wave |
| CN105192723A (en) * | 2015-07-01 | 2015-12-30 | 中国科学院过程工程研究所 | Maca dietary fiber as well as preparation method and application thereof |
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Application publication date: 20160921 |