CN106984409A - Aspirator and application method are crushed in a kind of rice protein negative pressure series connection - Google Patents
Aspirator and application method are crushed in a kind of rice protein negative pressure series connection Download PDFInfo
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- CN106984409A CN106984409A CN201710255626.0A CN201710255626A CN106984409A CN 106984409 A CN106984409 A CN 106984409A CN 201710255626 A CN201710255626 A CN 201710255626A CN 106984409 A CN106984409 A CN 106984409A
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- China
- Prior art keywords
- pulverizer
- negative pressure
- aspirator
- crushed
- series connection
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- 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.)
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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
- B02C18/00—Disintegrating by knives or other cutting or tearing members which chop material into fragments
- B02C18/06—Disintegrating by knives or other cutting or tearing members which chop material into fragments with rotating knives
- B02C18/16—Details
- B02C18/22—Feed or discharge means
- B02C18/2216—Discharge 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
- B02C11/00—Other auxiliary devices or accessories specially adapted for grain mills
- B02C11/08—Cooling, heating, ventilating, conditioning with respect to temperature or water content
-
- 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
- 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
- B02C23/14—Separating or sorting of material, associated with crushing or disintegrating with more than one separator
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Disintegrating Or Milling (AREA)
Abstract
The present invention crushes aspirator for a kind of series connection of rice protein negative pressure, including pulverizer, blower fan and discharge bin, the pulverizer includes the one-level pulverizer and at least one secondary breaker connected by linker, the one-level pulverizer is provided with aggregate bin, the blower fan, discharge bin and secondary breaker pass sequentially through pipeline connection, the invention provides supporting application method on the basis of above-mentioned, i.e., complete wind in negative pressure state in whole device under blower fan and pulverizer effect and be kept completely separate with material.Beneficial effect of the present invention is：The not outer spray material of crushing process is disclosure satisfy that in industrialized production, do not block, environmental protection and improve work efficiency, while also solving reasonable adjusting air draught strength problem and in the absence of any pollution.
Description
Technical field
The present invention relates to general method or apparatus technical field physically or chemically, more particularly to rice intensive processing skill
Art field, specifically refers to a kind of rice protein negative pressure series connection and crushes aspirator and application method.
Background technology
Rice protein extracts processing at this stage turns into an industry, forms many new processing in process of production and sets
It is standby.Such as it is used for the pulverizer of lapping process after drying, general to be operated using Universal disintegrating machine in air cleaning, this kind is crushed
There are many unsurmountable defects such as in device：When granular material block feeding mouth in screen cloth after, can cause granular material from
Feeding mouth is floatd rapidly to throughout the room, and whole environment is destroyed.When using two-stage pulverizer occur one-level discharge it is not smooth when, can make
Into the motor overload of pulverizer, so that burning motor；And existing pulverizer uses single wind collecting port, cause air pressure air flow uneven
Weighing apparatus, has material to spray or screen cloth blocking, so as to influence environment not produce normally often.So urgently needing to rice protein essence
The development of honed journey new equipment, is also the primary study direction of those skilled in the art.
The content of the invention
In order to solve the above-mentioned technical problem the present invention provides a kind of rice protein negative pressure series connection and crushes aspirator and use
Method, the present invention is achieved through the following technical solutions：The device includes pulverizer, blower fan and discharge bin, the pulverizer
Including the one-level pulverizer and at least one secondary breaker connected by linker, the one-level pulverizer, which is provided with, to gather materials
Bucket, the blower fan, discharge bin and secondary breaker pass sequentially through pipeline connection.
Preferably, the aggregate bin is located at the top on one-level crusher cavity top, and along the discharging of one-level pulverizer
Mouth opening opposite direction Central Symmetry is set, and the aggregate bin bottom is provided with valve.
Preferably, the discharging opening respective chamber top of the one-level pulverizer is provided with inlet scoop, the inlet scoop
Portion is provided with valve.
Preferably, the corresponding cavity top of charging aperture and discharging opening of each secondary breaker is respectively arranged with air draught
Mouthful, valve is arranged at the inlet scoop bottom.
Preferably, the aggregate bin top is provided with storage bin.
Preferably, the feed pipe bottom interior and embedded size L2 of mouth of pipe insertion aggregate bin of storage bin scope is 15mm
~40mm.
After adopting the above technical scheme, the technical problem solved moves material transferring, 170 μm of pan feeding, powder using wind conveyer belt
40~45 μm of materials are not excessive after broken, and the valve of quantity-adjustable is housed by each inlet scoop, and are set for the eccentric, the wind
Rotation suction air makes pressure subatmospheric in system to machine at a high speed, and material is conveyed along system, realizes inventory and air quantity
Matching regulation, it is ensured that rational allocation.It is also equipped with realizing that impurity divides completely with material after screen cloth realizes filtering in pulverizer cavity wall
From the charging of the series connection pulverizer is realized by storage bin by feed pipe and aggregate bin.
Preferably, the linker is the tubular structure being obliquely installed and is 5 °~15 ° with horizontal plane angle α scopes.
Sent using this parametric scheme by wind and avoid material from being blocked in the charging aperture of secondary breaker, can solve the problem that material exists
Retained in linker.
As an improvement, the discharge bin is revolving shell structure, air outlet, the air-out are provided with the top of the revolving shell
Mouth is connected by pipeline with blower fan, and revolving shell border top is provided with charging aperture, and the charging aperture passes through pipeline and two grades
The discharging opening connection of pulverizer, the revolving shell bottom is provided with discharging opening, and the discharging opening is provided with airlock.
Process is retained using material can be made to complete infall process in discharge bin after this improvement project, while by closing wind
Device completes conveying of the material to next stage.
The application method step that aspirator is crushed in a kind of rice protein negative pressure series connection is as follows：
1）It is first turned on the valve of inlet scoop and aggregate bin connection；
2）Blower fan and each pulverizer are opened, each valve is adjusted to control intake, whole device is interior in negative under fan action
Pressure condition, storage bin starts blowing, and material is entered by aggregate bin carries out one-level crushing in the cavity of one-level pulverizer, after crushing
Material linker is sent into by wind and enter each secondary breaker complete it is multiple crush, the material after crushing passes through pipe influx
Settled and retained to discharge bin.
Compared with prior art, beneficial effect of the present invention can be learnt according to the narration to such scheme：
The present invention meets in industrialized production the not outer spray material of crushing process, does not block, environmental protection and improves work efficiency, together
When also solve reasonable adjusting air draught strength problem.Due to the method using pure physics, in the absence of any pollution, with high-efficiency environment friendly
The characteristics of.
The method of above-mentioned pure physics is calculated according to the bernoulli's equation optimization in process fluid flow：
p+ρgz+(1/2)ρv2=C
P, ρ, v are respectively pressure, density and the speed of fluid in formula；Z is plumb height；G is acceleration of gravity, and C is constant.
The relation of air quantity and pressure：P is total=P1+P2+P3+P4.
Because P is always that blower fan air-introduced machine amount is constant, P1, P2, P3, P4 are variable.
The airflow value obtained according to data and feature technology parameter, optimized parameter detailed in Example data, by physico
Work principle material is acted on by the disintegrating mechanism of pulverizer driver drives inside cavity, make solid material particle in cavity by
To extruding, tear, collision, a variety of mechanisms such as shearing, so as to reach crushing purpose.Material is completed by suction function defeated
Send.After material is crushed by upper upper level, micro mist is sucked into next stage pulverizer by suction function, enters eventually into discharging
In storehouse, complete transmission and reclaim.When material is by negative-pressure ward, the wind flow at P1, P2, P3, P4 place of collecting folk songs transmission is played to
Close important function.
Each air quantity regulation account for total blast volume preferably than for：P1 accounts for 4/10, P2 and accounts for 1/10, P3 accounting for 3/10, P4 about
Account for 2/10.
Brief description of the drawings
The present invention is further illustrated below in conjunction with the accompanying drawings.
Accompanying drawing 1 is complete layout of the present invention.
Accompanying drawing 2 is air quantity schematic vector diagram of the invention.
Accompanying drawing 3 crushes aspirator part-structure schematic diagram for the negative pressure series connection of the present invention.
Accompanying drawing 4 is aggregate bin close-up schematic view A of the invention.
Shown in figure：
1st, total air outlet P, 2, blower fan, 3, pipeline, 4, discharge bin, 4.1, air outlet, 4.2, charging aperture, 4.3, discharging opening III, 5,
Airlock, 6, secondary breaker, 6.1, secondary breaker pedestal, 6.2, secondary breaker cavity, 6.2.1, discharging opening II,
6.2.2, screen cloth II, 6.2.3, charging aperture II, 6.3, inlet scoop P3,6.3.1, P3 valve, 6.4, inlet scoop P4,6.4.1, P4 valve
Door, 6.5, the broken motor of second patent flour, 7, one-level pulverizer, 7.1, one-level pulverizer pedestal, 7.2, one-level crusher cavity, 7.2.1,
Discharging opening I, 7.3, inlet scoop P2,7.3.1, P2 valve, 7.4, aggregate bin, 7.4.1, aggregate bin screen pack, 7.4.2, screen cloth I,
7.5th, one-level crushes motor, 8, linker, 9, storage bin be changed to 9,9.1, feed pipe, 10, sack cleaner, 11, packing scale.
Embodiment
For the technical characterstic for illustrating this programme can be understood, below by embodiment, this programme is illustrated.
Referring to the drawings 1-4, the aspirator embodiment is crushed in a kind of rice protein negative pressure series connection includes pulverizer, blower fan 2
With discharge bin 4, the preferred frequency conversion centrifugal blower of blower fan 2, the pulverizer includes the one-level pulverizer connected by linker 8
7 and at least one secondary breaker 6, preferably one secondary breaker 6 herein, while can require that increase is multistage according to screening precision
Secondary breaker 6 reaches the screening of more small material, and the one-level pulverizer 7 is provided with aggregate bin 7.4, the blower fan 2, discharging
Storehouse 4 and secondary breaker 6 pass sequentially through stainless steel pipes 3 and connected.The aggregate bin 7.4 is located at the cavity top of one-level pulverizer 7
Top, and along one-level pulverizer discharging opening opening opposite direction Central Symmetry set, the bottom of aggregate bin 7.4 be provided with valve
Door.The discharging opening respective chamber top of the one-level pulverizer 7 is provided with inlet scoop, and the inlet scoop bottom is provided with valve.Institute
The corresponding cavity top of charging aperture and discharging opening for stating secondary breaker 6 is respectively arranged with inlet scoop, and the inlet scoop bottom has
Valve.
Referring to the drawings 4, the linker 8 be the tubular structure that is obliquely installed and with horizontal plane angle α scopes be 5 °~
15 °, the pipe of the section circular of linker 8, rectangle or polygonal cross-section tilts 15 degree of connection one-level crusher cavities
7.2 and secondary breaker cavity 6.2, preferred rectangular tube or profile material tube herein.
Referring to the drawings 3, each pulverizer includes the cavity of correspondence pedestal and top connection：One-level pulverizer pedestal 7.1,
One-level crusher cavity 7.2, secondary breaker pedestal 6.1 and secondary breaker cavity 6.2, the cavity of each pulverizer pass through
Linker 8 connects the corresponding 7.2.1 of discharging opening I and charging aperture II 6.2.3.
In each pedestal provided with the preferred motor driving of respective drivers such as：One-level crushes motor 7.5 and the broken electricity of second patent flour
Machine 6.5, the one-level crusher cavity 7.2 and secondary breaker cavity 6.2 are preferably diameter 750mm hollow revolution shell and outer
Portion corresponds to the inlet scoop P2 7.3 for being connected with the 7.3.1 connections of P2 valves, the aggregate bin 7.4 of P1 valves 7.4.1 connections, collection respectively
The charging aperture of hopper 7.4 is inlet scoop P1, and cavity the border discharging opening I 7.2.1, the 6.2.3 of charging aperture II that are provided with and is gone out
The 6.2.1 of material mouth II, the valve preferred manual valve or electrically-controlled valve control and use prior art to realize, the 7.2.1 of discharging opening I
It is connected by linker 8 with the 6.2.3 of charging aperture II of secondary breaker cavity 6.2, the 6.2.1 of discharging opening II and stainless steel pipes 3
Connection.
It is connected in each pedestal provided with respective drivers with each inside cavity provided with disintegrating mechanism, disintegrating mechanism uses tooth
Claw structure, using 4 groups of cutterheads, the totally 56 grinding rotors work high speed rotation completion crushing that blade is constituted can use prior art
Means are realized and not repeated herein.
It is corresponding with the 7.2.1 of discharging opening I equipped with the 7.4.2 of 200 eye mesh screen I, described two grades in the one-level crusher cavity 7.2
The crusher cavity 6.2 and 6.2.1 of discharging opening II is equipped with the 6.2.2 of 300 eye mesh screen II, each serves as the effect of impurity screening, described
The charging aperture of aggregate bin 7.4 is inlet scoop P1 and connects storage bin 9, and aggregate bin screen pack is additionally provided with the aggregate bin 7.4
7.4.1, above-mentioned each inlet scoop can also external filter prevent external dust from entering.
The top of aggregate bin 7.4 is provided with storage bin 9, and the bottom of storage bin 9 is sequentially provided with airlock 5 and feed pipe
9.1, in the bottom mouth of pipe insertion aggregate bin 7.4 of the feed pipe of the storage bin 9 9.1 and embedded size L2 scope for 15mm~
40mm, feed pipe 9.1 a diameter of L1, the L1 scope are 260mm~560mm, refer to accompanying drawing 4.
Referring to the drawings 1, the discharge bin 4 is to be provided with air outlet 4.1, institute at the top of revolving shell structure, the revolving shell
Stating air outlet 4.1 and being connected with sack cleaner 10 and play filter material makes material retain to discharge bin 4, the sack cleaner
10 are connected by stainless steel pipes 3 with blower fan 2, and revolving shell border top passes through stainless steel pipes 3 provided with charging aperture 4.2
It is connected with the 6.2.1 of discharging opening II of secondary breaker 6, the revolving shell bottom is provided with discharging opening III 4.3, the discharging opening III
4.3 are connected with airlock 5, and the preferred manual valve of airlock 5 or electrically-controlled valve are controlled, and the air-flow in discharge bin 4 is by guide vane
Guide functions and produce strong rotation, air-flow is twist downwardly into discharge bin bottom along cylinder, and the big particle of density exists
Wall is thrown toward under centrifugal action, and under gravity, is dropped through airlock 5 along barrel and flows out, the airlock 5 connects
Packing scale 11 is connected to directly to seal material progress packaging up for safekeeping.
Referring to the drawings 2, described total air outlet P 1 is total blast volume 6400m3/h, and P1, P2, P3, P4 are a point air quantity.P1 is about
Account for 4/10, P2 and account for 1/10, P3 to account for 3/10, P4 to account for 2/10, P1 and P2 being one-level crushing, P3 and P4 is that second patent flour is broken.
The application method step that aspirator is crushed in a kind of rice protein negative pressure series connection is as follows：
1）It is first turned on the valve that each inlet scoop and aggregate bin 7.4 are connected；
2）The bottom mouth of pipe of feed pipe 9.1 for adjusting the bottom of storage bin 9 is embedded in the size of aggregate bin 7.4；
3）Be separately turned on frequency conversion centrifugal blower 2 and two-stage pulverizer, each valve P1, P2, P3, P4 on adjustment crusher cavity with
Control intake enters ambient atmos, while by the blowing of airlock 5 of the bottom of storage bin 9, whole device is interior to be in negative pressure
State, the material of storage bin 9 is entered by aggregate bin 7.4 carries out one-level crushing, the thing after crushing in the cavity of one-level pulverizer 7
Material sends into linker 8 by wind and enters the completion separating twice of secondary breaker 6, and material after crushing is by pipe influx to unloading
Feed bin 4 is settled and retained.
The above is illustrated below by different embodiments.
Embodiment 1：When system enters working condition, inventory is 3m3/h.P1=2500m3/h, P2=500m3/h are adjusted,
P3=1800m3/h, P4=1600m3/h, it is respectively 48A, 50A, respectively less than rated current 60A, suction that I and II, which crushes current of electric,
Air port does not occur excessive powder situation.
Embodiment 2：When system enters working condition, inventory is 3m3/h.P1=3000m3/h, P2=500m3/h are adjusted,
P3=1500m3/h, P4=1400m3/h, it is respectively 62A, 55A that I and II, which crushes current of electric, beyond rated current 60A, motor
Overload, inlet scoop does not occur excessive powder situation.
Embodiment 3：When system enters working condition, inventory is 3m3/h.P1=1600m3/h, P2=1600m3/h are adjusted,
P3=1600m3/h, P4=1600m3/h, it is respectively 45A, 43A that I and II, which crushes current of electric, and respectively less than rated current 60A is adopted
The broken inlet scoop of second patent flour is result in impartial air quantity and powder situation of overflowing occurs, when material is by negative-pressure ward, P1, P2, P3, P4 collect folk songs
The wind flow at place plays most important effect to transmission, each air quantity regulation account for total blast volume by statistics preferably than for：P1 accounts for 4/
10, P2, which account for 1/10, P3, accounts for 3/10, P4 and accounts for 2/10, and said structure scheme is used admittedly to realize that air quantity is adjustable.
Relevant parameter detailed in Example summary sheet in above-mentioned three kinds of embodiments.
Certainly, described above is also not limited to the example above, the technical characteristic of the invention without description can by or
Realized, will not be repeated here using prior art；Above example and accompanying drawing are merely to illustrate technical scheme not
It is limitation of the present invention, preferred embodiment the present invention is described in detail for reference, the ordinary skill people of this area
Member is it should be appreciated that change, remodeling, the addition that those skilled in the art are made in the essential scope of the present invention
Or replace without departure from spirit of the invention, it should also belong to the claims of the present invention.
Claims (9)
1. aspirator, including pulverizer are crushed in a kind of rice protein negative pressure series connection, it is characterised in that：Also include blower fan（2）With
Discharge bin（4）, the pulverizer is including passing through linker（8）The one-level pulverizer of connection（7）With at least one secondary breaker
（6）, the one-level pulverizer（7）It is provided with aggregate bin（7.4）, the blower fan（2）, discharge bin（4）And secondary breaker（6）According to
It is secondary to be connected by pipeline.
2. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：It is described to gather materials
Bucket（7.4）Positioned at one-level pulverizer（7）The top on cavity top, and along the discharging opening opening opposite direction center pair of one-level pulverizer
Claim to set, the aggregate bin（7.4）Bottom is provided with valve.
3. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：The one-level
Pulverizer（7）Discharging opening respective chamber top be provided with inlet scoop, the inlet scoop bottom is provided with valve.
4. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：Described each two
Level pulverizer（6）Charging aperture and the corresponding cavity top of discharging opening be respectively arranged with inlet scoop, valve is arranged at the inlet scoop bottom
Door.
5. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：It is described to gather materials
Bucket（7.4）Top is provided with storage bin（9）.
6. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 5, it is characterised in that：The storing
Storehouse（9）Feed pipe（9.1）Bottom mouth of pipe insertion aggregate bin（7.4）Interior and embedded size L2 scope is 15mm~40mm.
7. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：The connection
Device（8）For the tubular structure being obliquely installed and be 5 °~15 ° with horizontal plane angle α scopes.
8. aspirator is crushed in a kind of rice protein negative pressure series connection according to claim 1, it is characterised in that：The discharging
Storehouse（4）For revolving shell structure, the revolving shell top is provided with air outlet, and the air outlet passes through pipeline and blower fan（2）Even
Connect, revolving shell border top is provided with charging aperture, the charging aperture passes through pipeline and secondary breaker（6）Discharging opening connect
Connect, the revolving shell bottom is provided with discharging opening, the discharging opening is provided with airlock（5）.
9. the application method of aspirator is crushed in a kind of rice protein negative pressure series connection a kind of as claimed in claim 1, its feature exists
In following steps：
1）It is first turned on inlet scoop and aggregate bin（7.4）The valve of connection；
2）Open blower fan（2）With each pulverizer, each valve is adjusted to control intake, whole device is in blower fan（2）In effect is lower
In negative pressure state, storage bin（9）Start blowing, material passes through aggregate bin（7.4）Into one-level pulverizer（7）Cavity in enter
Row one-level is crushed, and the material after crushing sends into linker by wind（8）And enter each secondary breaker（6）Complete repeatedly to crush,
Material after crushing passes through pipe influx to discharge bin（4）Settled and retained.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710255626.0A CN106984409A (en) | 2017-04-19 | 2017-04-19 | Aspirator and application method are crushed in a kind of rice protein negative pressure series connection |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710255626.0A CN106984409A (en) | 2017-04-19 | 2017-04-19 | Aspirator and application method are crushed in a kind of rice protein negative pressure series connection |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106984409A true CN106984409A (en) | 2017-07-28 |
Family
ID=59415990
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710255626.0A Pending CN106984409A (en) | 2017-04-19 | 2017-04-19 | Aspirator and application method are crushed in a kind of rice protein negative pressure series connection |
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| Country | Link |
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| CN (1) | CN106984409A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109303247A (en) * | 2018-12-07 | 2019-02-05 | 湖南袁禾农业科技有限公司 | Wheat bran processing method and wheat bran processed food |
| CN109847920A (en) * | 2019-02-18 | 2019-06-07 | 长沙开元仪器有限公司 | A kind of strength fuel pulverizing plant |
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| WO1985002810A1 (en) * | 1983-12-21 | 1985-07-04 | Heinrich Nagel Ag | Machine for the suction and comminution of a material transported in a gas medium |
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| CN203598898U (en) * | 2013-12-15 | 2014-05-21 | 白银普瑞特化工有限公司 | Material crushing system |
| CN203610191U (en) * | 2013-09-05 | 2014-05-28 | 福建南方路面机械有限公司 | Impact-type crushing machine capable of recycling dust grade by grade |
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| CN204182476U (en) * | 2014-09-29 | 2015-03-04 | 天门市金江粮机有限公司 | The radial air compensation device of horizontal non-screen smashing-classifying integrated machine pulverizing chamber |
| CN205236121U (en) * | 2015-12-11 | 2016-05-18 | 济宁学院 | Fluidized bed jet milling device |
| CN205903939U (en) * | 2016-06-20 | 2017-01-25 | 江西尚绿科技有限公司 | Screening system is smashed to negative pressure formula active carbon |
| CN206661380U (en) * | 2017-04-19 | 2017-11-24 | 信阳山信生物食品科技有限公司 | A kind of rice protein negative pressure series connection crushes aspirator |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1985002810A1 (en) * | 1983-12-21 | 1985-07-04 | Heinrich Nagel Ag | Machine for the suction and comminution of a material transported in a gas medium |
| CN102764686A (en) * | 2012-07-27 | 2012-11-07 | 福建南方路面机械有限公司 | Impact crusher capable of adjusting aggregate fineness modulus |
| CN203610191U (en) * | 2013-09-05 | 2014-05-28 | 福建南方路面机械有限公司 | Impact-type crushing machine capable of recycling dust grade by grade |
| CN203598898U (en) * | 2013-12-15 | 2014-05-21 | 白银普瑞特化工有限公司 | Material crushing system |
| CN103894278A (en) * | 2014-03-28 | 2014-07-02 | 贵州茅台酒股份有限公司 | Yeast crushing equipment and method for preparing yeast powder |
| CN204182476U (en) * | 2014-09-29 | 2015-03-04 | 天门市金江粮机有限公司 | The radial air compensation device of horizontal non-screen smashing-classifying integrated machine pulverizing chamber |
| CN205236121U (en) * | 2015-12-11 | 2016-05-18 | 济宁学院 | Fluidized bed jet milling device |
| CN205903939U (en) * | 2016-06-20 | 2017-01-25 | 江西尚绿科技有限公司 | Screening system is smashed to negative pressure formula active carbon |
| CN206661380U (en) * | 2017-04-19 | 2017-11-24 | 信阳山信生物食品科技有限公司 | A kind of rice protein negative pressure series connection crushes aspirator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109303247A (en) * | 2018-12-07 | 2019-02-05 | 湖南袁禾农业科技有限公司 | Wheat bran processing method and wheat bran processed food |
| CN109847920A (en) * | 2019-02-18 | 2019-06-07 | 长沙开元仪器有限公司 | A kind of strength fuel pulverizing plant |
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