CN206661380U - A kind of rice protein negative pressure series connection crushes aspirator - Google Patents
A kind of rice protein negative pressure series connection crushes aspirator Download PDFInfo
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- CN206661380U CN206661380U CN201720410069.0U CN201720410069U CN206661380U CN 206661380 U CN206661380 U CN 206661380U CN 201720410069 U CN201720410069 U CN 201720410069U CN 206661380 U CN206661380 U CN 206661380U
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- Prior art keywords
- aspirator
- crushes
- negative pressure
- pulverizer
- series connection
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Abstract
The utility model is that a kind of series connection of rice protein negative pressure crushes aspirator, and a kind of rice protein negative pressure series connection crushes aspirator, including pulverizer, blower fan（2）And 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）Pass sequentially through pipeline connection.The utility model beneficial effect 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 solves reasonable adjusting air draught strength problem and any pollution is not present.
Description
Technical field
The utility model is related to the method or apparatus technical field of in general physically or chemically, more particularly to rice it is profound plus
Work technical field, in particular to a kind of series connection of rice protein negative pressure crush aspirator.
Background technology
The processing of rice protein extraction 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, is typically crushed using Universal disintegrating machine in the interior operation of air cleaning, this kind
The defects of many unconquerable be present 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, there are material ejection or screen cloth to block often, can not normally be produced so as to influence environment.So urgently need to rice protein essence
The development of honed journey new equipment, and the focus on research direction of those skilled in the art.
Utility model content
In order to solve the above-mentioned technical problem the utility model provides a kind of rice protein negative pressure series connection and crushes aspirator, this
Utility model is achieved by the following technical solution：The device includes pulverizer, blower fan and discharge bin, and the pulverizer includes
The one-level pulverizer and at least one secondary breaker, the one-level pulverizer connected by linker is provided with aggregate bin, institute
State blower fan, discharge bin passes sequentially through pipeline with secondary breaker and connected.
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 center symmetric setting, 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, under the inlet scoop
Portion is provided with valve.
Preferably, cavity top corresponding to the 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 interior and embedded size L2 of feed pipe bottom nozzle 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 conveys along system, realizes inventory and air quantity
Matching regulation, ensure 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.
Being sent using this parametric scheme by wind avoids 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 level
The discharging opening connection of pulverizer, the revolving shell bottom are 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.
Compared with prior art, the utility model beneficial effect can be learnt according to the narration to such scheme：
The utility model meets in industrialized production the not outer spray material of crushing process, does not block, environmental protection and improves work
Make efficiency, while also solve reasonable adjusting air draught strength problem.Due to the method using pure physics, in the absence of any pollution, tool
There is the characteristics of high-efficiency environment friendly.
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 normal
Amount.
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, a variety of mechanisms such as collision, shearing, so as to reach crushing purpose.It is defeated that material is completed by suction function
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, transmission and recovery are completed.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 utility model is further described below in conjunction with the accompanying drawings.
Accompanying drawing 1 is the utility model complete layout.
Accompanying drawing 2 is air quantity schematic vector diagram of the present utility model.
Accompanying drawing 3 is that negative pressure of the present utility model series connection crushes aspirator part-structure schematic diagram.
Accompanying drawing 4 is aggregate bin close-up schematic view A of the present utility model.
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 valves, 6.5, two level crush motor, 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, 7.5, one-level crush motor, 8, linker, 9, storage bin be changed to 9,9.1, feed pipe, 10, sack cleaner, 11, bag
Fill 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, a kind of rice protein negative pressure series connection, which crushes the aspirator embodiment, 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, a preferably secondary breaker 6, while can require that increase is multistage according to screening precision herein
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 be provided with valve along the discharging opening opening opposite direction center symmetric setting of one-level pulverizer, the bottom of aggregate bin 7.4
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
State cavity top corresponding to the charging aperture and discharging opening of secondary breaker 6 and be respectively arranged with inlet scoop, 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 corresponding pedestal and the cavity of 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 the discharging opening I and 6.2.3 of charging aperture II.
The preferred motor driving of respective drivers is provided with each pedestal such as：One-level crushes motor 7.5 and two level crushes electricity
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, totally 56 the grinding rotor work high speed rotation completion crushing of blade composition prior art can be used using 4 groups of cutterheads
Means are realized and not repeated herein.
It is corresponding with the 7.2.1 of discharging opening I in the one-level crusher cavity 7.2 that the 7.4.2 of 200 eye mesh screen I, the two level are housed
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 nozzle of feed pipe 9.1 of the storage bin 9 insertion aggregate bin 7.4 and embedded size L2 scope for 15mm~
40mm, 9.1 a diameter of L1 of feed pipe, the scope of the L1 is 260mm~560mm, refers to accompanying drawing 4.
Referring to the drawings 1, the discharge bin 4 is revolving shell structure, and air outlet 4.1, institute are provided with the top of 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 control, 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
It is connected to packing scale 11 material is directly subjected to packaging and seals 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 to divide 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 that one-level crushes, P3 and P4 is two level crushing.
The above is illustrated below by different embodiments.
Embodiment 1：When system enters working condition, inventory 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 that I and II, which crushes current of electric, is inhaled
Air port does not occur excessive powder situation.
Embodiment 2：When system enters working condition, inventory 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 3m3/h.P1=1600m3/h, P2=1600m3/h are adjusted,
P3=1600m3/h, P4=1600m3/h, it is respectively 45A, 43A, respectively less than rated current 60A that I and II, which crushes current of electric, is adopted
Two level is result in impartial air quantity and crushes the excessive powder situation of inlet scoop appearance, and 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 count 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, and technical characteristic of the utility model without description can lead to
Cross or realized using prior art, be will not be repeated here；Above example and accompanying drawing are merely to illustrate technology of the present utility model
It is to limitation of the present utility model that scheme, which is not, and the utility model is described in detail with reference to preferred embodiment, this
Field it is to be appreciated by one skilled in the art that those skilled in the art institute in essential scope of the present utility model
For the variations, modifications, additions or substitutions made without departure from objective of the present utility model, should also belong to right of the present utility model will
Seek protection domain.
Claims (8)
1. a kind of rice protein negative pressure series connection crushes aspirator, including pulverizer, 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. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, 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. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, 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. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, it is characterised in that：Described each two
Level pulverizer（6）Charging aperture and discharging opening corresponding to cavity top be respectively arranged with inlet scoop, valve is arranged at the inlet scoop bottom
Door.
5. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, it is characterised in that：It is described to gather materials
Bucket（7.4）Top is provided with storage bin（9）.
6. a kind of rice protein negative pressure series connection according to claim 5 crushes aspirator, it is characterised in that：The storing
Storehouse（9）Feed pipe（9.1）Bottom nozzle is embedded in aggregate bin（7.4）Interior and embedded size L2 scope is 15mm~40mm.
7. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, it is characterised in that：The connection
Device（8）For the tubular structure being obliquely installed and it is 5 °~15 ° with horizontal plane angle α scopes.
8. a kind of rice protein negative pressure series connection according to claim 1 crushes aspirator, 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, and the charging aperture passes through pipeline and secondary breaker（6）Discharging opening connect
Connect, the revolving shell bottom is provided with discharging opening, and the discharging opening is provided with airlock（5）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720410069.0U CN206661380U (en) | 2017-04-19 | 2017-04-19 | A kind of rice protein negative pressure series connection crushes aspirator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720410069.0U CN206661380U (en) | 2017-04-19 | 2017-04-19 | A kind of rice protein negative pressure series connection crushes aspirator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206661380U true CN206661380U (en) | 2017-11-24 |
Family
ID=60374956
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720410069.0U Expired - Fee Related CN206661380U (en) | 2017-04-19 | 2017-04-19 | A kind of rice protein negative pressure series connection crushes aspirator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206661380U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106984409A (en) * | 2017-04-19 | 2017-07-28 | 信阳山信生物食品科技有限公司 | Aspirator and application method are crushed in a kind of rice protein negative pressure series connection |
| CN107966013A (en) * | 2017-12-25 | 2018-04-27 | 佛山市万善环保科技有限公司 | A kind of air-supply arrangement of ceramics drying equipment |
-
2017
- 2017-04-19 CN CN201720410069.0U patent/CN206661380U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106984409A (en) * | 2017-04-19 | 2017-07-28 | 信阳山信生物食品科技有限公司 | Aspirator and application method are crushed in a kind of rice protein negative pressure series connection |
| CN107966013A (en) * | 2017-12-25 | 2018-04-27 | 佛山市万善环保科技有限公司 | A kind of air-supply arrangement of ceramics drying equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171124 Termination date: 20200419 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |