CN101524672A - Cyclone separator and spore separation device therewith - Google Patents
Cyclone separator and spore separation device therewith Download PDFInfo
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- CN101524672A CN101524672A CN 200910097391 CN200910097391A CN101524672A CN 101524672 A CN101524672 A CN 101524672A CN 200910097391 CN200910097391 CN 200910097391 CN 200910097391 A CN200910097391 A CN 200910097391A CN 101524672 A CN101524672 A CN 101524672A
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- 238000000926 separation method Methods 0.000 title claims abstract description 46
- 238000007789 sealing Methods 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims description 14
- 239000004744 fabric Substances 0.000 claims description 11
- 239000007787 solid Substances 0.000 abstract description 19
- 238000000855 fermentation Methods 0.000 abstract description 10
- 230000004151 fermentation Effects 0.000 abstract description 10
- 230000002538 fungal effect Effects 0.000 abstract description 10
- 239000000843 powder Substances 0.000 description 26
- 239000002245 particle Substances 0.000 description 25
- 230000000694 effects Effects 0.000 description 9
- 230000006872 improvement Effects 0.000 description 8
- 239000002609 medium Substances 0.000 description 7
- 241000233866 Fungi Species 0.000 description 6
- 241000751139 Beauveria bassiana Species 0.000 description 5
- 241000223261 Trichoderma viride Species 0.000 description 5
- 241000209094 Oryza Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
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- 238000005096 rolling process Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000001963 growth medium Substances 0.000 description 3
- 239000002917 insecticide Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 240000005979 Hordeum vulgare Species 0.000 description 2
- 235000007340 Hordeum vulgare Nutrition 0.000 description 2
- 241000223250 Metarhizium anisopliae Species 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
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- 241000254043 Melolonthinae Species 0.000 description 1
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- 238000001574 biopsy Methods 0.000 description 1
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- 238000013461 design Methods 0.000 description 1
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- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/10—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by centrifugation ; Cyclones
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/44—Means for regulation, monitoring, measurement or control, e.g. flow regulation of volume or liquid level
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Abstract
The invention discloses a cyclone separator, comprising a primary separator and a secondary separator (8) which are communicated by a channel (9), the bottom of the primary separator is connected with a primary collection tube (6), the bottom of the secondary separator is connected with a secondary collection tube (7); the top surface of the primary separator is provided with an air outlet channel (2), the side wall of the primary separator is tangentially provided with an air inlet channel (1), the air outlet channel (2) and the air inlet channel (1) are both communicated with the inner cavity of the primary separator; an air volume regulator (10) is arranged inside the air inlet channel (1), and the channel (9) is positioned below the air inlet channel (1). The invention also discloses a spore separation device with the cyclone separator, wherein a blower component (300) is connected with the air outlet channel (2) in a sealing way, and a swirling flow feeder component (200) is connected with the air inlet channel (1) in a sealing way. The spore separation device of the invention can efficiently separate solid fermentation fungal spore.
Description
Technical field
The present invention relates to a kind of cyclone separator and the spore separation device that has this cyclone separator.
Background technology
Fungus insecticide (Mycoinsecticides) be develop in the world in recent years very rapid, effectively infect the quasi-microorganism pesticide of body (being generally gas living spore estranged) with biocontrol fungi (Fungalbiocontrol agents) as active ingredient; Wherein the purity of conidial powder and quality are directly connected to quality, shelf life and the field effect (whether blocking sprayer and good disinsection effect) of spore preparation (as finish, suspension emulsion etc.); In addition because the impure quality problems such as too much of conidia powder cause China's fungus insecticide Industrialization Progress slow; Therefore need separating high-purity and high-quality conidia powder efficiently, just can push forward the fast development of fungus insecticide industry comprehensively.
The method of existing separating solids particulate material is usually based on cyclonic separation.Because fungal spore particle diameter small (diameter is often less than 10 microns), easily be suspended in the air at separation process miospore powder, be difficult to sedimentation and collection, therefore need utilize the centrifugal force of air-flow to reach the effect of separation.Shortcomings such as labour intensity was big when the screen cloth separation method had screening, the separation rear impurity is many.Centrifugal separation method is owing to spore and the disengaging fully of solid fermentation culture medium particle, so can make separation efficient low.And filter separation method to the performance requirement of filtrate all than higher, be easy to cause the excessive separating effect that influences of filtration resistance in the separation process.
The gas powder of fungal spore separates employing filtrate method in the separator of the patent No. 87107268, but the logical resistance of its Dual-Phrase Distribution of Gas olid is big, and energy consumption is also bigger.The fungal spore separator of the patent No. 01275732.2, earlier the solid medium particle is pulverized in the separation chamber, to be suspended in the conidia powder importing cyclone separator of top, separation chamber with circulating current then, and utilize the rotating centrifugal separation to carry out Dual-Phrase Distribution of Gas olid again and separate with the technology that sack cleaner combines.The advantage of this equipment is simple in structure, and is better to the separating property of fine dust, but the dead angle that also occurs easily stirring, stirs energy consumption height and the big problem of cloth bag resistance when feeding quantity is big.The fungal spore separator of publication number 200510047737.x circulates solid particle material early stage in separation earlier, and fungal spore is fully separated with culture medium, utilizes contain spore air-flow the separated and collected spore of cyclone separator from introducing again.It is simple in structure, and separating rate is fast, and is also more thorough to the separation of fine dust.Abroad other cyclone separator general using fluid bed is with the solid fermentation culture medium particle spore separation surperficial with it; spore is imported in the cyclone separator of a plurality of parallel connections with air-flow then; to increase work efficiency; but also be owing to can not solve the escape problem of spore usually, still need set up protective device.The employed cyclone dust collectors of above-mentioned these patents are applicable to that generally purification is greater than the non-sticky of 5-10 micron, the dried dust of non-fiber; But when spore after the fragmentation of separating solids fermentate and mycelia, always there are both problems that is difficult to separate mixed in together in the whirlwind process, are being mingled with the mycelia fragment in the final feasible conidia powder of collecting, have a strong impact on the purity of conidia powder.
Summary of the invention
The technical problem to be solved in the present invention provides the cyclone separator of a kind of separative efficiency height, safe and low consumption and has the spore separation device of this cyclone separator.
In order to solve the problems of the technologies described above, the invention provides a kind of cyclone separator, comprise the main separator and the secondary separator that rely on passage to be connected, the bottom of main separator connects main surge drum, the bottom auxiliary connection surge drum of secondary separator; End face at main separator is provided with the air-out passage, and air intake passage tangentially is set on the sidewall of main separator, air-out passage and air intake passage all with the intracavity inter-connection of main separator; Be provided with blast regulator in the air intake passage, passage is positioned under the air intake passage.
Improvement as cyclone separator of the present invention: main separator comprises cylindrical body and the cone that is connected successively from top to bottom, end face in cylindrical body is provided with the air-out passage, air intake passage tangentially is set on the sidewall of cylindrical body, air-out passage and air intake passage all with the intracavity inter-connection of cylindrical body; Cylindrical body relies on passage to be connected with secondary separator, in the junction of cylindrical body and cone the ring wing is set, and passage is positioned on the ring wing.
Further improvement as cyclone separator of the present invention: air intake passage is beloid passage, and the narrow end of air intake passage tangentially links to each other with the sidewall of cylindrical body.
Further improvement as cyclone separator of the present invention: cone is up big and down small inversion shape cone, and the upper end of cone links to each other with cylindrical body.
Further improvement as cyclone separator of the present invention: the air-out passage is L-shaped, and the lower end of air-out passage is arranged in the inner chamber of cylindrical body, and the lower end of this air-out passage is positioned under the air intake passage and is positioned on the passage.
The present invention also provides the spore separation device that has above-mentioned cyclone separator simultaneously, comprises fan assembly and eddy flow feeder assembly; Fan assembly links to each other with the air-out channel seal, and eddy flow feeder assembly links to each other with the air intake passage sealing.
Improvement as spore separation device of the present invention: eddy flow feeder assembly comprises the eddy flow feeder of hollow, at the end face of eddy flow feeder discharging opening is set, and charging aperture tangentially is set on the sidewall of eddy flow feeder; Discharging opening links to each other with the air intake passage sealing.
Further improvement as spore separation device of the present invention: be provided with screen cloth in the eddy flow feeder, screen cloth is between discharging opening and charging aperture.
Further improvement as spore separation device of the present invention: fan assembly comprises fan box, is provided with air inlet and exhaust outlet on fan box, is provided with blower fan in fan box; Air inlet links to each other with the air-out channel seal.
Further improvement as spore separation device of the present invention: be provided with filter in the fan box, filter bits is between air inlet and blower fan.
Adopt spore separation device of the present invention to carry out the solid fermentation fungal spore separation method, its operation logic is: contain spore solid medium particle and rotate at a high speed and mutual frictional impact along barrel in the eddy flow feeder, because the gravity effect, particle can not enter in the cyclone separator by discharging opening; And after conidia powder that particle surface adheres to and mycelia fully break away from particle, can tangentially enter in the main separator (being cyclone separator) by discharging opening and air intake passage successively with air-flow.Owing to selected the cyclone separator that improves design according to vortex pair air-flow principle for use, the air-flow that therefore contains conidia powder and mycelia is when acquisition rotatablely moves, and air-flow separately forms the vortex pair motion up and down, forms two air rings up and down.Produce strong centrifugation at the vortex pair boundary, thicker mycelia particle enters secondary separator by passage with descending vortical flow to be separated to the inwall (being the inwall of cylindrical body) of main separator behind the barrier effect of the ring wing, enter secondary surge drum at last.Conidia powder is brought main surge drum into by downward air-flow.
In the present invention, utilize blast regulator to adjust air velocity, thereby regulate air quantity, can make more thorough that conidia powder that particle surface adheres to and mycelia break away from.
The present invention can be used for separating the fungal spore that fermentation backs such as the green green muscardine fungus of chafer, Trichoderma viride, beauveria bassiana produce.
Spore separation device of the present invention has following beneficial effect: (1) safe and low consumption: whole system is airtight, separates thoroughly, and purification filtering is complete, operation environment safety, energy-conservation (general power is 1.4kw); (2) simple in structure: critical piece is eddy flow feeder assembly, cyclone separator and fan assembly; (3) apparatus structure compactness, area occupied is little, and for example floor space only is 1000 * 500 * 1200mm.Adopting spore separation device of the present invention to carry out solid fermentation fungal spore separates, have the following advantages: the efficient separation, separating rate is fast: by the master, the setting of secondary separator, can be with the separating substances and the collection of Different Weight, for example mycelia can be separated respectively with spore and collect, improved the collection purity of spore, make the separation purity height.
Description of drawings
Below in conjunction with accompanying drawing the specific embodiment of the present invention is described in further detail.
Fig. 1 is the schematic diagram after the cyclone separator biopsy cavity marker devices of the present invention;
Fig. 2 is the partial schematic diagram of overlooking of Fig. 1;
Fig. 3 is the structural representation of spore separation device of the present invention;
Fig. 4 is the rotation schematic diagram that A-A cuts open among Fig. 3.
The specific embodiment
End face in cylindrical body 3 is provided with the air-out passage 2 that stainless steel is made, and this air-out passage 2 is L-shaped, and air-out passage 2 is fixedly linked hermetically with the end face of cylindrical body 3, and the lower end 11 of air-out passage 2 is arranged in the inner chamber of cylindrical body 3.Be provided with otch on the sidewall of cylindrical body 3, this otch parallels with the tangent line of cylindrical body 3 sidewalls, and this otch is near the end face of cylindrical body 3; The air intake passage of being made by stainless steel 1 is a beloid passage, and the cut sealing ground on the narrow end of this air intake passage 1 and cylindrical body 3 sidewalls is connected; This air intake passage 1 is perpendicular to the sidewall of cylindrical body 3, thus tangential the linking to each other and the intracavity inter-connection of air intake passage 1 and cylindrical body 3 of having realized air intake passage 1 and cylindrical body 3 sidewalls.Be provided with blast regulator 10 in the air intake passage 1.The lower end 11 of air-out passage 2 is positioned at the lower end of air intake passage 1, and promptly the lower end 11 of air-out passage 2 is lower than the otch on cylindrical body 3 sidewalls.In the junction of cylindrical body 3 and cone 5 the ringwise ring wing 4 is set.The bottom of cone 5 links to each other with main surge drum 6.
Eddy flow feeder assembly 200 comprises the eddy flow feeder 22 that being of hollow is cylinder-shaped, at the end face of eddy flow feeder 22 discharging opening 20 is set; Be provided with otch on the sidewall of eddy flow feeder 22, this otch parallels with the tangent line of eddy flow feeder 22 sidewalls, and this otch is near the bottom surface of eddy flow feeder 22; Cut sealing ground on charging aperture 23 and eddy flow feeder 22 sidewalls is connected, and this charging aperture 23 is perpendicular to the sidewall of eddy flow feeder 22; Thereby tangential the linking to each other and the intracavity inter-connection of charging aperture 23 and eddy flow feeder 22 of having realized charging aperture 23 and eddy flow feeder 22 sidewalls.Be provided with screen cloth 21 in eddy flow feeder 22, screen cloth 21 is between discharging opening 20 and charging aperture 23; Be that screen cloth 21 is positioned on the charging aperture 23, under the discharging opening 20.Discharging opening 20 links to each other with air intake passage 1 sealing by connecting leg 42.The bottom surface of eddy flow feeder 22 relies on screw thread to link to each other with the sidewall of eddy flow feeder 22.
Utilize spore separation device of the present invention to carry out solid fermentation fungal spore and separate, its course of work is specific as follows:
1, will contain spore solid medium oven dry and its rolling loose into particle; Granular size generally is controlled in the 10mm.And the above-mentioned container that contains spore solid medium particle (hereinafter to be referred as particle) will be housed link to each other with charging aperture 23.
Start blower fan 32 by control components and parts 34, the suction that utilizes blower fan 32 to produce, above-mentioned particle enters in the eddy flow feeder 22 with tangential direction through charging aperture 23 with air-flow.Can pass through blast regulator 10, thereby change air velocity, air velocity generally is controlled at 8.5～44.5 meter per seconds.
2, particle barrel along eddy flow feeder 22 in eddy flow feeder 22 rotates at a high speed and mutual frictional impact, conidia powder and mycelia enter in the cylindrical body 3 with tangential direction through screen cloth 21, discharging opening 20, connecting leg 42 and air intake passage 1 after breaking away from from particle successively.
Particle can't rise to discharging opening 20 under the effect of gravity, and screen cloth 21 also plays the effect that stops that particle rises.
3, conidia powder and mycelia enter in the cylindrical body 3 with tangential direction and further separate, and be specific as follows:
The air-flow that contains conidia powder and mycelia is when acquisition rotatablely moves, and air-flow separately forms the vortex pair motion up and down, forms two air rings up and down.Produce strong centrifugation at the vortex pair boundary, thicker mycelia particle enters secondary separator 8 by passage 9 with descending vortical flow to be separated to the inwall of cylindrical body 3 behind the barrier effect of the ring wing 4, enter secondary surge drum 7 at last.Most conidia powder are brought main surge drum 6 into by downward air-flow.
The conidia powder of few part along with air-flow successively through air-out passage 2, connecting leg 41, air inlet 30, and then discharged through exhaust outlet by blower fan 32 through after the filtration of filter 31.The effect of filter 31 is to avoid entering in the extraneous air-flow being mingled with conidia powder.
4, when no longer including conidia powder and mycelia in the eddy flow feeder 22 and kick up, can close blower fan 32, thereby finish separation process because of whirlwind.Open the spiral cover of eddy flow feeder 22 bottoms, outwell remaining particle.
Test one, from the barley solid medium, separate Metarhizium anisopliae:
Claim 324.4 grams dried Metarhizium anisopliae ARSEF 576 barley solid fermentation culture mediums (water content 8% ± 1%), rolling is loose into particle and is placed in the clean container; Adopt above-mentioned separation method, utilize blast regulator 10 to adjust air velocity to 20.9 meter per second earlier.
Separate carry out 30 seconds after, adjust air velocity to 40 meter per second, purpose be make conidia powder and mycelia from particle break away from more thorough.The air velocity that keeps 40 meter per seconds separated 1 minute again; Close blower fan 32, finish whole mask work.
(spore content is: 0.61 ± 0.15 * 10 to obtain 12.7 gram muscardine spore powder at main surge drum 6
11/ gram powder), adopt the back that suspends to detect with the blood counting chamber method.In secondary surge drum 7, obtain 2.6 gram green muscardine fungus mycelia.
Experiment two: from the rice solid medium, separate Trichoderma viride:
Claim 832 grams dried Trichoderma viride CICC 40495 rice solid fermentation culture mediums (water content 7.5% ± 1%), rolling is loose into particle and is placed in the clean container, adopts above-mentioned separation method, adjusts air velocity to 20 meter per second.After separation is carried out 1 minute, close blower fan 32, finish whole mask work.
(spore content is: 0.63 ± 0.01 * 10 to obtain 15 gram Trichoderma viride conidia powder in main surge drum 6
11/ gram powder).In secondary surge drum 7, obtain 12 gram Trichoderma viride mycelia.
Experiment three: from the rice solid medium, separate beauveria bassiana
Claim 354.2 grams dried beauveria bassiana ARSEF 734 rice solid fermentation culture mediums (water content 7.4% ± 1%), rolling is loose into particle and is placed in the clean container, adopts above-mentioned separation method, adjusts air velocity to 12.9 meter per second earlier.After separation is carried out 1 minute; Close blower fan 32, finish whole mask work.
(spore content is: 1.73 ± 0.05 * 10 to obtain 5.4 gram beauveria bassiana conidia powder in main surge drum 6
11/ gram powder).In secondary surge drum 7, obtain 0.4 gram beauveria bassiana mycelia.
At last, it is also to be noted that what more than enumerate only is several specific embodiments of the present invention.Obviously, the invention is not restricted to above embodiment, many distortion can also be arranged.All distortion that those of ordinary skill in the art can directly derive or associate from content disclosed by the invention all should be thought protection scope of the present invention.
Claims (10)
1, a kind of cyclone separator is characterized in that: comprise the main separator and the secondary separator (8) that rely on passage (9) to be connected, the bottom of main separator connects main surge drum (6), the bottom auxiliary connection surge drum (7) of secondary separator (8); End face at main separator is provided with air-out passage (2), and air intake passage (1) tangentially is set on the sidewall of main separator, described air-out passage (2) and air intake passage (1) all with the intracavity inter-connection of main separator; Be provided with blast regulator (10) in the air intake passage (1), passage (9) is positioned under the air intake passage (1).
2, cyclone separator according to claim 1, it is characterized in that: described main separator comprises cylindrical body (3) and the cone (5) that is connected successively from top to bottom, end face in cylindrical body (3) is provided with air-out passage (2), air intake passage (1) tangentially is set on the sidewall of cylindrical body (3), air-out passage (2) and air intake passage (1) all with the intracavity inter-connection of cylindrical body (3); Cylindrical body (3) relies on passage (9) to be connected with secondary separator (8), and the ring wing (4) is set in the junction of cylindrical body (3) and cone (5), and passage (9) is positioned on the ring wing (4).
3, cyclone separator according to claim 2 is characterized in that: described air intake passage (1) is beloid passage, and the narrow end of described air intake passage (1) tangentially links to each other with the sidewall of cylindrical body (3).
4, according to claim 2 or 3 described cyclone separators, it is characterized in that: described cone (5) is up big and down small inversion shape cone, and the upper end of described cone (5) links to each other with cylindrical body (3).
5, cyclone separator according to claim 4, it is characterized in that: described air-out passage (2) is L-shaped, the lower end (11) of air-out passage (2) is arranged in the inner chamber of cylindrical body (3), and the lower end (11) of this air-out passage (2) is positioned under the air intake passage (1) and is positioned on the passage (9).
6, have the spore separation device of any one cyclone separator in the claim 1～5, it is characterized in that: comprise fan assembly (300) and eddy flow feeder assembly (200); Described fan assembly (300) links to each other with air-out passage (2) sealing, and eddy flow feeder assembly (200) links to each other with air intake passage (1) sealing.
7, spore separation device according to claim 6, it is characterized in that: described eddy flow feeder assembly (200) comprises the eddy flow feeder (22) of hollow, end face at eddy flow feeder (22) is provided with discharging opening (20), and charging aperture (23) tangentially is set on the sidewall of eddy flow feeder (22); Described discharging opening (20) links to each other with air intake passage (1) sealing.
8, spore separation device according to claim 7 is characterized in that: be provided with screen cloth (21) in the eddy flow feeder (22), described screen cloth (21) is positioned between discharging opening (20) and the charging aperture (23).
9, according to claim 7 or 8 described spore separation devices, it is characterized in that: described fan assembly (300) comprises fan box (33), on fan box (33), be provided with air inlet (30) and exhaust outlet, in fan box (33), be provided with blower fan (32); Air inlet (30) links to each other with air-out passage (2) sealing.
10, spore separation device according to claim 9 is characterized in that: be provided with filter (31) in the described fan box (33), filter (31) is positioned between air inlet (30) and the blower fan (32).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910097391 CN101524672B (en) | 2009-04-13 | 2009-04-13 | Cyclone separator and spore separation device therewith |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200910097391 CN101524672B (en) | 2009-04-13 | 2009-04-13 | Cyclone separator and spore separation device therewith |
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| CN101524672A true CN101524672A (en) | 2009-09-09 |
| CN101524672B CN101524672B (en) | 2010-09-08 |
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| CN 200910097391 Expired - Fee Related CN101524672B (en) | 2009-04-13 | 2009-04-13 | Cyclone separator and spore separation device therewith |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101878701A (en) * | 2010-08-10 | 2010-11-10 | 无锡五芝源生物农业科技有限公司 | Ganoderma lucidum spore collector |
| CN102225394A (en) * | 2011-04-29 | 2011-10-26 | 杨国旺 | Wind separating screen device and separating method thereof |
| CN102965277A (en) * | 2012-11-27 | 2013-03-13 | 北京市西山试验林场 | Cross-flow type cyclone-cloth bag combined dust collector system for bio-active spore powder |
| CN103962249A (en) * | 2013-01-29 | 2014-08-06 | 昆山尚达智机械有限公司 | Cyclone separator |
| WO2015066954A1 (en) * | 2013-11-07 | 2015-05-14 | 中国科学院天津工业生物技术研究所 | Solid-state biological reaction device and method for preparing filamentous fungus spores by using same |
| CN104630049A (en) * | 2015-01-23 | 2015-05-20 | 中国科学院合肥物质科学研究院 | Full-automatic separation device and separation method of solid fermentation fungus spores |
| CN105907646A (en) * | 2016-04-29 | 2016-08-31 | 上海理工大学 | Preparation method of antrodia camphorata conidial powder and antrodia camphorata grain powder |
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