CN107824321A - A kind of liquid clasfficiator for colloid mill - Google Patents
A kind of liquid clasfficiator for colloid mill Download PDFInfo
- Publication number
- CN107824321A CN107824321A CN201711293209.1A CN201711293209A CN107824321A CN 107824321 A CN107824321 A CN 107824321A CN 201711293209 A CN201711293209 A CN 201711293209A CN 107824321 A CN107824321 A CN 107824321A
- Authority
- CN
- China
- Prior art keywords
- clasfficiator
- colloid mill
- finished product
- liquid
- product discharge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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- 239000000084 colloidal system Substances 0.000 title claims abstract description 41
- 239000007788 liquid Substances 0.000 title claims abstract description 23
- 239000012634 fragment Substances 0.000 claims abstract description 35
- 230000007246 mechanism Effects 0.000 claims abstract description 29
- 239000000919 ceramic Substances 0.000 claims description 36
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 8
- 239000000463 material Substances 0.000 abstract description 80
- 238000000227 grinding Methods 0.000 description 97
- 238000005520 cutting process Methods 0.000 description 34
- 230000003068 static effect Effects 0.000 description 28
- 230000000694 effects Effects 0.000 description 16
- 238000001914 filtration Methods 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000011049 pearl Substances 0.000 description 9
- 238000010008 shearing Methods 0.000 description 8
- 239000011324 bead Substances 0.000 description 7
- 238000007599 discharging Methods 0.000 description 6
- 238000003801 milling Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000004945 emulsification Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 238000005096 rolling process Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
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- 244000068988 Glycine max Species 0.000 description 2
- 235000010469 Glycine max Nutrition 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
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- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000005580 one pot reaction Methods 0.000 description 2
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910001928 zirconium oxide Inorganic materials 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 235000013527 bean curd Nutrition 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 229910001651 emery Inorganic materials 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000001238 wet grinding Methods 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- 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
- B02C17/10—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 with one or a few disintegrating members arranged in the container
-
- 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
-
- 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
- B02C17/20—Disintegrating members
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/02—Feeding devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/10—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
- B02C23/12—Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone with return of oversize material to crushing or disintegrating zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/02—Crushing or disintegrating by disc mills with coaxial discs
- B02C7/04—Crushing or disintegrating by disc mills with coaxial discs with concentric circles of intermeshing teeth
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
- B02C7/12—Shape or construction of discs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
- B02C7/16—Driving mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/175—Disc mills specially adapted for paste-like material, e.g. paint, chocolate, colloids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/02—Arrangement of air or material conditioning accessories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Abstract
The invention discloses a kind of liquid clasfficiator for colloid mill, including clasfficiator shell, finished product discharge line and classification mechanism, one end of the finished product discharge line is inserted and upwardly extended from the clasfficiator outer casing bottom；The clasfficiator side wall of outer shell lower end, which is provided with back, grinds flow export；The classification mechanism includes buncher and clasfficiator revolving fragment, and the clasfficiator revolving fragment is set in outside the finished product discharge line；The upper end of the clasfficiator revolving fragment is connected with the buncher, and the buncher can drive the clasfficiator revolving fragment to be rotated by axis of the finished product discharge line.A kind of liquid clasfficiator for colloid mill of the present invention is rotated using clasfficiator revolving fragment to material, the material of different thicknesses degree is set to produce different speed so as to be layered, thicker material continues to grind from returning to grind flow export and flow back into colloid mill, satisfactory material is entered in finished product discharge line from leaking hole and discharged, convenient and swift.
Description
Technical field
The present invention relates to mechanical field, more particularly to a kind of liquid clasfficiator for colloid mill.
Background technology
Colloid mill is the conventional scattered milling apparatus of the industries such as food, chemical industry, medicine, building materials, especially building coating factory
House, commonly use colloid mill grinding material.
Traditional colloid mill main part is made up of housing, stator, rotor, governor motion, cooling body, motor etc..Shell
Body is provided with hopper, and housing bottom is provided with two passages, a drain hole and a feedback outlet.During usual grinding material, thing
Material is added in colloid mill charge funnel, is closed drain hole, is started motor, and material starts to grind, and material is in grinding from feed back
Mouth, which is pumped into, to be back in charge funnel, is ground with not having the material of grinding to be together again introduced into colloid mill in charge funnel,
Such multiple circular grinding, until grinding the material to required fineness, drain hole is opened, material is released.
The special clasfficiator of the typically no configuration of colloid mill currently on the market, the fineness degree of polished material may be not
Reach production requirement just to be exported by finished product, one pot of one pot of ground mill, it is impossible to continuous production, cause product quality to decline.
The content of the invention
The shortcomings that in order to overcome prior art and deficiency, the invention discloses a kind of liquid clasfficiator for colloid mill,
Including clasfficiator shell, finished product discharge line and classification mechanism, one end of the finished product discharge line is from the clasfficiator shell
Bottom is inserted and upwardly extended；The clasfficiator side wall of outer shell lower end, which is provided with back, grinds flow export；The classification mechanism includes adjusting
Speed motor and clasfficiator revolving fragment, the clasfficiator revolving fragment are set in outside the finished product discharge line；The clasfficiator rotation
The upper end of piece is connected with the buncher, and the buncher can drive the clasfficiator revolving fragment to be discharged with the finished product
Pipeline rotates for axis.
Further, the upper end of the finished product discharge line is provided with leaking hole.
Further, the upper end of the finished product discharge line is concordant with the clasfficiator shell upper end.
Further, the leaking hole is circular hole.
Further, the outer wall of the finished product discharge line is provided with clasfficiator and fixes ceramic bearing, the clasfficiator rotation
The lower end of rotor is connected on the fixed ceramic bearing.
Further, the fixed ceramic bearing is zirconia ceramics bearing.
Further, the clasfficiator revolving fragment is taper barrel, and its diameter is from top to bottom gradually reduced.
Further, the clasfficiator outer casing inner wall is provided with flow deflector.
Further, the flow deflector is spiral vane.
Further, the clasfficiator shell is infundibulate.
A kind of liquid clasfficiator for colloid mill of the present invention utilizes clasfficiator revolving fragment to material in clasfficiator
Scroll-tupe rotates, and produces a peripherad centrifugal force so that the water that flows into the material mixt of clasfficiator, bulky grain,
In the material of little particle, liquid etc.：The material of larger particles, heavier material, can be in the presence of rotary centrifugal force
It is preferential to throw away close to the rotation of clasfficiator inwall, because clasfficiator inwall is provided with spiral flow deflector, so the material of larger particles, heavier
Material the bottom of clasfficiator can be preferentially transferred in the presence of spiral flow deflector, return to funnel regrinding.Thinner
Lighter being always held among clasfficiator rotates, and is provided with finished product discharge line among clasfficiator, and go directly product outlet.Reach
To the purpose of classification.It is convenient and swift, it is possible to achieve quantity-produced purpose.There is no screen pack setting, without midway cleaning and
The worry of network blocking.
In order to more fully understand and implement, the invention will now be described in detail with reference to the accompanying drawings.
Brief description of the drawings
Fig. 1 is the schematic diagram of the present invention.
Fig. 2 is the enlarged diagram of grinding mechanism of the present invention.
Embodiment
Fig. 1 and 2 is referred to, the invention discloses a kind of ultra micro colloid mill apparatus, including base 10 and is arranged on described
Drive mechanism, colloid mill grinding mechanism, funnel on base 10, the liquid clasfficiator for colloid mill, classification connecting tube 15 and
Return and grind pipeline 16.The funnel is arranged on above the grinding mechanism, and the drive mechanism can convey dynamic to the grinding mechanism
Power, the liquid clasfficiator for colloid mill are connected with the funnel and the colloid mill grinding mechanism respectively.The funnel
Discharging opening be connected with the charging aperture of the colloid mill grinding mechanism, the discharging opening of the colloid mill grinding mechanism and the classification
One end of connecting tube 15 is connected, and the other end of the classification connecting tube 15 is communicated to the liquid clasfficiator for being used for colloid mill,
Described time the both ends for grinding pipeline 16 are respectively connecting to the funnel and the clasfficiator.The both ends difference of the classification connecting tube 15
For connecting tube inflow entrance 151 and connecting tube flow export, the discharging opening of the connecting tube inflow entrance 151 and colloid mill grinding mechanism connects
Logical, the connecting tube flow export 152 is arranged in the clasfficiator.
The drive mechanism includes motor 11, belt pulley 12, belt 13 and driving shaft 14.The motor 11
Output shaft is connected by belt 13 with the belt pulley 12, and the belt pulley 12 is fixed on the driving shaft 14, so as to pass through
The belt pulley 12 drives the driving shaft 14 to rotate.The driving shaft 14 is inserted into described grind below the grinding mechanism
In grinding machine structure.
The funnel includes funnel body 21, funnel revolving fragment 22, spiral flow deflector 23, water inlet 24, V-arrangement protective cover 25
With strong magnetic filter 26.The lower end of the funnel body 21 is provided with discharging opening, and the V-arrangement protective cover 25 is arranged on the funnel
The top surface of body 21, ensure the safety of safeguard work personnel during machine operation.The spiral flow deflector 23 is arranged on the funnel
The inwall of body 21, the spiral flow deflector 23 is from the inwall upper end edge spiral shape of the funnel body 21 to the funnel body
21 discharging opening extension.The water inlet 24 is arranged on the upper end of the hopper side walls, and the water inlet 24 is led with the spiral
Flow 23 is equidirectional, and the water inlet 24 connects the fluidic interface of outside need mill, or is directly connected to water.The funnel rotation
Rotor 22 is arranged in the funnel body 21, and the funnel revolving fragment 22 can be by external connection power source so as to rotation.It is described strong
Magnetic filter 26 is arranged on the lower end discharging opening outer wall of the funnel body 21, will be by strong magnetic when there is swarf to be strayed into
Firmly, avoid damaging mill.In the present embodiment, the funnel revolving fragment 22 in the funnel is triangle rotating piece, the funnel rotation
The width of rotor 22 is from top to bottom gradually reduced.The direction of rotation of the funnel revolving fragment 22 and the extension side of spiral flow deflector 23
To be equidirectional, the side wall lower ends of funnel body 21 are provided with for grinding inflow entrance 27 for returning for feed back.The funnel
Revolving fragment 22 is connected with screw rod.
Colloid mill funnel with the funnel revolving fragment 22 of rotation using that can drive Scroll-tupe of the material in funnel to rotate, together
When spiral flow deflector 23 material can be allowed to keep certain track to carry out Scroll-tupe slip, and produce a peripherad centrifugal force,
So that add in the material of the water needed in grind materials mixture of funnel, solid, bulky grain, little particle, liquid etc.：Larger
Material, heavier material, the solid material of grain, can be in the presence of rotary centrifugal force and in the presence of spiral flow deflector 23
Funnel bottom preferentially is transferred to, is ground so as to preferentially enter mill area, reaches the function of differential grinding after classification.Directly improve
Milling zone needs efficiency and the useful work ground.Greatly reduce it is honed after material repeat mill idle work.Add in funnel
When having floating object or producing foam, floating object or foam can preferentially be involved in funnel bottom under vortex action power.Reduce mill
Less than fish that has escape the net.
The funnel revolving fragment 22 is inserted from the lower end exit of funnel body 21 and protruding upward, the funnel rotation
Piece 22 is located on the central axis of spiral flow deflector 23, and the lower end of the funnel revolving fragment 22 is connected with driving shaft 14, described
Drive mechanism can drive the funnel revolving fragment 22 rotation on the central axis of the spiral flow deflector 23.In funnel revolving fragment
22 drive under rotation, and in the presence of inertia, and in the presence of inner wall of hopper spiral flow deflector 23, material can accelerate to screw in material
Just grinder is ground one-level, and material can be avoided not preferentially enter milling zone timely and effectively after being put into funnel.
The colloid mill grinding mechanism of the present invention includes grinding housing, multiple static cutting disks and multiple movable grinding discs, the movable grinding disc
Outer surface and the static cutting disk inner surface are equipped with roll flute, and the static cutting disk is arranged on the inwall of the corresponding grinding shell,
The movable grinding disc is arranged in the corresponding static cutting disk, and certain interval, institute are left between the static cutting disk and the movable grinding disc
State movable grinding disc to be connected with the drive mechanism, the driving machine drives the movable grinding disc to rotate.Material is from static cutting disk and movable grinding disc
Between gap flowing, and be ground.The driving shaft 14 is relatively fixed through the movable grinding disc and with the multiple movable grinding disc,
So as to allow the driving shaft 14 to drive the movable grinding disc to rotate.The grinding mechanism be divided into from top to bottom arrange first mill area,
Second mill area, the 3rd mill area, the 4th mill area and the 5th mill area.
The first mill area includes first mill area's shell 35 and the be arranged in the first mill area's shell 35 the 1st
Level static cutting disk 31, the first one-level movable grinding disc 32, the first two level static cutting disk 33 and the first two level movable grinding disc 34.First one-level is quiet
Mill 31 is arranged on the first two level static cutting disk 33, and the first one-level movable grinding disc 32 is arranged on the dynamic mill of first two level
On disk 34.First mill area primarily serves the effect of just broken corase grind to material, can carry out preliminary destruction to material and pulverize.
The first one-level static cutting disk 31 is the straight roll flute of reverse sawtooth line, often encloses roll flute number no less than 60, the described 1st
Level movable grinding disc 32 is the positive left inclined screw tooth of 25 degree of sawtooth, and in the first one-level static cutting disk 31 and the first one-level movable grinding disc
Diamond is coated with 32, the first one-level static cutting disk 31 is fixed on the first mill area's shell 35, and first one-level is moved
Mill 32 is arranged on main shaft.The spacing of the first one-level static cutting disk 31 and the first one-level movable grinding disc 32 is 10~20
Silk, both mutually never contact.
The first two level static cutting disk 33 is square teeth, often encloses the number of teeth and is no less than 60, square teeth anterior angle is minus 10
Degree, and a plurality of cross-flow groove is carried, multiple cross-flow grooves are lined up as square block diagonal strip shape.This cross-flow groove is right oblique 2 degree.Described
One two level movable grinding disc 34 is cylindrical milling cutter tooth, often encloses the number of teeth and is no less than 60, cylindrical milling cutter rake angle is minus 15 degree, is 25
Spend left inclined screw tooth.The first two level static cutting disk 33 is fixed on the first mill area's shell 35, the dynamic mill of first two level
Disk 34 is arranged on the first one-level movable grinding disc 32.The first two level static cutting disk 33 and the first two level movable grinding disc 34
Spacing is 4~6 silks, and both mutually never contact.
The first mill area the advantages of so setting is that just broken power is strong, eats that the amount of cutting is big, and corase grind effect is good, and makes grinding charge material
Powerful downward mobilization power is produced, is that the three-dimensional edge of a knife carries out closing compact form shearing when mill interacts, generation, which is grabbed, cuts original
Reason, makes grinding charge material not skidded in shear history, and the dissimilar tooth form for the roll flute for passing through setting and front-and-back angle are come to thing
Material is effectively ground so that continuous baffling and rolling on roll flute by material so that grinding charge material can be by different angle
Be sheared, because baffling and rolling are not easy to miss the chance of shearing in shear history, improve grinding efficiency so that grinding efficiency
It is higher more abundant.Caused temperature is not more than 50 degree in process of lapping, meets grinding requirement of the client to special material.
Mill hardness is superpower, not easy to wear.
The second mill area is the second ceramic bearing group 41, and the second ceramic bearing group 41 also is located at the first mill area
In shell 35.The driving shaft 14 passes through the second ceramic bearing group 41, and the second ceramic bearing group 41 is by two full pearls
Ceramic bearing mounted on top forms, wherein being provided with oil sealing at following full pearl ceramic bearing both ends, ceramic bearing below plays
Stablize the effect of the position of driving shaft 14, meanwhile, above ceramic bearing can be right during material from top to bottom flows
Material through bearing ball is rolled,.Above-mentioned bearing is full pearl, and material is corrosion resistant zirconia material.Material passes through
When, bearing bead high-speed rotation, phase mutual friction.Grinding charge material is effectively rolled and rubbed, changes the thing that upper level gets off
Expect geometry, more preferable preparation is played to obtain more fully shearing into next stage mill area.
The 3rd mill area includes the 3rd mill area's shell 55 and the be arranged in the 3rd mill area's shell 55 the 3rd 1
Level static cutting disk 51, the 3rd one-level movable grinding disc 52, the 3rd two level static cutting disk 53 and the 3rd two level movable grinding disc 54.3rd one-level is quiet
Mill 51 is arranged on the 3rd two level static cutting disk 53, and the 3rd one-level movable grinding disc 52 is arranged on the dynamic mill of the 3rd two level
On disk 54.Fine grinding is played a part of in 3rd mill area to material and fine grinding emulsifies.Lock nut 43 is connected to grind the described 3rd outside area
Shell 55 is connected and fixed with cylinder staving 61.
The 3rd one-level static cutting disk 51 is that wedge angle reverse side shape tooth is processed into, and often encloses the number of teeth and is no less than 90, each point
Angle reverse side shape space width≤1.5mm, each total height≤1.5mm of wedge angle reverse side shape teeth groove.Anterior angle on tooth is minus 10 degree, up and down point
Angle reverse side shape tooth row is classified as right oblique 2 degree, and forms wedge angle reverse side shape groove, and multiple wedge angle reverse side shape grooves line up lightning mark reverse side shape
Right slanted bar shape.The right slanted bar shape total length of this lightning mark reverse side shape at least >=30mm.
The 3rd one-level movable grinding disc 52 is that wedge angle reverse side shape tooth is processed into, and often encloses the number of teeth and is no less than 90, each point
Angle reverse side shape space width≤1.5mm, each total height≤1.5mm of wedge angle reverse side shape teeth groove.Anterior angle on tooth is minus 10 degree, up and down point
Angle reverse side shape tooth row is classified as left oblique 25 degree, and forms wedge angle reverse side shape groove, and multiple wedge angle reverse side shape grooves line up lightning mark reverse side
The left slanted bar shape of shape.The right slanted bar shape total length of this lightning mark reverse side shape at least >=30mm.
The 3rd one-level static cutting disk 51 is arranged on the described 3rd mill area's shell 55, and the 3rd one-level movable grinding disc 52 is pacified
On main shaft.The 3rd one-level movable grinding disc 52 and the 3rd one-level static cutting disk 51 are not in contact with each other, between the two away from
From for 3~4 silks.There is powerful grabbing to cut function for setting between the static cutting disk of the one-level in the 3rd mill area and movable grinding disc grinding,
It is not easy to skid, grabs and the rolling of reverse side shape is constantly pointed at after cutting, grinding charge material is constantly overturn, forces grinding charge material from different several
What angle is fully cut.This cutting times greatly increases, per minute up to million times.Grinding charge material passes through the gap between mill
When, by powerful shearing force, frictional force, dither, the physical action such as high speed vortex, high-speed impact, to being had by material
Superpower scattered, homogeneous, crushing, stirring, the fineness of effect material of grinding are up to 4um ranks.
In following ceramics in the full pearl ceramic bearing group 42 in the mill of full pearl ceramic bearing group 41 and the 4th area in the second mill area
The bearing assembling fixation of driving shaft 14, the second mill area and the 4th mill area are by two completely above and below pearl ceramic bearings
Stack together, wherein following play fixation, there is oil sealing at bearing both ends, and porcelain bearing above, which serves, to roll.Described second
It is full pearl ceramic bearing to grind area and the 4th mill area.
Not phase mutual friction when being worked between the 3rd one-level static cutting disk 51 and the 3rd one-level movable grinding disc 52, temperature lifting are controllable
Within 10 DEG C, material and mill produce heat and material cut the heat that discharges in itself can be in water leaking-in or by grinding fluid body
In rapidly enter next mill area.
The two level mill in the 3rd mill area mainly plays fine grinding emulsification.
The 3rd two level static cutting disk 53 is processed into for sawtooth, often encloses the number of teeth no less than 100, and each sawtooth groove width≤
1.5mm, each total height≤1.5mm of z fonts teeth groove.Anterior angle on tooth is positive 10 degree, and upper and lower sawtooth is arranged as right oblique 2 degree, and shape
Into the staggered groove of sawtooth, multiple kerves are staggered into right slanted bar shape.This staggered sawtooth strip total length is extremely
Few >=30mm.
The 3rd two level movable grinding disc 54 is processed into for sawtooth, often encloses the number of teeth and is no less than 100, each saw space width
≤ 1.5mm, each total height≤1.5mm of serrated slot.Anterior angle on tooth is positive 10 degree, and upper and lower sawtooth is arranged as staggered, and shape
Into the groove that staggers, this groove total length at least >=30mm.
The 3rd two level static cutting disk 53 is arranged on the 3rd mill area's shell 55, and the 3rd two level movable grinding disc 54 is arranged on
On main shaft.Be not in contact with each other between the 3rd two level movable grinding disc 54 and the 3rd two level static cutting disk 53, between the two away from
From for 3~4 silks.There is powerful grabbing to cut work(for the grinding of the 3rd two level static cutting disk 53 and the 3rd two level movable grinding disc 54
Can, it is not easy to skid, has to grab and cut rear continuous baffling, grinding charge material is constantly overturn, force grinding charge material from different geometry angles
Degree fully cutting.This cutting times greatly increases, per minute up to million times.When grinding charge material is by gap between mill,
It is superpower to being had by material by powerful shearing force, frictional force, dither, the physical action such as high speed vortex, high-speed impact
Broken wall emulsification (this is main purpose), simultaneously also have：Scattered, homogeneous, crushing, stirring, the effect of grinding sum are ground
The fineness of material is up to 3um ranks, during work temperature lifting can be controlled in 15 DEG C.
The 4th mill area is the 4th ceramic bearing group 42, and the 4th ceramic bearing group 42 also is located at the first mill area
In shell 35.The driving shaft 14 passes through the 4th ceramic bearing group 42, and the 4th ceramic bearing group 42 is by two full pearls
Ceramic bearing mounted on top forms, wherein being provided with oil sealing at following full pearl ceramic bearing both ends, ceramic bearing below plays
Stablize the effect of the position of driving shaft 14, meanwhile, above ceramic bearing can be right during material from top to bottom flows
Material through bearing ball is rolled.
The 5th mill area be sanding device, including cylinder staving 61, rotating wheel 62, grinding bead 63, upper filters the and of cover plate 64
Lower filtering cover plate 65.The upper filtering cover plate 64 is arranged on the upper end of cylinder staving 61, and the lower filtering cover plate 65 is arranged on
Filter bores are provided with the lower end of cylinder staving 61, the upper filtering cover plate 64 and the lower filtering cover plate 65.Material is through institute
Flowed into after the grinding in Shu Simo areas from the upper filtering cover plate 64 in the cylinder staving 61.The driving shaft 14 by lower and
On through the lower filtering cover plate 65, cylinder staving 61 and upper filtering cover plate 64, the rotating wheel 62 is located at the cylinder staving
In 61 and it is set on the driving shaft 14, the rotating wheel 62 can be rotated with the driving shaft 14 and rotated, the rotating wheel
The grinding bead 63 is provided between 62 and the cylinder staving 61.The rotating wheel 62 can drive the grinding bead 63 when rotating
Move, the collision friction between the grinding bead 63 further can produce grinding effect to material.The appearance of rotating wheel 62
Face set fluted 621, the groove 621 along the rotating wheel circumferentially.The cross section of the groove 621 is V-arrangement.Utilize
The uneven motion that can further increase the grinding bead 63 on the surface of rotating wheel 62.The rotating wheel 62 is oxidation
Zircon ceramic rotating wheel 62.The upper filtering cover plate 64 and the 4th is provided with central shaft fixation ceramic bearing 44 between grinding area.It is described
Cylinder staving 61, the rotating wheel 62, the upper filtering cover plate 64 and the lower filtering cover plate 65 are made by zirconium oxide, described
Grinding bead 63 is zirconium oxide material.Material is ground in the 5th mill area, makes to get off inherently very high-fineness from the 4th mill area
Material be sanded again, realize the effect that ultra micro melts, highest can make materials fine degree reach 2um ranks.
Grind pipeline 16 by being classified connecting tube 15 and returning between the grinding mechanism and the clasfficiator and connect.Described 5th
The lower section for grinding the lower filtering cover plate 65 in area is connected with the inflow entrance of the classification connecting tube 15, the connection of the classification connecting tube 15
Pipe flow export 152 is communicated to the clasfficiator.
The liquid clasfficiator for colloid mill includes clasfficiator shell 72, finished product discharge line 73 and classification mechanism,
The classification mechanism discharges material up to standard after classification from the finished product discharge line 73, and material not up to standard is from the Hui Yan
Pipeline 16 flows back into the funnel body 21.The classification mechanism includes buncher 71 and clasfficiator revolving fragment 74, described point
The flow export of level connecting tube 15 is arranged in the clasfficiator shell 72, and the inwall of clasfficiator shell 72 is provided with spiral shape and led
Flow 75.The clasfficiator shell 72 is infundibulate, and one end of the finished product discharge line 73 is from the bottom of clasfficiator shell 72
Portion inserts and upwardly extended, and the outer wall of the finished product discharge line 73 is provided with clasfficiator and fixes ceramic bearing 76, the classification
Device revolving fragment 74 is set in outside the finished product discharge line 73, and the lower end of the clasfficiator revolving fragment 74 is connected to the clasfficiator
On fixed ceramic bearing 76, the upper end of the clasfficiator revolving fragment 74 is connected with the buncher 71, the buncher 71
The clasfficiator revolving fragment 74 can be driven to be rotated with the finished product discharge line 73 for axis.The finished product discharge line 73
Upper end is provided with leaking hole 731, finished product discharge line described in the present embodiment 73 the clasfficiator fix ceramic bearing 76 with
On part be provided with leaking hole 731.The connecting tube flow export of the classification connecting tube 15 is located at the clasfficiator revolving fragment 74
Top.In the present embodiment, the clasfficiator revolving fragment 74 is taper barrel, and its diameter is from top to bottom gradually reduced.The connection
Pipe flow export is positioned at the top of clasfficiator revolving fragment 74.The fixed ceramic bearing 76 is zirconia ceramics bearing.Described point
The side wall lower ends of level device shell 72, which are provided with back, grinds flow export 721.Outside the upper end of the finished product discharge line 73 and the clasfficiator
The upper end of shell 72 is concordant, and the leaking hole 731 is circular hole.
The returning of described time one end for grinding pipeline 16 and the side wall lower ends of the clasfficiator shell 72 is ground flow export 721 and is connected,
The other end is connected to the side wall lower ends of the funnel body 21, grinds for described time and check valve 161 is provided with pipeline 16, described unidirectional
The flow direction of valve 161 is arranged to flow to the funnel body 21 from the clasfficiator shell 72.It is additionally provided with below grinding mechanism
One cleaning outlet 45, the cleaning outlet 45 are communicated to the classification connecting tube 15, and the cleaning outlet 45 can play on or off
Close.
Material is poured into the funnel, is filtered through the water conservancy diversion of spiral flow deflector 23, then through the strong magnetic filter 26,
Then the grinding mechanism is flowed into from the bottom of the funnel, five Ge Mo areas of the material through the grinding mechanism are from top to bottom
Grinding, eventually flow into the classification connecting tube 15, flowed to through the classification connecting tube 15 in the clasfficiator, the clasfficiator
Buncher 71 drives the clasfficiator revolving fragment 74 to rotate.Larger material grain can be thrown out of the clasfficiator because of centrifugal force
Revolving fragment 74, then preferentially flow to described return downwards according to spiral flow deflector from the inwall of clasfficiator shell 72 and grind pipeline 16, through institute
State back and grind pipeline 16 and flow back into the funnel body 21, be ground again；And meet thickness requirement smaller material because from
Mental and physical efforts are smaller and still remain in the clasfficiator revolving fragment 74, enter through the leaking hole 731 on the finished product discharge line 73
In to the finished product discharge line 73, flow downward out.Material can be ground into 1um ranks by highest.
For the ultra micro colloid mill apparatus of the present invention compared with common colloid mill prior art, the present invention has advantages below：
(1) power is compared to relatively low, 2.2 kilowatts high with regard to Yield comparison, and thinning effect is also ultra-fine, the low-voltage of 220v electricity,
The slow-speed of revolution grinds high fineness effect, and fineness is thinner with condition in the whole nation, temporarily in most advanced level.Low-voltage, the slow-speed of revolution,
Low-power machine can make client's utilization scope than wide.
(2) to the string of flexible, oiliness, the property of water-bearing, containing moist fiber etc., thinning effect is ultra-fine,
For example soya bean 99% passes through the mesh of 100 mesh -500.Accomplish the defibrination machine really without slag soya-bean milk bean curd, mouthfeel is smooth, really nothing
Grain sense.
(3) this grinder is typically at 4000 revs/min, slow-speed of revolution can reach high fineness requirement (temporarily domestic only
Have).It is general to be not required to configure frequency converter and cooling device, cut down expenses in cost for client.
(4) this grinding machine, mill never contact, and the edge of a knife is sharp, and precision is higher.Life-span is common colloid mill more than 10 times.Just
Normal use is in addition to artificial damage, and if feeding on request, mill can use more than 5 years.
(5) this grinder, mill are independent entirety, will be best precision speciality when dispatching from the factory, whole when need to such as change
Body is changed to producer, and it is exactly brand-new machine that client, which installs, brand-new thinning effect.Client school abrasive disk space is not needed.
(6) this grinder, mill do not rub between each other, and strengthen hardness specially treated by Germany technology, no
Get rusty, food-grade, basic hardness is high, and case hardness is in 1200HV, good toughness.So abrasion is seldom, can almost ignore.
(7) solve temperature this great problem for client, can be controlled in feeding temperature height without temperature during additional cooling
10 ° or so (see material and distinguish).The physical property and chemical property of grinding material will not be changed.
(8) mill selection：Using the food-grade stainless steel of Japanese import, Germany technology processing, reach it is medical enter operation on mouth
On the rank of knife.This material non-corrosive, food-grade, medical grade.Have that hardness is high, the edge of a knife is sharp, extremely abrasive, toughness simultaneously
All very moderate with fragility, cost price is higher but the advantages of trusting handy and long lifespan.
(9) the disposable finished product percent of pass that grinds is very high, up to 99%.Realize uninterrupted continuous production.
(10) in structure technology, material has obvious grinding based on shearing, broken wall, mixes, and stirs, emulsification,
Matter, the mutual warm effect for melting mill.Grind in shearing work：(during by two to the edge of a knife, cut, do not pass through through cutting in principle
With regard to passing by, easily skid) add to grab and cut principle (3 cut to the edge of a knife is mutually crowded), while material can also constantly turn over stream in milling zone,
About 100,000 beats/min of number of stream is turned over, turns over and shears.Millions of beats/min of shearing time.The string of flexible is sheared
When the material that easily skids can grab and cut (3 mutually squeezed to the edge of a knife cut) effect.
(11) thickness is more or less the same than more uniform, easy to use to client.Pulping rate is higher, and customer utilization also carries
Height, thinning effect is relatively good, and client's discomposing effect might as well be a lot.
(12) this grinding machine structure independently assembles, and maintenance is convenient.Machine inner structure precision is higher, long lifespan.
(13) noise in the course of work is smaller, is difficult to without " chirp chirp " caused by mill phase mutual friction pleasant
In a shrill voice.
(14) the machine is provided with cleaning interface, can once be cleaned up in half a minute inner high voltage.
The ultra micro colloidal mill cost of the present invention is relatively low, long lifespan, low temperature, high fineness, low speed, low-voltage, environmental protection and energy saving.
Machine materials food-grade, use range are very extensive.It is the upgrade version of common colloid mill, is the following hair for substituting common colloid mill
The new birth product of exhibition, and common burrstone mill, emery wheel grinding machine, ball mill, breast machine, three-roller, bruisher, sub.
Still another recent development technology of wet grinding mill, development prospect are wide simultaneously.And large-scale national Important Project can be used
On.The field industry of the company and enterprise more needed, individual and each needs is may also aid in, solves the corresponding various difficulties of grinding
Topic.
Above-described embodiment is the preferable embodiment of the present invention, but embodiments of the present invention are not by above-described embodiment
Limit, change, modification, replacement, combination, the simplification made under other any scopes and principle without departing from the present invention,
It is equivalent substitute mode, is included within protection scope of the present invention.
Claims (10)
- A kind of 1. liquid clasfficiator for colloid mill, it is characterised in that：Including clasfficiator shell, finished product discharge line and classification Mechanism, one end of the finished product discharge line are inserted and upwardly extended from the clasfficiator outer casing bottom；The clasfficiator shell Side wall lower ends, which are provided with back, grinds flow export；The classification mechanism includes buncher and clasfficiator revolving fragment, the clasfficiator rotation Rotor is set in outside the finished product discharge line；The upper end of the clasfficiator revolving fragment is connected with the buncher, the tune Speed motor can drive the clasfficiator revolving fragment to be rotated by axis of the finished product discharge line.
- A kind of 2. liquid clasfficiator for colloid mill according to claim 1, it is characterised in that：The finished product discharge pipe The upper end in road is provided with leaking hole.
- A kind of 3. liquid clasfficiator for colloid mill according to claim 2, it is characterised in that：The finished product discharge pipe The upper end in road is concordant with the clasfficiator shell upper end.
- A kind of 4. liquid clasfficiator for colloid mill according to claim 2, it is characterised in that：The leaking hole is circle Hole.
- A kind of 5. liquid clasfficiator for colloid mill according to claim 1, it is characterised in that：The finished product discharge pipe The outer wall in road is provided with clasfficiator and fixes ceramic bearing, and the lower end of the clasfficiator revolving fragment is connected to the fixed ceramic bearing On.
- A kind of 6. liquid clasfficiator for colloid mill according to claim 5, it is characterised in that：The fixed ceramic shaft Hold as zirconia ceramics bearing.
- A kind of 7. liquid clasfficiator for colloid mill according to claim 1, it is characterised in that：The clasfficiator rotation Piece is taper barrel, and its diameter is from top to bottom gradually reduced.
- A kind of 8. liquid clasfficiator for colloid mill according to claim 1, it is characterised in that：The clasfficiator shell Inwall is provided with flow deflector.
- A kind of 9. liquid clasfficiator for colloid mill according to claim 8, it is characterised in that：The flow deflector is spiral shell Revolve shape flow deflector.
- A kind of 10. liquid clasfficiator for colloid mill according to claim 1, it is characterised in that：Outside the clasfficiator Shell is infundibulate.
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| CN201711293209.1A CN107824321B (en) | 2017-12-08 | 2017-12-08 | Liquid classifier for colloid mill |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111387513A (en) * | 2020-04-23 | 2020-07-10 | 西南科技大学 | Method for extracting pleurotus djamor dietary fiber |
| CN112169910A (en) * | 2019-07-03 | 2021-01-05 | 上海谷励智能设备有限公司 | Quick radiating ceramic mill device |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4405454A (en) * | 1980-05-28 | 1983-09-20 | Krauss-Maffei Aktiengesellschaft | Process and apparatus for the dewatering of solids in suspension |
| CN1966121A (en) * | 2006-10-30 | 2007-05-23 | 周俊培 | Multiple stage continuous adverse current type centrifugal leaching device suitable for powdery material |
| CN200940148Y (en) * | 2006-04-16 | 2007-08-29 | 孙利涵 | Centrifugal treatment equipment for steel slag |
| CN201579126U (en) * | 2009-12-17 | 2010-09-15 | 于春梅 | Inner spiral groove type hydroclone |
| CN105396650A (en) * | 2015-09-22 | 2016-03-16 | 广州派勒机械设备有限公司 | Screen-free type intelligent nanometer grinding system |
| CN205704374U (en) * | 2016-04-20 | 2016-11-23 | 杭州华威药业股份有限公司 | A kind of Chinese medicine shearing device |
| CN106334354A (en) * | 2015-07-17 | 2017-01-18 | 重庆蓝洁广顺净水材料有限公司 | Energy-saving diversion type cyclone separator |
| CN107252725A (en) * | 2017-07-29 | 2017-10-17 | 赣州伟嘉合金有限责任公司 | A kind of tungsten powder milling apparatus and control method |
| CN207667795U (en) * | 2017-12-08 | 2018-07-31 | 韶关市超微磨机设备有限公司 | A kind of liquid clasfficiator for colloid mill |
-
2017
- 2017-12-08 CN CN201711293209.1A patent/CN107824321B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4405454A (en) * | 1980-05-28 | 1983-09-20 | Krauss-Maffei Aktiengesellschaft | Process and apparatus for the dewatering of solids in suspension |
| CN200940148Y (en) * | 2006-04-16 | 2007-08-29 | 孙利涵 | Centrifugal treatment equipment for steel slag |
| CN1966121A (en) * | 2006-10-30 | 2007-05-23 | 周俊培 | Multiple stage continuous adverse current type centrifugal leaching device suitable for powdery material |
| CN201579126U (en) * | 2009-12-17 | 2010-09-15 | 于春梅 | Inner spiral groove type hydroclone |
| CN106334354A (en) * | 2015-07-17 | 2017-01-18 | 重庆蓝洁广顺净水材料有限公司 | Energy-saving diversion type cyclone separator |
| CN105396650A (en) * | 2015-09-22 | 2016-03-16 | 广州派勒机械设备有限公司 | Screen-free type intelligent nanometer grinding system |
| CN205704374U (en) * | 2016-04-20 | 2016-11-23 | 杭州华威药业股份有限公司 | A kind of Chinese medicine shearing device |
| CN107252725A (en) * | 2017-07-29 | 2017-10-17 | 赣州伟嘉合金有限责任公司 | A kind of tungsten powder milling apparatus and control method |
| CN207667795U (en) * | 2017-12-08 | 2018-07-31 | 韶关市超微磨机设备有限公司 | A kind of liquid clasfficiator for colloid mill |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112169910A (en) * | 2019-07-03 | 2021-01-05 | 上海谷励智能设备有限公司 | Quick radiating ceramic mill device |
| CN111387513A (en) * | 2020-04-23 | 2020-07-10 | 西南科技大学 | Method for extracting pleurotus djamor dietary fiber |
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| CN107824321B (en) | 2024-04-16 |
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