CN106693760A - High speed dispersing device - Google Patents
High speed dispersing device Download PDFInfo
- Publication number
- CN106693760A CN106693760A CN201611143983.XA CN201611143983A CN106693760A CN 106693760 A CN106693760 A CN 106693760A CN 201611143983 A CN201611143983 A CN 201611143983A CN 106693760 A CN106693760 A CN 106693760A
- Authority
- CN
- China
- Prior art keywords
- dispersion
- dispersing
- wheel
- high speed
- intermediate layer
- 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.)
- Pending
Links
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000006185 dispersion Substances 0.000 claims description 130
- 238000007599 discharging Methods 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims 1
- 239000002002 slurry Substances 0.000 abstract description 34
- 239000002245 particle Substances 0.000 abstract description 11
- 230000008901 benefit Effects 0.000 abstract description 2
- 230000000903 blocking effect Effects 0.000 abstract 4
- 230000000694 effects Effects 0.000 description 10
- 239000002086 nanomaterial Substances 0.000 description 9
- 230000009471 action Effects 0.000 description 4
- 238000010008 shearing Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000005054 agglomeration Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002131 composite material Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 235000003283 Pachira macrocarpa Nutrition 0.000 description 1
- 241001083492 Trapa Species 0.000 description 1
- 235000014364 Trapa natans Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011982 device technology Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 235000009165 saligot Nutrition 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/181—Preventing generation of dust or dirt; Sieves; Filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/181—Preventing generation of dust or dirt; Sieves; Filters
- B01F35/187—Preventing generation of dust or dirt; Sieves; Filters using filters in mixers, e.g. during venting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/50—Mixing receptacles
- B01F35/53—Mixing receptacles characterised by the configuration of the interior, e.g. baffles for facilitating the mixing of components
- B01F35/532—Mixing receptacles characterised by the configuration of the interior, e.g. baffles for facilitating the mixing of components with guide tubes on the wall or the bottom
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention discloses a high speed dispersing device. The high speed dispersing device comprises a dispersing bucket, a main shaft, a dispersing wheel, a guide plate, a linking part, a feed blocking plate and a feed outlet chamber, the dispersing wheel is installed at the lower end of the main shaft, the upper end of the main shaft is connected to a driving device, the lower end of the dispersing bucket is provided with a feed inlet, the two ends of the guide plate are fixed above the feed inlet through the linking part, a feed passing hole is formed in the linking part, the feed blocking plate is in a circular shape, and is arranged above the dispersing wheel, the feed outlet chamber is located above the feed blocking plate, one side of the feed outlet chamber is provided with a feed outlet, the high speed dispersing device further comprises a dispersing middle layer, the dispersing middle layer is located between the dispersing bucket and the dispersing wheel, the upper end of the dispersing middle layer is fixed to the feed blocking plate, and the dispersing wheel and the dispersing middle layer are both provided with convection holes. The high speed dispersing device has the advantages that on the premise of not increasing the power of equipment, the dispersing middle layer is added, a slurry is dispersed among the dispersing bucket circularly, the dispersing middle layer and the dispersing wheel, a narrower particle size distribution range can be obtained, and the obtained nanometer material is even and stable, and can be stored for a long time.
Description
Technical field
The present invention relates to a kind of dispersal device, more particularly to a kind of high speed dispersing device.
Background technology
The every profession and trades such as new energy, chemical industry, coating, food, medical treatment, cosmetics, for the mixing between different nano materials,
All it is to be completed by dispersed with stirring device.The particle diameter very little of nano material, thus generally all have larger specific surface area and
Free energy higher, causes to be very easy to reunite between nano-grain.Aggregate it is general all with several times, decades of times,
Or even the form of 1,100 times of former nano-grain volumes is present.Compound tense is carried out in nano material and other materials, it is necessary to
Make it in other matrix materials in dispersed distribution, and this reunion existing way of nano-grain makes
It can not be effectively dispersed in matrix material, and the performance that not only making nano material has is difficult to play completely, and
The difficulty of working process is increased, would generally also negative impact be produced to the performance of composite, or even cause composite
The deterioration of performance.Therefore, obtain uniform and stable scattered nano material and seem most important.
Existing stirring at low speed device, is carried out in the container of barrel shape, and planet dispersion impeller, stirring are provided with container
Oar, carries out rotation while planet dispersion impeller revolves round the sun in agitator, agitating paddle is also carried out certainly while revolution in agitator
Turn.The planet dispersion impeller of rotation applies energy to slurry at a high speed disperses it, and agitating paddle is stirred to slurry makes its equal
It is even, but because the rotary speed of planet dispersion impeller and agitating paddle is relatively low, the material of reunion during dispersion impeller is scattered only
Only by the shear action of dispersion impeller, the shock between mutual rubbing action and material and size barrel bucket wall between material is made
With very little, so the dispersion of aggregate needs long time in slurry, scattered efficiency is very low, also there is certain in itself to material
Destruction, micronized effect is also very poor.
With updating for agitating device technology, also there are many patents on high-speed stirring apparatus at present.It is a kind of high
Fast dispersal device and equipment (country origin:China, publication number:205019987U, publication date:2016-02-10), slurry is disclosed
After bottom enters dispersion bucket, using the high speed rotation and the effect of striker plate of dispersion wheel, formation slurry is followed in dispersion bucket
Ring.Due to the centrifugal action of dispersion wheel, slurry can at a high speed depart from dispersion wheel outer wall, high-speed impact dispersion bucket wall.Slurry is at a high speed
Depart from wheel wall, vacuum can be formed in wheel wall surface moment, so slurry inside dispersion wheel can under vacuum through dispersion
Dispersion hole on wheel.Because the speed of service of slurry is very high, in 30 seconds that slurry is detained in the dispersion bucket, this suction, throw away,
Clash into, the process that return is sucked again can be repeated several times, and be compared with stirring at low speed device, substantially increase dispersion efficiency.But should
Device disperses also less thoroughly to nano material aggregate, does not reach preferable dispersion effect, it is impossible to be fully solved a nanometer material
Expect the agglomeration traits of particle, it is impossible to exist steadily in the long term, be unfavorable for storing and transport, significantly limit its range of application.
The content of the invention
Goal of the invention:Regarding to the issue above, it is an object of the invention to provide a kind of high speed dispersing device, nano material point is made
Dissipate thorough, solve the agglomeration traits of nano-grain, obtain uniform and stable scattered nano material.
Technical scheme:
A kind of high speed dispersing device, including dispersion bucket, main shaft, dispersion wheel, deflector, attachment, striker plate, discharge chamber,
The main shaft lower end and the dispersion wheel are installed, and the main shaft upper end connects drive device, the dispersion bucket lower end offer into
The charging aperture top is fixed in material mouth, the deflector two ends by the attachment, and punishment in advance is offered in the attachment
Hole, the striker plate is in annular, and located at the dispersion wheel top, the striker plate top is the discharge chamber, the discharging
The side of room offers discharging opening, and also including dispersion intermediate layer, the dispersion intermediate layer is located at the dispersion bucket and the dispersion
Between wheel, and its upper end is fixed with the striker plate, and convection holes are offered on the dispersion wheel and the dispersion intermediate layer,
A dispersion intermediate layer is set up between dispersion bucket and dispersion wheel, strengthens the circulation shear and high-speed impact of slurry.
Preferably, the dispersion intermediate layer is cylindrical, is set to and disperses wheel and dispersion bucket identical shape, convenient peace
Assembly and disassembly.
Preferably, the dispersion intermediate layer is that several piece arc plate or helical blade are circumferentially set, to by dispersion
The slurry of interbed carries out the shock and bounce-back of multi-angle, and dispersion effect is more preferable.
Preferably, it is equipped with the dispersion wheel inside and outside wall, dispersion intermediate layer inside and outside wall, the dispersion bucket inwall convex
Line, the burr is set to rhombus burr, annular knurl or car flower, further increases frictional force and shearing force of the slurry between three.
Preferably, the convection holes are manhole or waist through hole, and the convection holes set multiple, in longitudinally, laterally
Equidistantly arrangement.
Preferably, the convection holes that the dispersion intermediate layer is taken turns with the dispersion are often capable highly one on horizontally set position
Cause, further strengthen shear force, it is ensured that while dispersion effect, it is ensured that the mass output rate of slurry.
Other, the device also dynamic screen separators including annular, the annulus of the striker plate is fixed in upper end
On on shape inner ring, positioned at the dispersion wheel inner side, further screening meets the particle that dispersion requires particle diameter to dynamic screen separators,
The bad particle of dispersion effect returns to dispersion bucket and proceeds dispersion.
Beneficial effect:Compared with prior art, it is an advantage of the invention that on the premise of plant capacity is not increased, disperseing
Increase a dispersion intermediate layer between bucket and dispersion wheel, slurry is by after dispersion wheel shearing, again passing by cutting for dispersion intermediate layer
Cut, the dispersion effect of slurry is remarkably reinforced, slurry dispersion bucket, dispersion intermediate layer, dispersion wheel three between iterative cycles diffusion,
Clash into, and then disperse more thorough, can obtain narrower particle size distribution range, thus acquisition nano material evenly, it is more steady
It is fixed, efficiently solve the agglomeration traits of slurry, hence it is evident that improve the scattered efficiency of slurry, improve micronized effect.
Brief description of the drawings
Fig. 1 is half-sectional structural representation of the invention;
Fig. 2 is stereochemical structure profile of the invention;
Fig. 3 is the structural representation in the dispersion intermediate layer for being provided with manhole;
Fig. 4 is the structural representation in the dispersion intermediate layer for being provided with waist through hole;
Fig. 5 be provided with manhole, while be provided with rhombus burr dispersion intermediate layer plane outspread drawing;
Fig. 6 is rhombus burr enlarged diagram on dispersion bucket inwall;
Fig. 7 is the Section A-A schematic diagram of Fig. 6.
Specific embodiment
Below in conjunction with the accompanying drawings and specific embodiment, the present invention is furture elucidated, it should be understood that these embodiments are merely to illustrate
The present invention rather than limitation the scope of the present invention, after the present invention has been read, those skilled in the art are to of the invention each
The modification for planting the equivalent form of value falls within the application appended claims limited range.
As shown in accompanying drawing 1-2, a kind of high speed dispersing device, including dispersion bucket 1, main shaft 2, dispersion wheel 3, deflector 4, connection
It is portion 5, striker plate 6, discharge chamber 7, charging aperture 8, material path 9, discharging opening 10, dispersion intermediate layer 11, convection holes 12, burr 13, dynamic
State screen separators 14.
Installed in the center of dispersion bucket 1, the lower end of main shaft 2 is provided with dispersion wheel 3, upper end connection drive device driving point to main shaft 2
Dissipate 3 high-speed rotations of wheel, charging aperture 8 is opened in the lower end of dispersion bucket 1, and the two ends of deflector 4 are fixed with connecting portion 5, integral installation in
The top of charging aperture 8, offers material path 9 in attachment 5, striker plate 6 is annular, and dispersion bucket 1 is installed on through the side of main shaft 2
Bucket wall on, positioned at the top of dispersion wheel 3, discharge chamber 7 is opened in the side of discharge chamber 7 located at the top of striker plate 6, discharging opening 10.
As shown in accompanying drawing 3-4, disperse the shape in intermediate layer 11 from cylindric, upper end is fixed on striker plate 6, positioned at point
Dissipate between bucket 1 and dispersion wheel 3.Offer convection holes 12 on dispersion wheel 3 and dispersion intermediate layer 11, convection holes 12 be manhole or
Waist through hole, sets multiple, and in longitudinally, laterally equidistantly arrangement, dispersion intermediate layer 11 is with the convection holes 12 disperseed on wheel 3 in horizontal stroke
To in set location often go it is highly consistent, between mutually correspond to.
As shown in accompanying drawing 5-7, water chestnut is equipped with 3 inside and outside walls of dispersion wheel, the dispersion inside and outside wall of intermediate layer 11, the inwall of dispersion bucket 1
Shape burr, increases slurry with 3 inside and outside walls of dispersion wheel, the dispersion inside and outside wall of intermediate layer 11, the frictional force of the inwall of dispersion bucket 1 and shearing
Power.
Dynamic screen separators 14 are installed on the annular inner ring of striker plate 6, dynamic screen separators 14 are cylindrical,
Slurry after dispersion is screened, finely dispersed slurry passes through dynamic screen separators 14, into discharge chamber 7, from discharging
Mouthfuls 10 discharge, and are not uniformly dispersed, the slurry that particle diameter is larger returns to 3 regions of dispersion wheel and continues to participate in dispersion process.
Certainly, dispersion intermediate layer 11 can also be set to several piece arc plate or helical blade circumferentially;Convection holes 12 also may be used
To be set to other common shape through holes such as square opening, slotted eye or polygonal hole, while the size of convection holes 12, quantity and position
Putting can respectively carry out different settings according to the property of different slurries, slurry is reached preferable dispersion effect and higher point
Dissipate efficiency;Burr 13 on 3 inside and outside walls of dispersion wheel, the dispersion inside and outside wall of intermediate layer 11, the inwall of dispersion bucket 1, except rhombus burr, also
It can be annular knurl, car flower or other burrs, it is not limited to above example.
Need the slurry of decentralized processing to be sent into from charging aperture, through the stop of deflector, shunted since the charging aperture left and right sides,
By the material path in attachment, space, dispersion intermediate layer and the dispersion bucket between dispersion wheel and dispersion intermediate layer are sequentially entered
Between gap.Stirred by rotary dispersion, the slurry between dispersion wheel and dispersion intermediate layer is impinged upon in dispersion intermediate layer
On wall, part size is rebounded to the outer wall of dispersion wheel, and part size is divided by disperseing the shearing of convection holes on intermediate layer to enter
The gap between intermediate layer and dispersion bucket is dissipated, the slurry fractions between dispersion intermediate layer and dispersion bucket are impinged upon on dispersion bucket wall,
On part bounce-back to dispersion intermediate layer outer wall, dispersion wheel is entered again with dispersion intermediate layer by the convection holes disperseed in the middle of intermediate layer
Between, in dispersion wheel, impact several times, dispersion between dispersion intermediate layer and dispersion bucket.Under the mass action of dispersion wheel rotation,
Slurry is finally moved up to when at striker plate, and by the screening of dynamic screen separators, the slurry for meeting Particle size requirements passes through
Dynamic screen separators, enter back into discharge tank, are sent out from discharging opening.Slurry more than dynamic screen separators particle diameter is turned again to
In dispersion bucket, proceed dispersion, the particle size range of the slurry for obtaining is narrower, slurry stabilization, dispersion effect is more preferable.
Claims (9)
1. a kind of high speed dispersing device, including dispersion bucket (1), main shaft (2), dispersion wheel (3), deflector (4), attachment (5), gear
Flitch (6), discharge chamber (7), main shaft (2) lower end are installed with dispersion wheel (3), and main shaft (2) the upper end connection drives
Device, dispersion bucket (1) lower end offers charging aperture (8), and deflector (4) two ends are fixed by the attachment (5)
In the charging aperture (8) top, material path (9) is offered on the attachment (5), the striker plate (6) is located in annular
Dispersion wheel (3) top, striker plate (6) top is the discharge chamber (7), and the side of the discharge chamber (7) offers
Discharging opening (10), it is characterised in that:Also include dispersion intermediate layer (11), the dispersion intermediate layer (11) is positioned at the dispersion bucket
(1) between dispersion wheel (3), and its upper end and the striker plate (6) are fixed, in dispersion wheel (3) and the dispersion
Convection holes (12) are offered on interbed (8).
2. a kind of high speed dispersing device according to claim 1, it is characterised in that:The dispersion intermediate layer (11) is in cylinder
Shape.
3. a kind of high speed dispersing device according to claim 1, it is characterised in that:The dispersion intermediate layer (11) is several piece
Arc plate or helical blade are circumferentially set.
4. a kind of high speed dispersing device according to claim 1, it is characterised in that:Described dispersion wheel (3) inside and outside wall, described
Burr (13) is equipped with dispersion intermediate layer (11) inside and outside wall, the dispersion bucket (1) inwall.
5. a kind of high speed dispersing device according to claim 4, it is characterised in that:The burr (13) is rhombus burr,
Annular knurl or car are spent.
6. a kind of high speed dispersing device according to claim 1, it is characterised in that:The convection holes (12) are manhole
Or waist through hole.
7. a kind of high speed dispersing device according to claim 1, it is characterised in that:The convection holes (12) set multiple,
In longitudinally, laterally equidistantly arrangement.
8. a kind of high speed dispersing device according to claim 1, it is characterised in that:The dispersion intermediate layer (11) with it is described
Convection holes (12) in dispersion wheel (3) are often gone highly consistent on horizontally set position.
9. a kind of high speed dispersing device according to claim 1, it is characterised in that:Dynamic screen cloth point also including annular
From device (14), upper end is fixed on the annular inner ring of the striker plate (6), positioned at dispersion wheel (3) inner side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611143983.XA CN106693760A (en) | 2016-12-13 | 2016-12-13 | High speed dispersing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611143983.XA CN106693760A (en) | 2016-12-13 | 2016-12-13 | High speed dispersing device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106693760A true CN106693760A (en) | 2017-05-24 |
Family
ID=58935769
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611143983.XA Pending CN106693760A (en) | 2016-12-13 | 2016-12-13 | High speed dispersing device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106693760A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107159003A (en) * | 2017-07-03 | 2017-09-15 | 深圳市广源智能设备有限公司 | A kind of novel slurry Homogenization Treatments device |
CN107308849A (en) * | 2017-08-11 | 2017-11-03 | 上海弗鲁克科技发展有限公司 | Sub- high speed nano-fluid disperser |
CN109589835A (en) * | 2017-09-30 | 2019-04-09 | 深圳市比亚迪锂电池有限公司 | A kind of dispersion machine |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4792238A (en) * | 1984-09-11 | 1988-12-20 | Pola Kasei Kogyo Kabushiki Kaisha | Continuous dispersion apparatus having multi-step dispersion chambers |
CN202921206U (en) * | 2012-11-06 | 2013-05-08 | 深圳市尚水智能设备有限公司 | High-speed stirring device |
CN104096506A (en) * | 2014-07-09 | 2014-10-15 | 深圳市尚水智能设备有限公司 | Integrated slurry making device |
CN105148766A (en) * | 2015-09-09 | 2015-12-16 | 深圳市尚水智能设备有限公司 | High-speed dispersing device, high-speed dispersing equipment and high-speed dispersing method |
CN105268347A (en) * | 2014-05-26 | 2016-01-27 | 邓昌沪 | Dynamic friction disperser |
CN205019987U (en) * | 2015-09-09 | 2016-02-10 | 深圳市尚水智能设备有限公司 | High speed dispersion device and equipment |
CN105664765A (en) * | 2016-03-21 | 2016-06-15 | 江苏中兴派能电池有限公司 | Stirring device of high-speed dispersion equipment |
CN206372728U (en) * | 2016-12-13 | 2017-08-04 | 力信(江苏)能源科技有限责任公司 | A kind of high speed dispersing device |
-
2016
- 2016-12-13 CN CN201611143983.XA patent/CN106693760A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4792238A (en) * | 1984-09-11 | 1988-12-20 | Pola Kasei Kogyo Kabushiki Kaisha | Continuous dispersion apparatus having multi-step dispersion chambers |
CN202921206U (en) * | 2012-11-06 | 2013-05-08 | 深圳市尚水智能设备有限公司 | High-speed stirring device |
CN105268347A (en) * | 2014-05-26 | 2016-01-27 | 邓昌沪 | Dynamic friction disperser |
CN104096506A (en) * | 2014-07-09 | 2014-10-15 | 深圳市尚水智能设备有限公司 | Integrated slurry making device |
CN105148766A (en) * | 2015-09-09 | 2015-12-16 | 深圳市尚水智能设备有限公司 | High-speed dispersing device, high-speed dispersing equipment and high-speed dispersing method |
CN205019987U (en) * | 2015-09-09 | 2016-02-10 | 深圳市尚水智能设备有限公司 | High speed dispersion device and equipment |
CN105664765A (en) * | 2016-03-21 | 2016-06-15 | 江苏中兴派能电池有限公司 | Stirring device of high-speed dispersion equipment |
CN206372728U (en) * | 2016-12-13 | 2017-08-04 | 力信(江苏)能源科技有限责任公司 | A kind of high speed dispersing device |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107159003A (en) * | 2017-07-03 | 2017-09-15 | 深圳市广源智能设备有限公司 | A kind of novel slurry Homogenization Treatments device |
CN107308849A (en) * | 2017-08-11 | 2017-11-03 | 上海弗鲁克科技发展有限公司 | Sub- high speed nano-fluid disperser |
CN109589835A (en) * | 2017-09-30 | 2019-04-09 | 深圳市比亚迪锂电池有限公司 | A kind of dispersion machine |
CN109589835B (en) * | 2017-09-30 | 2021-10-22 | 深圳市比亚迪锂电池有限公司 | Dispersing machine |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109173778B (en) | High-efficient agitating unit | |
CN202778319U (en) | Single shaft coulter type mixing machine | |
CN207899359U (en) | A kind of blender for producing high light-fast Polypropylene | |
CN106693760A (en) | High speed dispersing device | |
CN205196958U (en) | Feed mixing device | |
CN105965711A (en) | Plastic particle mixing device | |
CN213253915U (en) | Powder animal remedy compounding device | |
CN206372728U (en) | A kind of high speed dispersing device | |
CN105771752A (en) | Hydraulic vertical fodder stirring machine | |
CN216224246U (en) | Improve full-automatic whole grain wet process mixing granulator of medicine security | |
CN105214551B (en) | The blender that may filter that | |
CN210617000U (en) | Raw material mixer of production plastic tubing | |
CN104647609A (en) | Continuous dry mortar mixing equipment | |
CN111152363B (en) | Compounding device for composite titanium dioxide produced from fly ash | |
CN204193836U (en) | A kind of modified form Pneumatic blender | |
CN208542070U (en) | A kind of uniformly lossless batch mixer | |
CN207446021U (en) | A kind of cone screw mixer | |
CN109621794A (en) | A kind of low-speed high-efficiency horizontal type trommel mixer | |
CN215353234U (en) | High-efficient emery wheel raw materials compounding equipment | |
CN212492717U (en) | Low-speed mixer | |
CN209612782U (en) | A kind of low-speed high-efficiency horizontal type trommel mixer | |
CN211677430U (en) | Cement manufacture compounding device | |
CN211803668U (en) | Sand mixing device for hardware production and casting machine | |
CN207359413U (en) | One kind drying mixer | |
CN204712277U (en) | A kind of continous way mixing apparatus of dry powder and mortar |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170524 |