CN100531744C - Method for extracting active components of ginseng by mechanical means - Google Patents
Method for extracting active components of ginseng by mechanical means Download PDFInfo
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- CN100531744C CN100531744C CNB2005800113865A CN200580011386A CN100531744C CN 100531744 C CN100531744 C CN 100531744C CN B2005800113865 A CNB2005800113865 A CN B2005800113865A CN 200580011386 A CN200580011386 A CN 200580011386A CN 100531744 C CN100531744 C CN 100531744C
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- 241000208340 Araliaceae Species 0.000 title claims abstract description 92
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 title claims abstract description 92
- 235000003140 Panax quinquefolius Nutrition 0.000 title claims abstract description 92
- 235000008434 ginseng Nutrition 0.000 title claims abstract description 92
- 238000000034 method Methods 0.000 title claims abstract description 41
- 239000000843 powder Substances 0.000 claims abstract description 54
- 239000008187 granular material Substances 0.000 claims abstract description 9
- 239000002245 particle Substances 0.000 claims abstract description 9
- 239000003814 drug Substances 0.000 claims description 16
- 229940079593 drug Drugs 0.000 claims description 16
- 230000018044 dehydration Effects 0.000 claims description 4
- 238000006297 dehydration reaction Methods 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 4
- 239000000084 colloidal system Substances 0.000 claims description 2
- 238000003801 milling Methods 0.000 abstract description 7
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 15
- 229930182490 saponin Natural products 0.000 description 15
- 150000007949 saponins Chemical class 0.000 description 15
- 238000000926 separation method Methods 0.000 description 12
- 235000019750 Crude protein Nutrition 0.000 description 9
- 238000000605 extraction Methods 0.000 description 9
- 230000002378 acidificating effect Effects 0.000 description 8
- 150000004676 glycans Chemical class 0.000 description 8
- 238000000227 grinding Methods 0.000 description 8
- 229920001282 polysaccharide Polymers 0.000 description 8
- 239000005017 polysaccharide Substances 0.000 description 8
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000003818 cinder Substances 0.000 description 5
- 235000012054 meals Nutrition 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 238000004904 shortening Methods 0.000 description 3
- 238000000638 solvent extraction Methods 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical class CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 229940107131 ginseng root Drugs 0.000 description 2
- 239000012925 reference material Substances 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 238000007696 Kjeldahl method Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- AEMOLEFTQBMNLQ-UHFFFAOYSA-N beta-D-galactopyranuronic acid Natural products OC1OC(C(O)=O)C(O)C(O)C1O AEMOLEFTQBMNLQ-UHFFFAOYSA-N 0.000 description 1
- AEMOLEFTQBMNLQ-DTEWXJGMSA-N beta-D-galacturonic acid Chemical compound O[C@@H]1O[C@H](C(O)=O)[C@H](O)[C@H](O)[C@H]1O AEMOLEFTQBMNLQ-DTEWXJGMSA-N 0.000 description 1
- 231100000693 bioaccumulation Toxicity 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 125000004464 hydroxyphenyl group Chemical group 0.000 description 1
- -1 m-hydroxyphenyl Chemical group 0.000 description 1
- OQUKIQWCVTZJAF-UHFFFAOYSA-N phenol;sulfuric acid Chemical compound OS(O)(=O)=O.OC1=CC=CC=C1 OQUKIQWCVTZJAF-UHFFFAOYSA-N 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
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- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05B—ELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
- H05B6/00—Heating by electric, magnetic or electromagnetic fields
- H05B6/64—Heating using microwaves
- H05B6/6408—Supports or covers specially adapted for use in microwave heating apparatus
- H05B6/6411—Supports or covers specially adapted for use in microwave heating apparatus the supports being rotated
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/01—Instant products; Powders; Flakes; Granules
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- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Medicines Containing Plant Substances (AREA)
Abstract
The present invention relates to a method of processing ginseng and extracting active components therefrom; more specifically, a method of extracting active components of ginseng by mechanical means of milling and air-classifying dehydrated ginseng via a mill and an air classification system, respectively. The constitution of the present invention includes: a process of placing the dehydrated ginseng into a crude mill and obtaining ginseng granules having 60~80mesh of fineness; a process of placing thus obtained granules into a single track jet mill to obtain hyperfine ginseng powder with its particles having a size of 1~100 mum; a process of air-classifying thus obtained powder in an air classification system to produce a powder with its particles having a size of 1~9 mum.
Description
Technical field
The present invention relates to Radix Ginseng is processed to extract the method for active component from Radix Ginseng; More specifically, the present invention relates to use grinding machine to milling through the Radix Ginseng of dehydration and the Radix Ginseng through milling being carried out selecting crude drugs with winnower and from Radix Ginseng, extract the method for active component by mechanical means with aidr bells blast system.
Background technology
After Garrigues in 1854 isolated panaxcoside, the scientific research of relevant Radix Ginseng had obtained comprehensively carrying out.Particularly the main component saponin of panaxcoside has become the focus of research; Correspondingly, the various products that contain saponin have obtained positive exploitation and sale.
In addition, along with the growth of the sale of the various products that contain constituent of ginseng, the productivity's that improves the Radix Ginseng product interest is also being increased.That is to say that along with increasing of the various products that contain the Radix Ginseng active component that come into the market, providing at a low price, the Radix Ginseng product has become main market strategy.For this reason, the method for minimizing Radix Ginseng production cost has obtained deep research.
Yet although to improving the research that the method for extracting the efficient of active component from Radix Ginseng continues, research worker does not also propose any effective method.Extracting the method that active component adopted at present from Radix Ginseng is hydrothermal solution extraction method or organic solvent extraction method.
The shortcoming of hydrothermal solution extraction method and organic solvent extraction method is: complex manufacturing, and production cost can not significantly be reduced, and this is because the constituent of ginseng waste material contains the active component of utmost point low content.
In addition, study improving the method for from Radix Ginseng, extracting the efficient of active component by the extraction conditions in the control said method.Yet the effort of adopting these methods to improve extraction efficiency has reached their limit; Therefore, study shortening extraction time.
In case develop the active component required time is extracted in shortening from Radix Ginseng method, just can obviously reduce the Radix Ginseng production cost of products; Yet the result does not also have extremely successful.
Therefore, press for the active component required time is extracted in shortening from Radix Ginseng the method for developing.
Summary of the invention
Technical problem to be solved
The present inventor has made great efforts to solve existing problem in the prior art; As a result, they propose to use grinding machine and aidr bells blast system to obtain to contain the simple and rapid method of Radix Ginseng powder of the Radix Ginseng active component of high percentage ratio.
Formation of the present invention comprises: will put into kibbling mill and obtain the operation that fineness is 60～80 purpose ginseng granules through the Radix Ginseng of dehydration; The granule of gained is sent in the single track aeropulverizer (single trackjet mill) and obtained the operation that particle size is the hyperfine Radix Ginseng powder of 1 μ m～100 μ m; And the Radix Ginseng powder to gained carries out selecting crude drugs with winnower and produces the hyperfine Radix Ginseng powder that particle size is 1 μ m～9 μ m in aidr bells blast system.
To put into kibbling mill and can provide superfine Radix Ginseng powder to the operation that the granule that so obtains carries out selecting crude drugs with winnower through the Radix Ginseng of dehydration at aidr bells blast system, described superfine Radix Ginseng powder contains polysaccharide acid (polysaccharide acid), total sugar, crude protein of high concentration etc., also contains the main component saponin of Radix Ginseng simultaneously; Therefore, this will shorten the extraction required time of active component from Radix Ginseng.
Formation to the grinding machine (kibbling mill) of granulation Radix Ginseng has no particular limits, but preferably uses such as grinding machines such as needle mill, impact mill, roller mill, vibratory bowl or colloid mills.In addition, the ginseng granules of milling is also had no particular limits with the formation of the single track aeropulverizer that obtains hyperfine Radix Ginseng powder, but preferably use such as aeropulverizer or vibratory bowl grinding machine grinding machines such as (vibratory bowl mill).
These millings and selecting crude drugs with winnower operation can be used as series interlocking operation and are undertaken by automatization.
With different such as existing methods such as hydrothermal solution extraction method and organic solvent extraction methods, the present invention extracts active component from Radix Ginseng method allows to use kibbling mill, single track aeropulverizer and aidr bells blast system to come carrying out rapid extraction such as Radix Ginseng active component such as saponin, acidic polysaccharose (acid polysaccharide), total sugar, crude protein.
The specific embodiment
Extracting the method for Radix Ginseng active component can further explain by following embodiment by the mechanical means with above-mentioned formation.
Provide these embodiment to come the present invention is explained in more detail, and, according to main points of the present invention, it will be apparent to those of ordinary skill in the art that scope of the present invention is not limited to these embodiment.
Embodiment
Embodiment 1
At first; Radix Ginseng to life in 6 years dewaters; take by weighing 4.5kg and do not comprise the Radix Ginseng of its upper end; being granulated into fineness in needle mill is about 60～80 purpose granules; promoting pressure and 0.7MPa with 2.0 kilograms/hour charging rate at 0.7MPa then mills under the condition of pressure in single track aeropulverizer (Alpine, Germany) to described particle grinding once.Adopt granularity analyser (LMS-30, Seishin, Japan) that the particles of powder degree of the gained of milling by electricity is measured, intermediate value granularity (median granularity) is X
10=2.511 μ m, X
50=7.789 μ m and X
90=25.245 μ m.
Then, in aidr bells blast system (Alpine, Germany) with 6,500rpm (rev/min), 5,000rpm, 3,500rpm and 2, the separation wheel of 000rpm (classification wheel) speed is to 4, the hyperfine Radix Ginseng powder of 341.6g carries out selecting crude drugs with winnower.That is to say, it is 6 that described hyperfine Radix Ginseng powder is put into separation wheel speed, in the aidr bells blast system of 500rpm, and fine powder that will be by separation wheel (6,500F) with unsanctioned corase meal (6,500C) separate, with 5, the speed of 000rpm puts on described corase meal then, will be by the described fine powder of taking turns (5,000F) with unsanctioned corase meal (5,000C) separate, then with 3, the speed of 500rpm puts on described 5, the 000C powder, will by described fine powder of taking turns (3,500F) with unsanctioned corase meal (3,500C) separate, then with 2, it is described 3 that the speed of 000rpm puts on, and the 500C powder will be by the described fine powder of taking turns (2,000F) with unsanctioned corase meal (2,000C) separate (seeing: table 1).
[table 1]
The selecting crude drugs with winnower condition
| Carry out the number of times of sorting | 1 | 2 | 3 | 4 |
| Processing capacity (kilogram/hour) | 2.5 | 2.3 | 2.8 | 3.0 |
| Separation velocity (rpm) | 6,500 | 5,000 | 3,500 | 2,000 |
| Pressure reduction (mmAq) | 300 | 300 | 280 | 300 |
| Air-supply equipment (Hz) | 54.5 | 56.4 | 60.1 | 60.5 |
| Running time (hour) | 100 | 100 | 75 | 50 |
The analysis result of the granularity of the Radix Ginseng powder by the selecting crude drugs with winnower gained under the condition of last table 1 is as shown in table 2.
[table 2]
The granularity analysis of Radix Ginseng powder
As above shown in the table 2, these results show that particle size increases with the reduction of separation velocity.
Then, by the AOAC method basis of above-mentioned Radix Ginseng powder through sorting is carried out quantitatively.Measure moisture by 105 ℃ of air dryings; Measure crude protein content by semimicro-Kjeldahl method; Come cinder content is carried out quantitatively by 550 ℃ of incinerations; Carbohydrate content is for getting rid of back remaining surpluses such as moisture, crude protein, cinder.Use without the Radix Ginseng powder of sorting and organize (seeing: table 3) in contrast.
Basis content (unit: weight %) through the Radix Ginseng powder of sorting
| Sample | Moisture | Cinder | Carbohydrate | Crude protein |
| Matched group | 6.72 | 4.36 | 76.21 | 15.22 |
| 2,000C | 6.43 | 4.20 | 76.77 | 14.49 |
| 3,500C | 6.25 | 4.17 | 77.55 | 14.58 |
| 5,000C | 6.39 | 4.27 | 77.66 | 14.42 |
| 6,500C | 6.85 | 4.34 | 76.11 | 14.66 |
| 2,000F | 6.13 | 4.42 | 77.88 | 14.19 |
| 3,500F | 6.01 | 4.44 | 76.68 | 15.37 |
| 5,000F | 5.38 | 4.81 | 73.65 | 18.27 |
| 6,500F | 5.54 | 5.04 | 71.51 | 20.99 |
As shown in table 3, crude protein and cinder tend to 5, and 000F and 6,500F obtain separating; Particularly 6, the crude protein concentration of 500F is up to 1.38 times of matched group concentration, and this shows active component enrichment by selecting crude drugs with winnower of Radix Ginseng, and depends on separation velocity through the content of the active component of enrichment.
Through the polysaccharide of the Radix Ginseng powder of sorting and the content analysis of saponin
Use glucose total sugar content to be measured by the phenol sulfuric acid process as reference material.Use β-D-galacturonic acid acidic polysaccharose content to be measured by a hydroxy phenyl method (m-hydroxyphenyl method) as reference material.
According to the method for analyzing constituent of ginseng, the 1g sample dissolution in the 80 volume % methanol of 30ml, is extracted and vacuum drying, thereby obtained powder, then described powder dissolution is extracted in distilled water and with ether, thereby obtain aqueous layer.Then, the aqueous layer that so obtains with butanols extraction, thereby obtain classified butanols, vacuum drying and obtain powder, with this powder dissolution in 50ml methanol and obtain wherein 100 μ l.
In the gained sample, 8 volume % vanillin-alcoholic solution of 300 μ l are mixed with the sulphuric acid of the 72 volume % of 4ml, measure the absorbance at 545nm place then and carry out quantitatively after 10 minutes 60 ℃ of colour developings.Employing is without the Radix Ginseng powder of the sorting matched group (seeing Table 4) as this method.
[table 4]
Through the polysaccharide of the Radix Ginseng powder of sorting and the content (unit: mg/g) of saponin
| Sample | Acidic polysaccharose | Saponin | Total sugar |
| Matched group | 18.98 | 27.33 | 275.22 |
| 2,000C | 16.99 | 24.89 | 252.01 |
| 3,500C | 17.77 | 21.15 | 251.33 |
| 5,000C | 18.12 | 26.55 | 265.42 |
| 6,500C | 18.79 | 26.01 | 271.33 |
| 2,000F | 19.46 | 24.98 | 269.25 |
| 3,500F | 20.43 | 28.21 | 315.22 |
| 5,000F | 24.37 | 41.23 | 377.43 |
| 6,500F | 29.34 | 48.55 | 431.22 |
The same with in the table 3, table 4 also shows acidic polysaccharose, saponin and total sugar content 6,500F is highly enriched.Compare with matched group, the acidic polysaccharose of institute's enrichment is up to 1.54 times, and saponin is up to 1.78 times, and total sugar is up to 1.57 times.Therefore, by control selecting crude drugs with winnower condition, the more effectively active component of enrichment Radix Ginseng.
Embodiment 2
Improve the establishment of the sorting condition of the Radix Ginseng powder amount of returning
The foregoing description 1 shows can be by the active component of selecting crude drugs with winnower enrichment Radix Ginseng.Yet 6, the Radix Ginseng powder amount that 500F and 5,000F obtain only is 9.5 weight % of used Radix Ginseng; Therefore, we attempt to improve the amount of returning of described powder.
That is, with 4, the hyperfine Radix Ginseng powder that 895g adopts embodiment 1 method milling with the method for embodiment 16,000rpm selecting crude drugs with winnower 2 times, 5,000rpm selecting crude drugs with winnower 2 times and 3, the 500rpm selecting crude drugs with winnower once (is seen: table 5).
When measuring the granularity of above-mentioned hyperfine Radix Ginseng powder, the intermediate value granularity is as follows: X
10=2.511 μ m, X
50=7.789 μ m and X
90=25.245 μ m.
[table 5]
The selecting crude drugs with winnower condition
| Carry out the number of times of sorting | 1 | 2 | 3 | 4 | 5 |
| Processing capacity (kilogram/hour) | 2.5 | 2.3 | 2.9 | 3.0 | 3.5 |
| Separation velocity (rpm) | 6,000 | 6,000 | 5,000 | 5,000 | 3,500 |
| Pressure reduction (mmAq) | 310 | 270 | 245 | 230 | 210 |
| Air-supply equipment (Hz) | 60 | 60 | 60 | 60 | 60 |
| Running time (hour) | 110 | 70 | 60 | 45 | 50 |
Result with the granularity of the methods analyst Radix Ginseng powder of embodiment 1 is as shown in table 6.
[table 6]
The granularity analysis of Radix Ginseng powder
As above shown in the table 6,4 times selecting crude drugs with winnower has obtained 1, and the Radix Ginseng fine powder of 110g accounts for the about 22.7 weight % through the Radix Ginseng powder of sorting.
Method by embodiment 1 is measured the content through content, polysaccharide and the saponin of the basis of the Radix Ginseng powder of sorting, and the result is respectively shown in table 7 and table 8.
[table 7]
Basis content (unit: weight %) through the Radix Ginseng powder of sorting
| Sample | Moisture | Cinder | Carbohydrate | Crude protein |
| Matched group | 8.25 | 4.69 | 77.11 | 14.55 |
| The first time 6,000F | 4.79 | 4.51 | 76.44 | 19.88 |
| The second time 6,000F | 5.09 | 4.65 | 76.45 | 19.35 |
| The first time 5,000F | 4.78 | 4.75 | 78.79 | 16.66 |
| The second time 5,000F | 5.10 | 4.48 | 79.23 | 15.86 |
| 3,500F | 5.54 | 4.49 | 79.79 | 14.34 |
| The first time 6,000C | 6.38 | 4.23 | 79.34 | 13.99 |
| The second time 6,000C | 6.18 | 4.49 | 79.67 | 13.22 |
| The first time 5,000C | 6.19 | 4.42 | 79.89 | 13.44 |
| The second time 5,000C | 6.39 | 4.39 | 79.87 | 13.25 |
| 3,500C | 5.92 | 4.29 | 80.79 | 13.02 |
[table 8]
Through the polysaccharide of the Radix Ginseng powder of sorting and the content (unit: mg/g) of saponin
| Sample | Acidic polysaccharose | Saponin | Total sugar |
| Matched group | 16.38 | 34.38 | 229.67 |
| The first time 6,000F | 29.14 | 63.05 | 405.01 |
| The second time 6,000F | 27.87 | 51.28 | 399.22 |
| The first time 5,000F | 23.46 | 45.99 | 340.84 |
| The second time 5,000F | 21.79 | 40.50 | 317.30 |
| 3,500F | 16.67 | 34.88 | 277.35 |
| The first time 6,000C | 19.24 | 36.45 | 274.52 |
| The second time 6,000C | 18.78 | 34.69 | 261.35 |
| The first time 5,000C | 18.01 | 33.21 | 258.27 |
| The second time 5,000C | 18.22 | 30.19 | 249.12 |
| 3,500C | 17.45 | 30.00 | 241.44 |
As above shown in table 7 and the table 8, these results show the content of content, polysaccharide and saponin of the basis of Radix Ginseng 6,000F and 5,000F enrichment; Particularly 6,000F, the acidic polysaccharose of institute's enrichment up to about 1.78 times, saponin up to about 1.83 times, total sugar is up to about 1.76 times, this show described active component in this Radix Ginseng powder than the more effectively enrichment in the Radix Ginseng powder of sorting that in embodiment 1, obtains.
According to the abovementioned embodiments of the present invention 1 and 2, when be of a size of 1 μ m～Radix Ginseng powder of 100 μ m in aidr bells blast system with 5,000rpm～6, when 500rpm carried out sorting, the active component of Radix Ginseng obtained the most effective enrichment; Yet the above-mentioned separation wheel speed of aidr bells blast system depends on the size of this aidr bells blast system.
That is, have the aidr bells blast system that is different from the used size of the embodiment of the invention if use, then the separation velocity of separation wheel (rpm) will change according to the size of this aidr bells blast system.
For example, if adopt the aidr bells blast system that has greater than the used size of the present invention, even be lower than the separation wheel speed that the foregoing description 1 and 2 is adopted so, also can obtaining wherein, the active component of Radix Ginseng obtains the Radix Ginseng powder that the most effective enrichment is of a size of 1 μ m～9 μ m; If adopt the aidr bells blast system that has less than the used size of the present invention, so adopted faster than the foregoing description 1 and 25,000rpm～6, the speed of 500rpm, can obtaining wherein, the active component of Radix Ginseng obtains the Radix Ginseng powder that the most effective enrichment is of a size of 1 μ m～9 μ m.
To be limited in 1 μ m～9 μ m through the granularity of the Radix Ginseng powder of aidr bells blast system sorting, this is because reach 9 μ m or when bigger, the bioaccumulation efficiency of Radix Ginseng active component can reduce when the granularity through the Radix Ginseng powder of sorting.
In this, by using aidr bells blast system rather than separating and the Radix Ginseng powder that obtains to be of a size of 1 μ m～9 μ m is important by control separation wheel speed.
Industrial applicibility
Explain in detail and description such as above-mentioned institute, the present invention make by the dry method of utilizing grinding machine and aidr bells blast system rather than wet method obtain containing high level the ginseng active component hyperfine Ginseng Root Powder simple and easy and fast method become easily, described ginseng active component is such as being saponin(e, acidic polysaccharose, total reducing sugar and crude protein etc.; Therefore, the present invention can be widely used for improving use by the productivity of the various Ginseng Products of the Ginseng Root Powder of its gained.
Claims (2)
1. extract the method for the active component of Radix Ginseng by mechanical means, described method comprises: will put into kibbling mill and obtain the operation that fineness is 60～80 purpose ginseng granules through the Radix Ginseng of dehydration; The granule that so obtains is put into the single track aeropulverizer and obtained the operation that particle size is the hyperfine Radix Ginseng powder of 1 μ m～100 μ m; In aidr bells blast system, the powder that so obtains is carried out selecting crude drugs with winnower and obtains the operation that particle size is the powder of 1 μ m～9 μ m.
2. the method for claim 1 is characterized in that, described kibbling mill is a kind of in needle mill, impact mill, roller mill, vibratory bowl or the colloid mill.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020040028878A KR100577032B1 (en) | 2004-04-27 | 2004-04-27 | Method for Extracting Active Components of Ginseng by Mechanical Means |
| KR1020040028878 | 2004-04-27 |
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|---|---|
| CN1942109A CN1942109A (en) | 2007-04-04 |
| CN100531744C true CN100531744C (en) | 2009-08-26 |
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| CNB2005800113865A Expired - Fee Related CN100531744C (en) | 2004-04-27 | 2005-04-27 | Method for extracting active components of ginseng by mechanical means |
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| Country | Link |
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| KR (1) | KR100577032B1 (en) |
| CN (1) | CN100531744C (en) |
| WO (1) | WO2005112666A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100855897B1 (en) * | 2007-01-15 | 2008-09-03 | 주식회사 케이티앤지 | Ultra-Fine Powders of Ginseng or Red Ginseng |
| KR100833996B1 (en) * | 2008-01-16 | 2008-05-30 | 주식회사 한국인삼공사 | Production method of ginseng steamed red nano-powder under micron size |
| KR101061258B1 (en) | 2008-05-21 | 2011-09-01 | 강원대학교산학협력단 | Shredding Method of Ginseng Powder to Improve Ginsenoside Extraction Efficiency |
| KR101576093B1 (en) * | 2015-06-09 | 2015-12-21 | (주)다정 | Manufacturing method of functional nanoparticle for maximizing absorption rate in the body and the nanoparticle made by the method |
| KR102000662B1 (en) * | 2018-10-18 | 2019-07-16 | (주)옥천당 | Production method of red ginseng concentrate with enhanced content of prosapogenin |
| KR102332777B1 (en) * | 2019-11-12 | 2021-11-30 | 경희대학교 산학협력단 | Method for preparing medicine herb extract using ball mill |
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| KR950024677A (en) * | 1994-02-24 | 1995-09-15 | 서중일 | Method of Making Barley Young Leaf Powder (Granules) |
| KR19980046598A (en) * | 1996-12-13 | 1998-09-15 | 남승우 | Method of manufacturing red ginseng granules containing red ginseng soluble ingredients and extracted ginseng |
| KR100303169B1 (en) * | 1998-10-22 | 2001-12-17 | 김길환 | Cold water soluble powder green tea and preparation method thereof |
| TWI298643B (en) * | 2002-05-17 | 2008-07-11 | wei-ren Zhuang |
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Non-Patent Citations (4)
| Title |
|---|
| 含人参皂苷类超微饮片与其传统饮片的化学对比研究. 徐华建等.中国实验方剂学杂志，第8卷第5期. 2002 |
| 含人参皂苷类超微饮片与其传统饮片的化学对比研究. 徐华建等.中国实验方剂学杂志，第8卷第5期. 2002 * |
| 超微人参粉粒度及分布测定. 张建平等.齐齐哈尔大学学报，第21卷第1期. 2005 |
| 超微人参粉粒度及分布测定. 张建平等.齐齐哈尔大学学报，第21卷第1期. 2005 * |
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| KR100577032B1 (en) | 2006-05-08 |
| KR20050103629A (en) | 2005-11-01 |
| CN1942109A (en) | 2007-04-04 |
| WO2005112666A1 (en) | 2005-12-01 |
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