CN102728489A - Self-drive centrifugal cyclone wet/dry water-powder-air separator - Google Patents
Self-drive centrifugal cyclone wet/dry water-powder-air separator Download PDFInfo
- Publication number
- CN102728489A CN102728489A CN2012101925566A CN201210192556A CN102728489A CN 102728489 A CN102728489 A CN 102728489A CN 2012101925566 A CN2012101925566 A CN 2012101925566A CN 201210192556 A CN201210192556 A CN 201210192556A CN 102728489 A CN102728489 A CN 102728489A
- Authority
- CN
- China
- Prior art keywords
- wet
- division board
- self
- cone
- plate
- 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.)
- Granted
Links
- 239000000843 powder Substances 0.000 claims abstract description 49
- 238000000926 separation method Methods 0.000 claims abstract description 35
- 238000007790 scraping Methods 0.000 claims abstract description 12
- 238000001238 wet grinding Methods 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 34
- 239000000049 pigment Substances 0.000 claims description 24
- 239000012530 fluid Substances 0.000 claims description 8
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 238000002955 isolation Methods 0.000 claims description 2
- 238000003466 welding Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- 239000000203 mixture Substances 0.000 abstract description 7
- 238000001914 filtration Methods 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 1
- 239000003570 air Substances 0.000 description 25
- 239000000428 dust Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- 239000002245 particle Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 238000004064 recycling Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 241001417527 Pempheridae Species 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
Images
Landscapes
- Cyclones (AREA)
Abstract
The invention discloses a self-drive centrifugal cyclone wet/dry water-powder-air separator, comprising a cylindrical outer barrel, an air outlet arranged on the outer barrel, a liquid outlet, a central collecting port, a wet powder outlet, a dry powder outlet and a wet powder collecting plate in the inner cavity, a lower separator, a dry powder collecting plate, a middle separator, an upper separator and a lower support plate, wherein a self-drive rotary scraping cone connected with a bearing is arranged above the lower support plate, a water filtration cone connected with the wet powder collecting plate and the central hole of the self-drive rotary scraping cone is arranged below the lower separator, a spiral channel is formed between the self-drive rotary scraping cone and the water filtration cone, four inverted cone cyclone separators and a round distributor with an X-shaped guide plate are arranged between the middle separator and the upper separator, the lower end of the round distributor is provided with the dry powder collecting plate, and the centers of the upper ends of the four cyclone separators are respectively provided with exhaust pipes. The invention is suitable for separating wet/dry water-powder-air mixtures with high separation efficiency.
Description
Technical field
The present invention relates to a kind of centrifugal cyclone Wet-dry pigment air separation of self drive.The water dust that it both can be used as wet and dry road sweeper separates use, also can be used for industry and goes up needs respectively with the water in the pigment gas mixture, wet-milling, the gentle separation of dry powder, can be widely used in fields such as environmental protection dedusting, industry water gas solid separation.
Background technology
At present, cyclone separator is to be well known, and has obtained extensive use in industrial gas solid separation and environmental protection dedusting field.In this device, have the inside that the air of powder is tangentially introduced the cyclonic separation body, the form circumferential flow is moving in the shape of a spiral around the inner surface of cyclonic separation body for air; Powder is separated from primary air under action of centrifugal force; And fall into the bottom of cyclonic separation body, and the air of cleaning leaves separator through the central gas outlet of cyclonic separation body, like patent: ZL00817415.6; ZL02135539.8 and ZL97197594.9; The characteristics of these cyclone separators are that under the effect of blower fan, it can (be called for short the powder that gets in the cyclone separator: dust) from air-flow, separate.They are not suitable for the separation of moisture pigment gas mixture, in separation process, can't water, dust and air three be separated respectively, just can't realize the purpose of waste water recycling yet.Can carry out the separation of pigment gas though the patent No. is 201110141791.6 patented technology, separate not thoroughly, especially be deposited in the conical surface at pigment, cleaning is inconvenient on the one hand, influences separating effect on the other hand, does not reach the purpose of high efficiency separation.
Summary of the invention
The objective of the invention is provides a kind of centrifugal cyclone Wet-dry pigment air separation of self drive in order to overcome above-mentioned existing separator to the halfway defective of water, powder and air separation.This pigment air separation can make full use of action of centrifugal force, efficiently water, powder and air is carried out in full force and effect separating, and on the other hand, realizes waste water recycling.
In order to achieve the above object, the technical scheme that adopted of technical solution problem of the present invention is:
A kind of centrifugal cyclone Wet-dry pigment air separation of self drive; Comprise cylindrical outer cylinder body 27; Be arranged on four back taper cyclone separators 26 in the cylindrical outer cylinder body 27, drainage awl 8, self-powered revolve to be scraped cone 10 and has the rounded dispensers 28 of Χ shape deflector; Described cylindrical outer cylinder body 27 top center are provided with exhaust outlet 1, and the bottom is provided with the mouth 15 that gathers materials; Lower supporting plate 12, the wet-milling that described cylindrical outer cylinder body 27 inwalls are connected with mutual isolation from bottom to top in turn gather materials plate 20, following gather materials plate 24, middle division board 4 and depart from the last division board 3 that is evenly equipped with four blast pipes 2 on the center circumferential of division board 23, dry powder; Wherein said wet-milling gathers materials and offers leakage fluid dram 17 on the wall of the cylindrical outer cylinder body 27 in lower end between plate 20 and the described lower supporting plate 12; Described down division board 23 and said wet-milling gather materials and offer wet-milling on the wall of the cylindrical outer cylinder body 27 in lower end between the plate 20 and export 21; Division board 4 and said dry powder gather materials and offer dry powder on the wall of the cylindrical outer cylinder body 27 in lower end between the plate 24 and export 6 in described; Plane Installation has the bearing 25 of coaxial line on the described division board 23 down, and lower plane is equipped with the clear powder cutter 7 of coaxial line; Described lower supporting plate 12 has some through holes; And be provided with on last plane to revolve and scrape the annular convex 13 that annular guide channel 14 that cone 10 lower surfaces are provided with matches with said self-powered; Said self-powered revolves to be scraped cone 10 outer surfaces and is connected with spiral scraper 9 and turbine 18 from top to bottom in turn, and it is matched that the gather materials centre bore and the bearing 25 of plate 20 and following division board 23 of wet-milling passed in its upper end; Match with annular convex 13 through annular guide channel 14 in the lower end; Said self-powered revolves to be scraped cone 10 skins and also is provided with the upper end and passes gather materials plate 20 and being connected of wet-milling; The drainage of the coaxial line that the lower end is connected with lower supporting plate 12 awl 8, offer on the said drainage awl 8 awl walls some treatment holes and and cylindrical outer cylinder body 27 inwalls between form a up big and down small toroidal cavity; Said self-powered revolve scrape offer on the cone 10 lower ends awls wall some dirt hole 16 and and said drainage awl 8 between formation one helical duct; The position of radially corresponding turbine 18 is provided with a tangential air admission hole 11 on the wall of said drainage awl 8 and said cylindrical outer cylinder body 27; Have on the division board 4 in described four with said on be used to install the hole of four coaxial lines of blast pipe 2 on the division board 3; Be equipped with between division board 4 and the last division board 3 in described respectively and be conical back taper cyclone separator 26 and have the rounded dispensers 28 of Χ shape deflector with four up big and down small middle parts that middle division board 4 is connected with last division board 3; Rounded dispensers 28 with Χ shape deflector has otch below last division board 3, tangentially communicate with four back taper cyclone separators 26 respectively; The center, upper end of described four back taper cyclone separators 26 respectively is provided with the blast pipe 2 that is connected with last division board 3.
Above-mentioned described leakage fluid dram 17, wet-milling outlet 21 and dry powder outlet 6 top separately offer corresponding first observation panel 19, second observation panel 22 and the 3rd observation panel 5.
The position of the treatment hole of offering on the above-mentioned described drainage awl 8 awl walls is that the lower end is higher than turbine 18, and the upper end is higher than dirt hole 16;
The above-mentioned described welding that is connected to.
The bottom surface of above-mentioned described cylindrical outer cylinder body 27 is that one to have inverted cone planar, and the vertex of a cone has the center that has lid and gathers materials mouthfuls 15.
Above-mentioned described spiral scraper 9 tops have otch.
A kind of advantage from the centrifugal cyclone Wet-dry pigment air separation that drives of the present invention mainly is:
Form a self-powered between the cone and revolve the structure of scraping the spiral tube because air inlet, the drainage of device awl and self-powered revolve to scrape, the pigment dirt in this spiral barrel structure gets into self-powered through air inlet and revolves and scrapes in the cone helical cavity that taper becomes with drainage, under the flow air effect; Revolve through the turbine drive self-powered and to scrape cone rotation, self-powered revolves the rotation of scraping cone can produce centrifugal force, and pigment dirt is scraped the cone rotation and received centrifugal action along with revolving; Water is gone up aperture owing to receive centrifugal action in the cavity of being thrown between outer cylinder body and the drainage awl through the drainage awl; Discharged by discharge outlet, solid particle then is deposited on the inner surface of drainage awl, revolves up the spinning along the spiral tube of spiral scraper effect of scraping on the cone through self-powered and moves; The distance of spiral scraper and drainage awl is very little; Effectively advance with the assurance dust, in separation process, because self-powered revolves the effect of scraping cone along the scraper direction of rotation; Centrifugal force to particle and moisture generation is bigger, can separate by the wet-milling that density is bigger.
Along with air-flow continues to move upward, dry powder is through disappearing the whirlpool passage, and it is inner to get into four small-sized back taper cyclone separators arranging by circular symmetry by the rounded dispensers tangential with Χ shape deflector.Because the blast pipe diameter of these four small-sized cyclone separators is less, air velocity is accelerated, and wherein particle receives centrifugal force equally, once more particle is separated.In this process once more with air-flow in remaining dry powder separate.
The present invention is applicable to the separation of moisture pigment gas mixture, can water, wet-milling, dry powder and air be separated respectively efficiently, and waste water is reclaimed, and reaches the effect of waste water recycling.
Description of drawings
Fig. 1 is the structural representation of the centrifugal cyclone Wet-dry pigment air separation of self drive of the present invention.
Fig. 2 is the A-A cross section view of Fig. 1.
Fig. 3 is the B-B cross section view of Fig. 1.
Fig. 4 is the C-C cross section view of Fig. 1.
Among the figure: 1, exhaust outlet; 2, blast pipe; 3, division board under the back taper cyclone separator; 4, middle division board; 5, the 3rd observation panel, 6, dry powder outlet; 7, fixing clear powder cutter; 8, drainage awl; 9, spiral scraper; 10, self-powered revolves and scrapes cone; 11, air inlet; 12, lower supporting plate; 13, convex body; 14, annular guide channel; 15, the center mouth that gathers materials; 16, pass through the dirt hole; 17, leakage fluid dram; 18, turbine; 19, first observation panel; 20, the wet-milling plate that gathers materials; 21, wet-milling outlet; 22, second observation panel; 23, following division board; 24, the dry powder plate that gathers materials; 25, bearing; 26, back taper cyclone separator; 27, cylindrical outer cylinder body; 28, the rounded dispensers that has Χ shape deflector.
The specific embodiment
Further specify below in conjunction with accompanying drawing and the specific embodiment centrifugal cyclone Wet-dry pigment air separation self drive of the present invention.
Shown in accompanying drawing 1; A kind of centrifugal cyclone Wet-dry pigment air separation of self drive is made up of four parts, and first is cylindrical outer cylinder body, and second portion is for scraping the pigment separation from driving to revolve; Third part is for scraping dried, wet-milling separation from driving to revolve, and the 4th part is that whirlwind dry powder separates.First: the cylindrical shell welded top of cylindrical outer cylinder body 27 has circular row gas port 1, and the bottom is welded with circular leakage fluid dram 17, air inlet 11 and center and gathers materials mouthfuls 15, and leakage fluid dram 17 tops are welded with observation panel 19; Be welded with the dry powder plate 24 that gathers materials respectively at cylindrical shell middle part, dry powder outlet 6, the wet-milling plate 20 that gathers materials, wet-milling outlet 21, dry powder outlet 6 exports 21 tops with wet-milling and is welded with observation panel 5 and 22 respectively.Second portion: drive certainly to revolve and scrape separator and mainly revolve and scrape cone 10 and turbine 18 is formed by cylindrical outer cylinder body 27 inwalls, drainage awl 8, self-powered; Drainage awl 8 welds together with cylindrical shell 27 bottoms; Self-powered revolves to be scraped cone 10 and welds together (shown in accompanying drawing 1) with turbine 18; Open the very little treatment hole of diameter above the drainage awl 8, self-powered revolves scrapes cone 10 lower ends and lower supporting plate 12 formation support relations.Third part: drive certainly to revolve and scrape dried wet-milling separation mainly by cylindrical outer cylinder body 27 inwalls; Spiral scraper 9 is formed with drainage awl 8, forms helical duct between drainage awl 8 and the spiral scraper 9, is welded with gather materials plate 20 and wet-milling of fixing clear powder cutter 7, wet-milling below the following division board 23 and exports 21; The upper end is fixed with bearing 25; Following division board 23 welds together with cylindrical outer cylinder body 27 inwalls, and distance is as far as possible little between spiral scraper 9 and the drainage awl 8, thereby makes dust mixture move upward along spiral scraper 9 direction of rotation; Get in cylindrical outer cylinder body 27 inner chambers wet-milling through the effect of fixing clear powder cutter 7 then and gather materials on the plate 20, discharge through wet-milling outlet 21; The 4th part (shown in accompanying drawing 2): rounded dispensers 28 bottoms with Χ shape deflector are provided with the dry powder plate 24 that gathers materials; And rounded dispensers 28 its inside with Χ shape deflector are separated into four separate space under the effect of Χ shape deflector, communicate with four back taper cyclone separators 26 respectively in the upper edge tangential direction; Four back taper cyclone separators 26 adopt turbulent structure to increase the effective area of dry powder passage; It is arranged by circular symmetry; Respectively with middle division board 4, go up division board 3 and weld together, and middle division board 4, go up division board 3 and weld together with cylindrical outer cylinder body 27 inwalls; The middle position and the last division board 3 of corresponding four back taper cyclone separators 26 weld together four blast pipes 2 respectively.
During work; The mixture that has water and dust is through air inlet 11; Blow turbine 18 (shown in accompanying drawing 4) thus driving self-powered revolves the rotation of scraping cone 10; The helical duct that water and dust mixture are bored formation between 8 along the rotation and the drainage of spiral scraper 9 moves upward by (shown in accompanying drawing 3), and water and dust shape motion in the shape of a spiral produce centrifugal force greatly, and water is then bored the treatment hole of opening above 8 through drainage and is discharged in the circular outer cylinder body 27.In this process; Water is separated and discharges through leakage fluid dram 17, and dust continues to move upward along spiral scraper 9, and it is indoor and through wet-milling outlet 21 discharges that wet-milling enters into down gather materials storage powder that plate 20 forms of division board 23 and wet-milling through the fixing clear powder cutter 7 in upper end; Dry powder then tangentially enters into four small-sized back taper cyclone separator 26 inside respectively with air-flow through the rounded dispensers 28 with Χ shape deflector; Produce rotary speed, dust is separated, and the powder of being separated by small-sized back taper cyclone separator 26 drops into by division board 23 is indoor with the storage powder that middle division board 4 forms down; Can be through the dry powder plate 24 that gathers materials; The powder that is scattered in down on the division board 23 is discharged by dry powder outlet 6, and the air-flow after the separation is discharged from exhaust outlet 1 then through blast pipe 2 then.Larger-diameter powder is scattering into the center and gathers materials mouthfuls 15, can open cover plate as required and clear up discharge, has the hole on the lower supporting plate 12, plays the supporting self-powered and revolves cone 10 effects of scraping.
Claims (7)
1. the centrifugal cyclone Wet-dry pigment air separation of a self drive; Comprise cylindrical outer cylinder body (27); Be arranged on four the back taper cyclone separators (26) in the cylindrical outer cylinder body (27); Drainage awl (8), self-powered revolves the rounded dispensers (28) of scraping cone (10) and having Χ shape deflector; Described cylindrical outer cylinder body (27) top center is provided with exhaust outlet (1), and the bottom is provided with gather materials mouthful (15); It is characterized in that: lower supporting plate (12), the wet-milling that described cylindrical outer cylinder body (27) inwall is connected with mutual isolation from bottom to top in turn gather materials plate (20), gather materials plate (24), middle division board (4) and depart from the last division board (3) that is evenly equipped with four blast pipes (2) on the center circumferential of division board (23), dry powder down; Wherein said wet-milling gathers materials and offers leakage fluid dram (17) on the wall of the cylindrical outer cylinder body in lower end (27) between plate (20) and the described lower supporting plate (12); Described down division board (23) and said wet-milling gather materials and offer wet-milling on the wall of the cylindrical outer cylinder body in lower end (27) between the plate (20) and export (21); Division board (4) and said dry powder gather materials and offer dry powder on the wall of the cylindrical outer cylinder body in lower end (27) between the plate (24) and export (6) in described; Described division board (23) is down gone up the bearing (25) that Plane Installation has coaxial line, and lower plane is equipped with the clear powder cutter (7) of coaxial line; Described lower supporting plate (12) has some through holes; And be provided with on last plane to revolve and scrape the annular convex (13) that annular guide channel (14) that cone (10) lower surface is provided with matches with said self-powered; Said self-powered revolves to be scraped cone (10) outer surface and is connected with spiral scraper (9) and turbine (18) from top to bottom in turn, and it is matched that the gather materials centre bore and the bearing (25) of plate (20) and following division board (23) of wet-milling passed in its upper end; Match with annular convex (13) through annular guide channel (14) in the lower end; Said self-powered revolves to be scraped cone (10) skin and also is provided with the upper end and passes gather materials plate (20) and being connected of wet-milling; The drainage of the coaxial line that the lower end is connected with lower supporting plate (12) awl (8), offer on said drainage awl (8) the awl wall some treatment holes and and cylindrical outer cylinder body (27) inwall between form a up big and down small toroidal cavity; Said self-powered revolve scrape offer on cone (10) the lower end awl wall some dirt hole (16) and and said drainage awl (8) between formation one helical duct; The position of radially corresponding turbine (18) is provided with a tangential air admission hole (11) on the wall of said drainage awl (8) and said cylindrical outer cylinder body (27); Have on the division board (4) in described four with said on be used to install the hole of four coaxial lines of blast pipe (2) on the division board (3); Be equipped with respectively between division board (4) and the last division board (3) in described and be conical back taper cyclone separator (26) and have the rounded dispensers (28) of Χ shape deflector with four up big and down small middle parts that middle division board (4) is connected with last division board (3); Rounded dispensers (28) with Χ shape deflector has otch in the below of last division board (3), tangentially communicates with four back taper cyclone separators (26) respectively; The center, upper end of described four back taper cyclone separators (26) respectively is provided with the blast pipe (2) that is connected with last division board (3).
2. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1; It is characterized in that: plate (20) and dry powder plate (24) arrangement that takes the form of inclined plane separately of gathering materials of gathering materials of described wet-milling, its inclined-plane low side separately are respectively the position that said wet-milling outlet (21) and said dry powder export (6).
3. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1 is characterized in that: described leakage fluid dram (17), wet-milling outlet (21) and dry powder export (6) top separately and offer corresponding first observation panel (19), second observation panel (22) and the 3rd observation panel (5).
4. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1 is characterized in that: the position of the treatment hole of offering on described drainage awl (8) the awl wall is that the lower end is higher than turbine (18), and the upper end is higher than dirt hole (16).
5. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1 is characterized in that: describedly be connected to welding.
6. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1 is characterized in that: the bottom surface of described cylindrical outer cylinder body (27) is that one to have inverted cone planar, and the vertex of a cone has the center that has lid gather materials mouthful (15).
7. the centrifugal cyclone Wet-dry pigment air separation of self drive according to claim 1 is characterized in that: have otch above the described spiral scraper (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101925566A CN102728489B (en) | 2012-06-12 | 2012-06-12 | Self-drive centrifugal cyclone wet/dry water-powder-air separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101925566A CN102728489B (en) | 2012-06-12 | 2012-06-12 | Self-drive centrifugal cyclone wet/dry water-powder-air separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102728489A true CN102728489A (en) | 2012-10-17 |
| CN102728489B CN102728489B (en) | 2013-12-04 |
Family
ID=46985198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101925566A Expired - Fee Related CN102728489B (en) | 2012-06-12 | 2012-06-12 | Self-drive centrifugal cyclone wet/dry water-powder-air separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102728489B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964226A (en) * | 2017-04-20 | 2017-07-21 | 江苏科技大学 | A kind of sack cleaner |
| CN107837973A (en) * | 2017-11-24 | 2018-03-27 | 无锡富岛科技股份有限公司 | A kind of cyclone separator |
| CN108273343A (en) * | 2018-03-05 | 2018-07-13 | 苏州双鑫华机械科技有限公司 | Gas-liquid separator |
| CN109682229A (en) * | 2018-12-29 | 2019-04-26 | 连云港利源电力节能设备有限公司 | A kind of stewing steam discharge cooling tower of steel slag hot |
| CN110017673A (en) * | 2019-04-26 | 2019-07-16 | 河南工业大学 | A kind of pneumatic conveying drying separator |
| CN116078214A (en) * | 2023-04-11 | 2023-05-09 | 四川省阳子森环保设备有限公司 | Efficient odorless washing wastewater treatment device and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002065532A (en) * | 2000-08-19 | 2002-03-05 | Lg Electronics Inc | Dust collector and vacuum cleaner using the same |
| CN2650881Y (en) * | 2003-07-25 | 2004-10-27 | 李成岳 | Dry and wet unitary dust remover |
| CN2709036Y (en) * | 2004-06-03 | 2005-07-13 | 陈书亚 | Powderless birotor powder selecting machine |
| JP2005224587A (en) * | 2004-02-11 | 2005-08-25 | Samsung Kwangju Electronics Co Ltd | Cyclone dust collecting device |
| CN201644250U (en) * | 2010-01-25 | 2010-11-24 | 中国矿业大学 | Three-product cyclone classifying screen |
| CN102228872A (en) * | 2011-05-30 | 2011-11-02 | 江苏科技大学 | Cyclone water-powder-air separator |
-
2012
- 2012-06-12 CN CN2012101925566A patent/CN102728489B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002065532A (en) * | 2000-08-19 | 2002-03-05 | Lg Electronics Inc | Dust collector and vacuum cleaner using the same |
| CN2650881Y (en) * | 2003-07-25 | 2004-10-27 | 李成岳 | Dry and wet unitary dust remover |
| JP2005224587A (en) * | 2004-02-11 | 2005-08-25 | Samsung Kwangju Electronics Co Ltd | Cyclone dust collecting device |
| CN2709036Y (en) * | 2004-06-03 | 2005-07-13 | 陈书亚 | Powderless birotor powder selecting machine |
| CN201644250U (en) * | 2010-01-25 | 2010-11-24 | 中国矿业大学 | Three-product cyclone classifying screen |
| CN102228872A (en) * | 2011-05-30 | 2011-11-02 | 江苏科技大学 | Cyclone water-powder-air separator |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106964226A (en) * | 2017-04-20 | 2017-07-21 | 江苏科技大学 | A kind of sack cleaner |
| CN107837973A (en) * | 2017-11-24 | 2018-03-27 | 无锡富岛科技股份有限公司 | A kind of cyclone separator |
| CN107837973B (en) * | 2017-11-24 | 2024-01-26 | 无锡富岛科技股份有限公司 | Cyclone separator |
| CN108273343A (en) * | 2018-03-05 | 2018-07-13 | 苏州双鑫华机械科技有限公司 | Gas-liquid separator |
| CN109682229A (en) * | 2018-12-29 | 2019-04-26 | 连云港利源电力节能设备有限公司 | A kind of stewing steam discharge cooling tower of steel slag hot |
| CN110017673A (en) * | 2019-04-26 | 2019-07-16 | 河南工业大学 | A kind of pneumatic conveying drying separator |
| CN110017673B (en) * | 2019-04-26 | 2024-04-26 | 郑州精华实业有限公司 | Air flow drying and separating device |
| CN116078214A (en) * | 2023-04-11 | 2023-05-09 | 四川省阳子森环保设备有限公司 | Efficient odorless washing wastewater treatment device and method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102728489B (en) | 2013-12-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102728489B (en) | Self-drive centrifugal cyclone wet/dry water-powder-air separator | |
| US7955405B2 (en) | Cyclonic separation apparatus | |
| CN102438496B (en) | Cyclone dust collector | |
| US7615088B2 (en) | Cyclonic separator for separating particles from an airflow and vacuum cleaner including such a separator | |
| US7955406B2 (en) | Cyclonic separation apparatus | |
| CN104668110B (en) | Starch milk dehydration horizontal screw centrifuge | |
| US20130105382A1 (en) | Disc filter | |
| CN104888972B (en) | A kind of solid-liquid separation centrifuge | |
| CN104905735A (en) | Cyclonic separation device | |
| CN110302617A (en) | A kind of efficient dust bubble deduster | |
| CN107072455A (en) | Dust catcher | |
| CN102228872B (en) | Cyclone water-powder-air separator | |
| CN108814421A (en) | Cyclone separation device and dust collector | |
| CN209186565U (en) | Cyclone separation device and dust collector | |
| CN209076931U (en) | A kind of thermosetting powder coating micro mist disintegrating apparatus cyclone separator | |
| CN207013103U (en) | Fluidized bed airflow grinding machine intelligence change system | |
| KR20200081866A (en) | solid matters discharging means provided with collector that includes multi- turning pocket | |
| CN202900590U (en) | Inlet filtering device for air compressor | |
| CN102327096A (en) | Dust cup for dust collector and dust collector | |
| CN113273924A (en) | Garbage separator and vacuum cleaner | |
| CN102172459A (en) | Rotary cyclone separator | |
| US1523611A (en) | Gas cleaner | |
| CN2336116Y (en) | Cone basket flat bar resistance filter centrifugal | |
| CN110075644A (en) | Dusty gas separator | |
| CN109647638A (en) | A kind of cyclone separator |
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 | ||
| CP02 | Change in the address of a patent holder |
Address after: 212028 Zhenjiang, Dantu Metro Industrial Park Rui East Road, No. 9 Patentee after: JIANGSU University OF SCIENCE AND TECHNOLOGY Address before: 212003 Zhenjiang City, Jiangsu province dream Creek Road, No. 2 Patentee before: Jiangsu University of Science and Technology |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131204 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |