CN106513116B - Intermittent medium dispersion machine - Google Patents
Intermittent medium dispersion machine Download PDFInfo
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- CN106513116B CN106513116B CN201610276307.3A CN201610276307A CN106513116B CN 106513116 B CN106513116 B CN 106513116B CN 201610276307 A CN201610276307 A CN 201610276307A CN 106513116 B CN106513116 B CN 106513116B
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- blade
- plectane
- 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
-
- 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 kind of intermittent medium dispersion machine.In container, by multiple plectane blades close to setting, so that generating the pump action for forming dish type flowing when rotated.By the pump action, material energetically attraction and flowing being energetically discharged from container into container will be handled by generating.It is acted on by the positive attraction, discharge, the cycle-index of the processing material across container can be made to increase.
Description
Technical field
The present invention relates to a kind of medium dispersion machine, the medium dispersion machine will chemistry, medical treatment, electronics, food, feed and its
Solid/liquid class used in his various fields handles the solids and decentralized medium in material（Pearl）It stirs and particle together
Sonization, and it is distributed to the solids in liquid.In particular to a kind of intermittent medium dispersion machine, the intermittent medium dispersion
Machine stores decentralized medium in container, and by the tank immersion in the processing material in tank, follows processing material in container
Ring carries out wet type decentralized processing.
Background technique
So-called intermittent medium dispersion machine, is to be able to use less decentralized medium and intensively carry out decentralized processing
Device, it is known to such as device shown in Japanese Unexamined Patent Publication Japanese Laid-Open Patent Publication 11-244679 bulletin.In the bulletin, note
It is loaded with following dispersal devices：The container for accommodating decentralized medium is made into the container for making upper opening by the dispersal device, and by its bottom
Portion is made into sieve.It is also known that there is the device that container is integrally formed into the cage body with sieve.In such container,
If the opening area of sieve is made to become smaller, there are following situations：The circular flow of processing material tails off, and can also generate eyelet blocking
Problem.If the opening area of sieve is made to become larger, decentralized medium is possible to flow out, and becomes the decentralized medium for not being available path.
Moreover, the abrasion of the sieve as caused by decentralized medium becomes more, become the reason of wear resistance is deteriorated.
In intermittent medium dispersion machine, stirs together with decentralized medium in order to which material will be handled, usually set in container
There is the stirring blade of needle-like.It is also known that there is following structures：Feeding paddle is set in tank or at the opening portion of container
Piece will handle material and be sent into container.But only by rotating above-mentioned feeding with stirring blade, it is difficult to make to flow into container
The flow of processing material become larger.Therefore, in previous intermittent medium dispersion machine, the processing material across container is passed through
Number is less, and handle residence time of the material in container is distributed with the trend to broaden.According to Lei Tinggeer
（Rittinger）Rule it is found that by ball mill（Medium dispersion machine）In the dispersion of progress, if processing material is in ball mill
Interior residence time distribution is precipitous, then the size distribution steepening of the particulate obtained by dispersion is high and steep.But as it is above-mentioned that
Sample, in previous intermittent dispersion machine, residence time distribution broadens, so being difficult to obtain the particle of precipitous particle distribution.
In turn, as described above, in previous intermittent medium dispersion machine, as the stirring blade being located in container
Using the needle-like extended radially from rotary shaft stirring blade the case where it is more.But such its blade of needle-like blade
Shear velocity at end section is poorer than plectane blade, it is difficult to by particle efficiency corpusculed well.It is also known that under having
State such intermittent medium dispersion machine：As the sieve of said vesse, the support spiral shell extended downward is set on the periphery of container
Bolt, multiple plates, or coiled wire at spaced intervals are installed in stacking at spaced intervals on the staybolt, thus constitute sieve
Net.But in such a configuration, when cleaning sieve, staybolt becomes barrier, and processing material occurs at staybolt part
The precipitating of material, cleaning become difficult, and lead to the problem of on cleaning.
Summary of the invention
The object of the present invention is in intermittent medium dispersion machine, make the flow of the processing material flowed in container at
For big flow, the intermittent medium dispersion machine stores decentralized medium in container, and by the tank immersion in the treatment fluid of tank
In, recycle processing material to carry out decentralized processing in tank and container.A kind of intermittent medium dispersion machine is provided as a result, it should
Intermittent medium dispersion machine can make the cycle-index of the processing material recycled in container become more, and the residence time is made to be distributed steepening
It is high and steep, to realize the precipitous corpusculed of size distribution.
Moreover, it is an object that one kind cleaning in intermittent medium dispersion machine is easier to, is not easy to produce
The above-mentioned intermittent medium dispersion machine of eyelet blocking.
According to the present invention, a kind of intermittent medium dispersion machine is provided, the intermittent medium dispersion machine makes to be accommodated with dispersion
The tank immersion of medium is in the processing material in tank, to carry out decentralized processing, which is characterized in that have container, rotary shaft and
Multiple plectane blades, the container are provided with the sieve and bottom plate of opening portion, tubular, and the opening portion is described in upper opening
The sieve of tubular is formed as tubular below above-mentioned opening portion, and has the impenetrable recirculation hole of decentralized medium, the bottom
Plate covers the bottom of above-mentioned sieve, and does not have recirculation hole, and the rotary shaft passes through above-mentioned opening portion and extends into container, institute
It states in the rotary shaft that multiple plectane blades are attached in container, and there is through hole, the close setting of above-mentioned multiple plectane blades,
So that generate from dish type in rotary shaft rotation and flow bring pump action and attract processing material into container, and
And processing material becomes spoke stream and is discharged to the periphery of plectane blade.
In addition, according to the present invention, providing above-mentioned intermittent medium dispersion machine, in above-mentioned dispersion machine, above-mentioned sieve and bottom
Plate integrally links, and multiple axis stream stirring blades are equipped in above-mentioned tank, so that the processing material in tank generates axis stream
And it is flowed in tank.
The present invention is constituted as described above, by multiple plectane blades close to setting, forms dish type stream to generate in container
Dynamic pump action, so if by rotary shaft plectane blade rotate, generate will processing material from the opening portion of container to
The sucking action energetically sucked in container.Across the plectane blade of top through hole and encounter lower section plectane blade place
Reason material becomes the spoke stream along the plane of plectane blade and flows radially, is discharged from the sieve of surrounding into tank.?
During this, processing material is stirred together with decentralized medium, so being carried out by dispersion bring corpusculed.By said pump
Effect is sent, the processing material being discharged in tank is energetically sucked into container again, and by decentralized processing.In this way, processing
Material is energetically sucked by the pump action generated in container into container, and is discharged from the container, so can
The flow for handling material for flowing into, flowing out relative to container is set to become big flow.As a result, it is possible to make the processing material across container
Cycle-index become it is more, residence time distribution becomes precipitous, so as to obtain the precipitous particulate of size distribution.
In turn, if setting generates multiple axis stream stirring blades of axis stream in above-mentioned tank, processing material can be made to exist
Flowing in tank forms sinking or forms overall flow.By the axis stream, can make by from the opening portion of container to container
The flow of the processing material of interior attraction becomes larger, and can further increase by big flow bring said effect.At this point, if making multiple
Axis stream is the paddle blade for generating laminar flow with stirring blade, and makes a side dirty as drawing（Sinking）, another party become draw
Stream（Upper up-flow）, then overall flow is formed in tank, the cycle-index across the processing material of container becomes more, the residence time
It is high and steep to be distributed steepening, rate of dispersion can be shortened, and precipitous size distribution can be obtained.In addition, by using plectane blade,
The shear velocity in blade end portion becomes 1.5 times or more of speed of needle-like blade, so as to improve dispersion effect.If by upper
It states sieve and integrally links with bottom plate, then it is heavy there is no being generated in the flowing of processing material around container in cleaning
Form sediment such barrier, can be improved cleaning.
Detailed description of the invention
It is the side view for indicating a part with section Fig. 1 shows one embodiment of the invention.
Fig. 2 indicates the embodiment for combining 3 plectane blades, is the side view for indicating a part with section.
Fig. 3 indicates the embodiment for combining 3 plectane blades, is the top view for indicating a part with section.
Fig. 4 is the top view for indicating clearance part.
Fig. 5 indicates an embodiment of the combination of plectane blade, and Fig. 5 A is cross-sectional view, and Fig. 5 B is in fig. 5 in top
The top view of plectane blade, Fig. 5 C are the top views in fig. 5 in intermediate plectane blade, and Fig. 5 D is to be in fig. 5
The top view of the plectane blade of lower section.
Fig. 6 indicates another embodiment of the combination of plectane blade, and Fig. 6 A is cross-sectional view, and Fig. 6 B is in fig. 6 in top
Plectane blade top view, Fig. 6 C is the top view in fig. 6 in intermediate plectane blade, and Fig. 6 D is to locate in fig. 6
In the top view of the plectane blade of lower section.
Fig. 7 indicates the another embodiment of the combination of plectane blade, and Fig. 7 A is cross-sectional view, and Fig. 7 B is in fig. 7 in top
Plectane blade top view, Fig. 7 C is the top view in fig. 7 in intermediate plectane blade, and Fig. 7 D is to locate in fig. 7
In the top view of the plectane blade of lower section.
Specific embodiment
Fig. 1 shows an embodiments of intermittent medium dispersion machine according to the present invention, are equipped with frame 4 in the top of main body 1,
It is set to be guided and move up and down on guidance axis 3 by lifting shaft 2.It is moved in the lower section of the frame 4 and is accommodated with processing material
The tank 5 of material, and the tank 5 is kept device 6 and is maintained at fixed position.Around the tank 5, equipped with making the temperature control mediums stream such as cooling water
Logical tank housing 7.
In above-mentioned tank 5, it is packed into container 8, the container 8 is accommodated with glass, zircon, zirconium oxide, steel, ceramics or other points
Dispersion media（Pearl）, preferably high specific gravity decentralized medium（Diagram is omited）.The container 8 has the temperature control mediums streams such as Cooling Water on top
Logical top housing 9, and be located under said frame 4 by the water service pipe dual-purpose strut 10 as the flow path for temperature control medium
Side.On the top of the container 8, equipped with the inclined next door 11 of interior side across top housing 9 towards container, and it is formed in its center
The opening portion 12 of opening.
In the lower section of the top housing 9 of said vesse 8, it can removably link the sieve 13 of tubular, the tubular
Sieve 13 has the recirculation holes such as aperture, slit, the mesh of following such sizes：The decentralized medium being accommodated in the container can not
It passes through and handling material can pass through.The bottom of the sieve 13 of tubular is covered with the bottom plate 14 without recirculation hole.The bottom plate
14 and sieve 13 pass through setting flange etc. interconnecting piece appropriate（Diagram is omited）The fasteners such as blending bolt, rivet it is affixed and integrally
Connection.Preferably, multiple sieves of recirculation hole of a size suitable can be prepared with replacing, so that the sieve can correspond to
In decentralized medium, the sieve of different sizes with recirculation hole is replaced.In addition, may be provided on above-mentioned bottom plate
Pick and place the outlet of decentralized medium（Diagram is omited）.
In said vesse 8, the rotary shaft 15 extended in oriented container is inserted into across opening portion 12.The rotary shaft 15 is from frame
Frame 4 is hung down, and the drive motor 16 for being arranged at frame 4 drives, and is equipped with multiple plectane blades 17 in lower end.In embodiment
In, combine 3 plectane blades 17, but 2 or 4 or more plectane blades can also be made to combine.Above-mentioned multiple plectane blades
By being formed with the plectane blade of appropriately sized through hole 18 in suitable position or the plectane blade without through hole is constituted.It is more
A plectane blade 17 flows bring pump action by dish type close to setting, so that generating when rotated.It is so-called by dish type
Bring pump action is flowed, is following such effects in embodiment：When plectane blade 17 rotates, opening portion is passed through
12 attract processing material into container, and the processing material being attracted in container passes through through hole 18 and flows in the axial direction, connect
Form radial spoke stream towards plectane blade（Radiation stream）, and along the plane of plectane blade to the peripheral direction of plectane blade
Discharge.By the pump action, the processing material for having passed through the recirculation hole of above-mentioned sieve is back in above-mentioned tank.In this way, by
The pump action acted on close to multiple plectane blades generation attraction, the discharge of setting is pumped as following well-known carousel-types
It is known：Carousel-type pump is acted on using the frictional force and centrifugal force of the fluid contacted with the surface of plectane blade, by fluid
In the radially discharge of plectane blade, fluid is attracted therewith.Thus, it, will not if the interval between plectane blade 17 is wide
Pump action is generated, so multiple plectane blades 17 are by being maintained as with relatively narrow interval in sandwich clearance part 19
Close state.
Above-mentioned clearance part 19 as shown in Figure 3, Figure 4, is formed as section substantially rectangular shape, plectane blade 17 radially
Configuration.The inner face 20 of center position towards plectane blade is formed as narrow by clearance part 19, by with the inner face 20
The side 21 of the side of direction of rotation in the connected two sides in both ends, towards plectane blade is formed as linearly, will be with rotation
The side 22 for turning contrary side is formed as inclined surface.By the structure, when in Fig. 3, Fig. 4 plectane blade to counterclockwise
When direction rotates, the discharge for handling material is promoted, and is capable of increasing discharge rate.Positioned at the outer end of the clearance part 19 of radial outside
One of 23 its corner of face is formed as cambered surface, another is formed as corner.In the planar portions of clearance part 19, such as Fig. 2 institute
Show, equipped with the protrusion 25 engaged with the recess portion 24 being located on plectane blade 17.Multiple plectane blades 17 are to clip the clearance part
19 mode is overlapped, and is fixed by bolt 26.
If the shear velocity between above-mentioned plectane blade 17 and the blade end of previous needle-like blade is compared, justify
Shear velocity between the blade end of plate leaf piece becomes larger about 1.5 times than the shear velocity between the blade end of needle-like blade, as a result,
It can accelerate decentralized processing.The surface of the planar portions of above-mentioned plectane blade 17 is also possible to keep plane, but it is also contemplated that place
Manage material particle diameter and hardness and pin 27 is set.It is further preferred that above-mentioned pin 27 is provided projectingly on the periphery of plectane blade 17
Portion, so as to apply impact force to the decentralized medium for the peripheral part for being easy to concentrate on plectane blade 17 and make its diffusion.In addition,
The pin is erect on the upper surface or lower surface of plectane blade in vertical direction in the embodiment shown in Figure 2, but can also be with
Protrude pin in the horizontal direction（Diagram is omited）.It can also be instead of pin and in the flat of plectane blade
Protrusion or recess portion are formed on face, are impacted with applying to decentralized medium（Diagram is omited）.
As described above, multiple plectane blades 17 rotate in container 8, and thus, it is possible to will handle material by pump action
It is attracted in container 8, but is additionally provided with feeding in embodiment（Sucking）Mechanism, so that processing material is energetically sent into container
It is interior.In Fig. 1, as feeding mechanism, helical member 28 is equipped with around the rotary shaft 15 of opening portion 12 for being located at container 8.If
Rotary shaft 15 rotates, then handles material and guided and be admitted to by the helical member 28（Sucking）In container 8.Alternatively, it is also possible to replace
Helical member and using axial flow turbine blade, paddle blade or other be sent into blades as feeding mechanism（Diagram is omited）.
It as described above, can setting through hole 18 in place on plectane blade 17.In Fig. 5 Fig. 7, show
Combined an example of the plectane blade with various through holes and the plectane blade without through hole is gone out.Fig. 5 A to Fig. 5 D institute
The embodiment shown has 3 plectane blades.On top plectane blade 29, as shown in Figure 5 B, for linking with rotary shaft 15
Mounting portion 30 around be formed with 4 through holes 31.On middle circle plate leaf piece 32, also in the same manner as top plectane blade 29
Equipped with 4 through holes 33.Through hole is not provided on lower part plectane blade 34.In the case of such a construction, by by plectane
29,32,34 bring pump action of blade and pass through opening portion 12 and the processing material that is attracted in the axial direction is justified across top
The through hole of plate leaf piece, middle circle plate leaf piece, and in the radially flowing of each plectane blade, encounter the place of lower part plectane blade
Reason material flows radially along the plane of lower part plectane blade.
In the case where the embodiment shown in Fig. 6 A, on top plectane blade 35 and middle circle plate leaf piece 36, to surround
The mode of rotary shaft 15 is formed with the big through hole 37,38 with plectane blade same heart shaped.It is equipped on lower part plectane blade 39
The mounting portion 30 of rotary shaft, but do not form through hole.In the case, also substantially same with embodiment shown in above-mentioned Fig. 5 A
Ground will handle material attraction, be discharged and make its flowing by pump action.
In the case where the embodiment shown in Fig. 7 A, on top plectane blade 40, it is equipped with rotation like that as shown in Figure 7 B
Mounting portion 30 and 4 through hole 41 of axis.On middle circle plate leaf piece 42 and lower part plectane blade 43, it is equipped with same with plectane blade
The big through hole 44,45 of heart shaped.In the case of the embodiment, if plectane blade 40,42,43 rotates, from opening portion 12
The processing material of feeding flows in the axial direction, and encounter container bottom plate 14 processing material by from lower part plectane blade 43
Through hole 45 attracts, and enters the space between middle circle plate leaf piece 42 and lower part plectane blade 43, along each plectane blade
Plane flows radially.
Referring to Fig.1, between container 8 and tank 5, it is equipped with the isometric stream stirring blade 46 of multiple paddle type stirring blades, so that
Processing material in tank forms axis stream and flows in the up-down direction.By the rotary shaft 47 and driving to hang down from said frame 4
Motor 48 rotates the axis stream stirring blade 46.It is shown in FIG. 12 paddle type stirring blades, but can also be with will be above-mentioned
The mode that container surrounds is equally spaced 3 or more paddle type stirring blades.The axis stream is with stirring blade 46 according to the shape of paddle
Shape and direction of rotation can generate upper up-flow in tank or generate sinking, so the flowing that can correspond to processing material is special
Property and suitably drive.For example, being generated downward in tank if whole axis stream stirring blades 46 is made to draw lower paddle type blade
Laminar flow, the flow of the processing material flowed into across opening portion 12 into container can be made to become much larger.In addition, if making an axis
Stream stirring blade is to draw lower paddle blade, and another is made to have drawn paddle blade, then the flowing in tank becomes opposite recycle stream
It is dynamic, the overall flow for not generating precipitating in processing material can be obtained.
Then, it is packed into decentralized medium to said vesse 8, is preferably encased high specific gravity decentralized medium, and the container is sunk to
Into tank, so that the container is under the liquid level for being accommodated with the tank 5 of processing material.If also, drive motor 16,48 is rotated,
Then via the rotary transfer machine that the illustration is omitted, above-mentioned rotary shaft 15,47 rotates.Processing material by the rotation, in tank
The helical member 28 for flowing, and being arranged in rotary shaft 15 towards the opening portion of container is sent into container.In turn, the plectane in container
Blade 17 plays pump action by rotation, so processing material passes through the opening portion 12 of container 8 by energetically into container
Attract.The processing material entered in container is stirred together with decentralized medium and is dispersed.Processing material after dispersion by by
The pump action bring discharge of plectane blade 17 acts on, and is discharged from container 8 into tank 5 across sieve 13.It is discharged from the container
Processing material by by 17 bring pump action of above-mentioned helical member 28 and plectane blade, pass through above-mentioned opening portion 12, again
It is attracted in container 8, reaches desired degree to be dispersed to.At this point, the fever in container 8 and in tank 5 is through tank
The cooling water of housing 7 and the top housing 9 being located on said vesse 8 is cooling.According to processing material, warm water conduct also can be used
Temperature control medium.
As described above, intermittent medium dispersion machine of the invention rotates multiple plectane blades close to setting, thus
Make to generate the pump action for forming dish type flowing in container, by processing material effectively and to make to locate in big flow sucking container
The cycle-index for managing material becomes more, keeps residence time distribution steepening high and steep, thus allows for the precipitous decentralized processing of size distribution.
Claims (4)
1. a kind of intermittent medium dispersion machine, the intermittent medium dispersion machine makes the tank immersion for being accommodated with decentralized medium in tank
In interior processing material, to carry out decentralized processing, which is characterized in that
Have container, rotary shaft and multiple plectane blades,
The container is provided with the sieve and bottom plate of opening portion, tubular, and the opening portion is in upper opening, the sieve of the tubular
Be formed as tubular below above-mentioned opening portion, and there is the impenetrable recirculation hole of decentralized medium, the bottom plate is by above-mentioned sieve
The bottom of net covers, and does not have recirculation hole,
The rotary shaft passes through above-mentioned opening portion and extends into container,
The multiple plectane blade is attached in the rotary shaft in container, and has through hole,
Above-mentioned multiple plectane blades are close to setting, so that generating and being made by dish type flowing bring pumping in rotary shaft rotation
Attract with and by processing material into container, also, handle material to become spoke stream and be discharged to the periphery of plectane blade,
It is equipped with multiple axis stream stirring blades in above-mentioned tank, is flowed in tank to make the processing material in tank generate axis stream
It is dynamic,
Above-mentioned axis stream is following such paddle type blade with stirring blade：At least one axis stream is generated with stirring blade will be in tank
The sinking under material is drawn is handled, other axis streams generate the upper up-flow drawn with stirring blade.
2. intermittent medium dispersion machine as described in claim 1, which is characterized in that
Above-mentioned multiple plectane vanes are concatenated by the clearance part configured radially, in the side of the clearance part towards
The side of the direction of rotation of plectane blade is formed as linearly, and the side of side opposite to the direction of rotation is formed as inclined surface.
3. intermittent medium dispersion machine as described in claim 1, which is characterized in that
Pin is equipped in the planar portions of above-mentioned plectane blade.
4. intermittent medium dispersion machine as described in claim 1, which is characterized in that
In said vesse, the sieve of above-mentioned tubular and above-mentioned bottom plate integrally link.
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 CN106513116A (en) | 2017-03-22 |
| CN106513116B true 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 (8)
| 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 |
| CN113797803A (en) * | 2021-09-23 | 2021-12-17 | 深圳宝峰印刷有限公司 | Environment-friendly printing ink not prone to oxidative discoloration, and preparation method and device thereof |
| KR102423099B1 (en) * | 2021-12-17 | 2022-07-20 | 주식회사 가람플랜텍 | Detachable stirred tank device |
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| US4451155A (en) * | 1983-01-20 | 1984-05-29 | A. R. Wilfley And Sons, Inc. | Mixing device |
| JPH01179730U (en) * | 1988-06-07 | 1989-12-25 | ||
| JPH0817930B2 (en) * | 1989-05-16 | 1996-02-28 | 株式会社荒木鉄工 | Disperser |
| JPH0699048A (en) * | 1992-09-24 | 1994-04-12 | Canon Inc | Wet dispersing device |
| JP4141054B2 (en) * | 1999-06-10 | 2008-08-27 | 株式会社荒木鉄工 | Distributed device |
| JP4189831B2 (en) * | 1999-10-25 | 2008-12-03 | 株式会社井上製作所 | Media distribution device |
| JP4054520B2 (en) * | 2000-11-16 | 2008-02-27 | 株式会社資生堂 | Method for producing emulsified cosmetic containing hydrophobized powder |
| US20040085856A1 (en) * | 2002-10-30 | 2004-05-06 | Murosako James K. | Mixer |
| JP4174000B2 (en) * | 2003-02-27 | 2008-10-29 | 株式会社荒木鉄工 | Distributed device |
| CN201399361Y (en) * | 2009-03-25 | 2010-02-10 | 蔡澳明 | Basket type sand mill |
| CN104383989B (en) * | 2014-10-31 | 2017-02-01 | 罗斯（无锡）设备有限公司 | Grinding miller structure |
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2015
- 2015-09-11 JP JP2015179627A patent/JP6326020B2/en active Active
-
2016
- 2016-03-25 MY MYPI2016701081A patent/MY188495A/en unknown
- 2016-04-08 SG SG10201602814UA patent/SG10201602814UA/en unknown
- 2016-04-29 CN CN201610276307.3A patent/CN106513116B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| MY188495A (en) | 2021-12-15 |
| CN106513116A (en) | 2017-03-22 |
| JP6326020B2 (en) | 2018-05-16 |
| JP2017051929A (en) | 2017-03-16 |
| SG10201602814UA (en) | 2017-04-27 |
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