CN106513116A - Intermittent media disperser - Google Patents
Intermittent media disperser Download PDFInfo
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- CN106513116A CN106513116A CN201610276307.3A CN201610276307A CN106513116A CN 106513116 A CN106513116 A CN 106513116A CN 201610276307 A CN201610276307 A CN 201610276307A CN 106513116 A CN106513116 A CN 106513116A
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- Prior art keywords
- plectane
- blade
- container
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/16—Mills in which a fixed container houses stirring means tumbling the charge
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/16—Mills in which a fixed container houses stirring means tumbling the charge
- B02C17/163—Stirring means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/18—Details
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Crushing And Grinding (AREA)
- Crushing And Pulverization Processes (AREA)
Abstract
The present invention provides a batch type media disperser. In the container, a plurality of circular plate blades are disposed close to each other so as to produce a pumping action which forms a disc-shaped flow upon rotation. With this pumping action, the flow of the treatment material is actively attracted to the container and actively discharged from the container. With this positive attraction and discharge action, the number of cycles of the processing material passing through the container can be increased.
Description
Technical field
The present invention relates to a kind of medium dispersion machine, the medium dispersion machine will be in the solids in the solid/liquid class process material used in chemistry, medical treatment, electronics, food, feedstuff and other various fields and disperse medium（Pearl）Stir and corpusculed together, and the solids is distributed in liquid.More particularly to a kind of batch (-type) medium dispersion machine, the batch (-type) medium dispersion machine receive disperse medium in container, and by the tank immersion in the process material in tank, make process material in container interior circulation to carry out wet type decentralized processing.
Background technology
So-called batch (-type) medium dispersion machine, is can intensively to carry out the device of decentralized processing using less disperse medium, it is known to the device for example shown in Japanese Unexamined Patent Publication Unexamined Patent 11-244679 publication.In the publication, following dispersal devices are recorded：The container for accommodating disperse medium is made and makes the container of upper opening by the dispersal device, and its bottom is made screen cloth.It is also known that there is the device that container is integrally formed into the cage body with screen cloth.In such container, if making the aperture area of screen cloth diminish, there are following situations：The circular flow for processing material tails off, and can also produce the problem of eyelet blocking.If making the aperture area of screen cloth become big, disperse medium is possible to flow out, and becomes to use the disperse medium of path.And, the abrasion of the screen cloth caused by disperse medium becomes many, the reason for becoming wear resistance and be deteriorated.
In batch (-type) medium dispersion machine, stir together with disperse medium in order to material will be processed, be generally provided with the stirring vane of needle-like in container.It is also known that there is following structures：Arrange feeding stirring vane to send into material is processed to container in tank or at the peristome of container.But, only rotated with stirring vane by making above-mentioned feeding, it is difficult to make to container the flow of the process material for flowing into become big.Therefore, in conventional batch (-type) medium dispersion machine, through container process material it is less through number of times, processing holdup time of the material in container is distributed with the trend for broadening.According to Lei Tinggeer（Rittinger）Rule understand, by ball mill（Medium dispersion machine）In the dispersion for carrying out, if processing, holdup time distribution of the material in ball mill is precipitous, the atomic particle size distribution obtained by dispersion becomes precipitous.But, as described above, in conventional batch (-type) dispersion machine, holdup time distribution broadens, so being difficult to obtain the particle that precipitous particle is distributed.
Further, as described above, in conventional batch (-type) medium dispersion machine, use from rotary shaft the situation of the stirring vane of the needle-like for diametrically extending more as the stirring vane being located in container.But, the shear rate at its blade end part of such needle-like blade is poorer than plectane blade, it is difficult to by particle efficiency corpusculed well.It is also known that there is following such batch (-type) medium dispersion machines：As the screen cloth of said vesse, the staybolt for extending downwards is set in the periphery of container, multiple flat boards, or coiled wire at spaced intervals are installed in stacking at spaced intervals on the staybolt, thus constitute screen cloth.But, in such a configuration, when screen cloth is cleaned, staybolt becomes barrier, and the precipitation for processing material occurs at staybolt part, and cleaning becomes difficult, produces problem on cleaning.
The content of the invention
The purpose of the present invention is, in batch (-type) medium dispersion machine, the flow of the process material flowed in container is made to become big flow, the batch (-type) medium dispersion machine receives disperse medium in container, and by the tank immersion in the treatment fluid of tank, make process material in tank and container interior circulation to carry out decentralized processing.Thus, there is provided a kind of batch (-type) medium dispersion machine, the batch (-type) medium dispersion machine can make the cycle-index of the process material in container interior circulation become many, make holdup time distribution become precipitous, precipitous so as to realize particle size distribution corpusculed.
Moreover, it is an object that a kind of cleaning in batch (-type) medium dispersion machine is easier to, is not easy to produce the above-mentioned batch (-type) medium dispersion machine of eyelet blocking.
According to the present invention，A kind of batch (-type) medium dispersion machine is provided，The batch (-type) medium dispersion machine makes to be accommodated with the tank immersion of disperse medium in the process material in tank，To carry out decentralized processing，It is characterized in that，Possesses container、Rotary shaft and multiple plectane blades，The container is provided with peristome、The screen cloth and base plate of tubular，The peristome is in upper opening，The screen cloth of the tubular is in the formed below for tubular of above-mentioned peristome，And there is the impenetrable opening of disperse medium，The bottom of above-mentioned screen cloth is covered by the base plate，And there is no opening，The rotary shaft extends into container through above-mentioned peristome，The plurality of plectane blade is attached in the rotary shaft in container，And there is through hole，Above-mentioned multiple plectane blades are close to and arrange，So that when rotary shaft rotates，Produce from the dish type pump action that brings of flowing and material will be processed and attracted into container，And，Processing material becomes spoke stream and discharges to the periphery of plectane blade.
Additionally, according to the present invention, there is provided above-mentioned batch (-type) medium dispersion machine, in above-mentioned dispersion machine, above-mentioned screen cloth is integratedly linked with base plate, and is provided with multiple axle stream stirring vanes in above-mentioned tank so that the process material in tank produces axle stream and flows in tank.
The present invention is constituted as described above, multiple plectane blades are close to and are arranged, to produce the pump action for forming dish type flowing in the container, if so the plectane blade rotation by rotary shaft, produce will process material from the peristome of container to container in the sucking action that energetically sucks.The material that processes for encountering the plectane blade of lower section through the through hole of the plectane blade of top becomes along the spoke stream of the plane of plectane blade and diametrically flows, and is discharged in from the screen cloth of surrounding to tank.During this period, process material and be stirred together with disperse medium, so being carried out by the corpusculed that dispersion brings.By above-mentioned pump action, the process material being discharged in tank is energetically sucked into container again, and by decentralized processing.So, process material energetically to be sucked into container by the pump action produced in container, and be discharged from the container, it is possible to making the flow for processing material for flowing into relative to container, flowing out become big flow.As a result, it is possible to make the cycle-index of the process material through container become many, holdup time distribution becomes precipitous such that it is able to obtain the precipitous micropartical of particle size distribution.
Further, if arranging the multiple axle stream stirring vanes for producing axle stream in above-mentioned tank, flowing of the process material in tank can be made to form sinking or form overall flow.By the axle stream, can make to be become big by the flow of the process material attracted in from the peristome of container to container, can further improve the effect above brought by big flow.Now, if making multiple axle stream stirring vanes be the paddle blade for producing laminar flow, and a side is become and draws dirty（Sinking）, the opposing party becomes and drawn stream（Upper up-flow）, then overall flow is formed in tank, the cycle-index through the process material of container becomes more, and holdup time distribution becomes precipitous, can shorten rate of dispersion, and can obtain precipitous particle size distribution.Additionally, by using plectane blade, the shear rate in blade end portion becomes more than 1.5 times of needle-like blade of speed such that it is able to improve dispersion effect.If above-mentioned screen cloth and base plate are integratedly linked, in cleaning, do not exist around container and produce barrier as precipitation in the flowing for processing material, it is possible to increase cleaning.
Description of the drawings
Fig. 1 represents one embodiment of the invention, is the side view for representing part section.
Fig. 2 is represented an embodiment of 3 plectane blade combinations, is the side view for representing part section.
Fig. 3 is represented an embodiment of 3 plectane blade combinations, is the top view for representing part section.
Fig. 4 is the top view for representing clearance part.
Fig. 5 represents an embodiment of the combination of plectane blade, Fig. 5 A are sectional views, Fig. 5 B are the top views of plectane blade in fig. 5 in top, and Fig. 5 C are top views in fig. 5 in middle plectane blade, and Fig. 5 D are the top views of the plectane blade being below in fig. 5.
Fig. 6 represents another embodiment of the combination of plectane blade, Fig. 6 A are sectional views, Fig. 6 B are the top views of plectane blade in fig. 6 in top, and Fig. 6 C are top views in fig. 6 in middle plectane blade, and Fig. 6 D are the top views of the plectane blade being below in fig. 6.
Fig. 7 represents the another embodiment of the combination of plectane blade, Fig. 7 A are sectional views, Fig. 7 B are the top views of plectane blade in fig. 7 in top, and Fig. 7 C are top views in fig. 7 in middle plectane blade, and Fig. 7 D are the top views of the plectane blade being below in fig. 7.
Specific embodiment
Fig. 1 represents an embodiment of batch (-type) medium dispersion machine of the invention, is provided with framework 4 in the top of main body 1 so as to is directed on guidance axis 3 by lifting shaft 2 and moves up and down.It is moved in the lower section of the framework 4 and is accommodated with the tank 5 for processing material, and the tank 5 is kept device 6 and is maintained at fixed position.Around the tank 5, the tank overcoat 7 for making the temperature control mediums such as cooling water circulate is provided with.
In above-mentioned tank 5, load container 8, the container 8 is accommodated with glass, zircon, zirconium oxide, steel, ceramics or other disperse medium（Pearl）, preferably high specific gravity disperse medium（Diagram is omited）.The container 8 has the top overcoat 9 of the temperature control mediums such as Cooling Water circulation on top, and is located at the lower section of said frame 4 by the water service pipe dual-purpose strut 10 as the stream for temperature control medium.On the top of the container 8, top overcoat 9 is provided through towards the inclined next door 11 of interior side of container, and is formed with the peristome 12 of heart opening wherein.
In the lower section of the top overcoat 9 of said vesse 8, can removably link the screen cloth 13 of tubular, the screen cloth 13 of the tubular has the openings such as the aperture of following such sizes, slit, mesh：The disperse medium being accommodated in the container cannot pass through and process material and can pass through.The bottom of the screen cloth 13 of tubular is covered with the not base plate 14 with opening.The base plate 14 and screen cloth 13 are by arranging the appropriate connecting portions such as flange（Diagram is omited）The fasteners such as blending bolt, rivet are affixed and integratedly link.Preferably, multiple screen clothes of opening of a size suitable can be prepared with changing, so that the screen cloth can the screen cloth of different sizes with opening be changed corresponding to disperse medium.In addition, on above-mentioned base plate, may be provided for picking and placeing the conveying end of disperse medium（Diagram is omited）.
In said vesse 8, the rotary shaft 15 extended in oriented container is inserted through peristome 12.The rotary shaft 15 is hung down from framework 4 downwards, and the drive motor 16 for being arranged at framework 4 drives, and is provided with multiple plectane blades 17 in lower end.In embodiment, combine 3 plectane blades 17, but it is also possible to combine the plectane blade of 2 or more than 4.By the plectane blade for being formed with appropriately sized through hole 18 in suitable position or not, the plectane blade with through hole is constituted above-mentioned multiple plectane blades.Multiple plectane blades 17 are close to and arrange so that produce the pump action brought by dish type flowing when rotated.The so-called pump action brought by dish type flowing, in embodiment, is following such effects：When plectane blade 17 rotates, material will be processed through peristome 12 and attracted into container, the process material being attracted in container will be flowed in the axial direction through through hole 18, be subsequently formed the spoke stream of the radial direction towards plectane blade（Stream）, and along plectane blade peripheral direction from plane to plectane blade discharge.By the pump action, the process material that have passed through the opening of above-mentioned screen cloth is back in above-mentioned tank.So, it is known as following well-known carousel-type pumps that the multiple plectane blades by close setting produce attraction, the pump action of discharge effect：Fluid, by fluid in the radially discharge of plectane blade, is attracted by the carousel-type pump frictional force and centrifugal action using the fluid contacted with the surface of plectane blade therewith.Thus, if the interval between plectane blade 17 is wide, pump action will not be produced, so multiple plectane blades 17 are by sandwich clearance part 19, being retained as the state being close to narrower interval.
Above-mentioned clearance part 19 as shown in Figure 3, Figure 4, is formed as section substantially rectangular shape, in the radially configuration of plectane blade 17.The inner face 20 of the center position towards plectane blade is formed as narrow by clearance part 19, it is in the two sides being connected with the two ends of the inner face 20, be formed as linear towards the side 21 of the side of the direction of rotation of plectane blade, the side 22 of side opposite to the direction of rotation is formed as into inclined plane.By the structure, when in Fig. 3, Fig. 4, plectane blade rotates counterclockwise, the discharge for processing material is promoted, and can increase output.One positioned at its corner portion of outer face 23 of the clearance part 19 of radial outside is formed as cambered surface, and another is formed as corner.In the planar portions of clearance part 19, as shown in Fig. 2 being provided with the convex portion 25 engaged with the recess 24 being located on plectane blade 17.Multiple plectane blades 17 are overlapped in the way of clipping the clearance part 19, and are bolted 26 fixations.
If the shear rate between the blade end of above-mentioned plectane blade 17 and conventional needle-like blade is compared, then the shear rate between the blade end of plectane blade than needle-like blade blade end between shear rate become about 1.5 times, as a result, it is possible to accelerate decentralized processing.The surface of the planar portions of above-mentioned plectane blade 17 can also be to maintain plane, but it is also possible to consider to process the particle footpath of material and hardness and arrange pin 27.It is further preferred that above-mentioned pin 27 is provided projectingly on the peripheral part of plectane blade 17, so as to impulsive force is applied to the disperse medium of the peripheral part for easily concentrating on plectane blade 17 and spreads which.In addition, the pin is erect on the upper surface or lower surface of plectane blade in the embodiment shown in Figure 2 in vertical direction, but it is also possible on the periphery of plectane blade 17 pin is projected in the horizontal direction（Diagram is omited）.Pin can also be replaced and convex portion or recess is formed in the plane of plectane blade, to apply to impact to disperse medium（Diagram is omited）.
As described above, multiple plectane blades 17 are rotated in container 8, thus, it is possible to be attracted to material is processed in container 8 by pump action, but are additionally provided with feeding in embodiment（Suction）Mechanism, sends in container will energetically to process material.In FIG, as feeding mechanism, helical member 28 is provided with around the rotary shaft 15 positioned at the peristome 12 of container 8.If rotary shaft 15 rotates, process material and guided and be admitted to by the helical member 28（Suction）In container 8.Alternatively, it is also possible to replace helical member and using axial flow turbine blade, paddle blade or other send into blades as feeding mechanism（Diagram is omited）.
As described above, on plectane blade 17, through hole 18 can be set in position.In Fig. 5 Fig. 7, show the plectane blade with various through holes and there is no one of the combination of the plectane blade of through hole.Embodiment shown in Fig. 5 A to Fig. 5 D has 3 plectane blades.On top plectane blade 29, as shown in Figure 5 B, 4 through holes 31 are formed with around the installation portion 30 for linking with rotary shaft 15.On middle circle plate leaf piece 32, also 4 through holes 33 are provided likewise with top plectane blade 29.Through hole is not provided with bottom plectane blade 34.In the case of such a construction, the material that processes for passing through peristome 12 and being attracted in the axial direction by the pump action brought by plectane blade 29,32,34 passes through top plectane blade, the through hole of middle circle plate leaf piece, and in the radially flowing of each plectane blade, the material that processes for encountering bottom plectane blade diametrically flows along the plane of bottom plectane blade.
In the case of the embodiment shown in Fig. 6 A, on top plectane blade 35 and middle circle plate leaf piece 36, big through hole 37,38 concentric with plectane blade is formed with the way of surrounding rotary shaft 15.The installation portion 30 of rotary shaft is provided with bottom plectane blade 39, but does not form through hole.In the case, also will process material attraction, discharge by pump action substantially samely with the embodiment shown in above-mentioned Fig. 5 A and make which flow.
In the case of the embodiment shown in Fig. 7 A, on top plectane blade 40, the installation portion 30 and 4 through holes 41 of rotary shaft is provided with as shown in Figure 7 B.On middle circle plate leaf piece 42 and bottom plectane blade 43, big through hole 44,45 concentric with plectane blade is provided with.In the case of the embodiment, if plectane blade 40,42,43 rotates, the process material then sent into from peristome 12 flows in the axial direction, and encounter the material that processes of the base plate 14 of container to be attracted by the through hole 45 from bottom plectane blade 43, and into the space between middle circle plate leaf piece 42 and bottom plectane blade 43, the plane along each plectane blade diametrically flows.
With reference to Fig. 1, between container 8 and tank 5, multiple paddle type stirring vane isometry stream stirring vanes 46 are provided with, so that the process material in tank forms axle stream and flows in the vertical direction.Rotate the axle stream stirring vane 46 by the rotary shaft 47 and drive motor 48 hung down from said frame 4.Figure 1 illustrates 2 paddle type stirring vanes, but it is also possible to be equally spaced the paddle type stirring vane of more than 3 in the way of said vesse to be surrounded.Axle stream stirring vane 46 can produce upper up-flow in tank or produce sinking, it is possible to suitably driving corresponding to the flow behavior for processing material according to shape and the direction of rotation of oar.For example, if whole axle stream stirring vanes 46 are made for drawing lower paddle type blade, produce laminar flow directed downwardly in tank, become much larger can the flow of the process material flowed in through peristome 12 to container.If additionally, making an axle stream stirring vane for drawing lower paddle blade, and making another for having drawn paddle blade, then the flowing in tank becomes relative and circulates, and can obtain not producing the overall flow of precipitation in material is processed.
Then, load disperse medium to said vesse 8, be preferably encased high specific gravity disperse medium, and the container is sunk in tank so that under the liquid level of tank 5 of the container in process material is accommodated with.If also, rotate drive motor 16,48, via the rotary transfer machine for eliminating diagram, above-mentioned rotary shaft 15,47 rotates.By the rotation, the material that processes in tank flows towards the peristome of container, and the helical member 28 being arranged in rotary shaft 15 is sent in container.Further, the plectane blade 17 in container plays pump action by rotation, so the peristome 12 for processing material through container 8 is by the energetically attraction into container.The process material entered in container is stirred together with disperse medium and is disperseed.Material is processed by the discharge effect brought by the pump action of plectane blade 17 after dispersion, discharged in from container 8 to tank 5 through screen cloth 13.What is be discharged from the container processes material by the pump action brought by above-mentioned helical member 28 and plectane blade 17, through above-mentioned peristome 12, is attracted in container 8 again, reaches desired degree so as to be dispersed to.Now, the cooling water cooling of top overcoat 9 that the heating in container 8 and in tank 5 is through tank overcoat 7 and is located on said vesse 8.According to process material, it is also possible to using warm water as temperature control medium.
As described above, the batch (-type) medium dispersion machine of the present invention makes to be close to multiple plectane blade rotations of setting, thus make to produce the pump action for forming dish type flowing in container, material will be processed effectively and with big flow suction container, the cycle-index of process material is made to become many, holdup time distribution is made to become precipitous such that it is able to carry out the precipitous decentralized processing of particle size distribution.
Claims (7)
1. a kind of batch (-type) medium dispersion machine, the batch (-type) medium dispersion machine make to be accommodated with the tank immersion of disperse medium in the process material in tank, carry out decentralized processing, it is characterised in that
Possess container, rotary shaft and multiple plectane blades,
The container is provided with peristome, the screen cloth of tubular and base plate, and, in upper opening, the screen cloth of the tubular is in the formed below for tubular of above-mentioned peristome for the peristome, and there is the impenetrable opening of disperse medium, the bottom of above-mentioned screen cloth is covered by the base plate, and does not have opening
The rotary shaft extends into container through above-mentioned peristome,
The plurality of plectane blade is attached in the rotary shaft in container, and has through hole,
Above-mentioned multiple plectane blades are close to and arrange, so that when rotary shaft rotate, produce from dish type flowing the pump action that brings and will process material and attract into container, also, process material becomes spoke stream and the periphery discharge to plectane blade.
2. batch (-type) medium dispersion machine as claimed in claim 1, it is characterised in that
Above-mentioned multiple plectane vanes are concatenated by the clearance part for diametrically configuring, and the side of the direction of rotation towards plectane blade in the side of the clearance part is formed as linear, and the side of side opposite to the direction of rotation is formed as inclined plane.
3. batch (-type) medium dispersion machine as claimed in claim 1, it is characterised in that
Pin is provided with the planar portions of above-mentioned plectane blade.
4. batch (-type) medium dispersion machine as claimed in claim 1, it is characterised in that
In said vesse, the screen cloth of above-mentioned tubular and above-mentioned base plate integratedly link.
5. batch (-type) medium dispersion machine as claimed in claim 1, it is characterised in that
Axle stream stirring vane is provided with above-mentioned tank, to produce axle stream in tank, process material is flowed up in upper and lower in tank.
6. batch (-type) medium dispersion machine as claimed in claim 5, it is characterised in that
Above-mentioned axle stream stirring vane is paddle type blade, is provided with multiple so that is produced the sinking processed under material is drawn in tank with stirring vane by least one axle stream, is produced with stirring vane by least other axle streams and will process the upper up-flow that material has been drawn.
7. batch (-type) medium dispersion machine as claimed in claim 5, it is characterised in that
Above-mentioned axle stream stirring vane is to produce the paddle type blade for processing the sinking under material is drawn by tank.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2015179627A JP6326020B2 (en) | 2015-09-11 | 2015-09-11 | Batch media disperser |
| JP2015-179627 | 2015-09-11 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106513116A true CN106513116A (en) | 2017-03-22 |
| CN106513116B CN106513116B (en) | 2018-11-20 |
Family
ID=58316502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610276307.3A Active CN106513116B (en) | 2015-09-11 | 2016-04-29 | Intermittent medium dispersion machine |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JP6326020B2 (en) |
| CN (1) | CN106513116B (en) |
| MY (1) | MY188495A (en) |
| SG (1) | SG10201602814UA (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107824077A (en) * | 2017-11-28 | 2018-03-23 | 上海德耐泵业有限公司 | Dispersion impeller component, super effect are stirred dispersion machine and continuous reaction system |
| KR102092386B1 (en) * | 2018-03-29 | 2020-04-23 | 블레쏘 주식회사 | Apparatus for stiring with top and bottom double vortex |
| KR102092385B1 (en) * | 2018-03-29 | 2020-03-23 | 블레쏘 주식회사 | Homo-mixer apparatus and method for stirring by double vortex |
| DE102018007103A1 (en) * | 2018-09-07 | 2020-03-12 | Hosokawa Alpine Aktiengesellschaft | Device and method for changing bulk material properties |
| CN112588376B (en) * | 2019-07-11 | 2022-04-22 | 浙江常山虎跃水泥有限责任公司 | Cement processing equipment |
| CN113828394B (en) * | 2021-09-03 | 2023-01-31 | 南京利卡维智能科技有限公司 | High-speed circulating feeding system of multi-shaft grinding machine |
| KR102423099B1 (en) * | 2021-12-17 | 2022-07-20 | 주식회사 가람플랜텍 | Detachable stirred tank device |
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| JP2002154923A (en) * | 2000-11-16 | 2002-05-28 | Shiseido Co Ltd | Method for producing emulsified cosmetic containing hydrophobized powder |
| CN201399361Y (en) * | 2009-03-25 | 2010-02-10 | 蔡澳明 | Basket type sand grinding machine |
| CN104383989A (en) * | 2014-10-31 | 2015-03-04 | 罗斯（无锡）设备有限公司 | Grinding miller structure |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2017051929A (en) | 2017-03-16 |
| CN106513116B (en) | 2018-11-20 |
| JP6326020B2 (en) | 2018-05-16 |
| SG10201602814UA (en) | 2017-04-27 |
| MY188495A (en) | 2021-12-15 |
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