CN206643006U - Gas method solid particle separator - Google Patents
Gas method solid particle separator Download PDFInfo
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- CN206643006U CN206643006U CN201720149971.1U CN201720149971U CN206643006U CN 206643006 U CN206643006 U CN 206643006U CN 201720149971 U CN201720149971 U CN 201720149971U CN 206643006 U CN206643006 U CN 206643006U
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- rotary body
- solid particle
- particle
- particle separator
- gas method
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Abstract
The utility model belongs to classification of solid particles technical field, it is related to a kind of gas method solid particle separator, including particle process equipment rotary body, it is characterized in that the material upstream end in rotary body is provided with gas feed, some lifting flights are set in the cylinder of rotary body, and the port of export of rotary body is provided with discharge component.The utility model is completed because large or fine granule separates in equipment, it is not necessary to screening plant；There is no screen cloth, avoid the blocking of screen cloth mesh especially dusting cover mesh, be suitable for the separation of fine particle；There is no screen cloth to paste sieve problem, being adapted to the particle of certain wetness and surface has necessarily viscous feed separation, better adaptability；Do not increase power-equipment, simple flow and reduction equipment, so as to reduce investment outlay and not take up an area, save the energy, while it also avoid the noise and airborne dust of screening plant, achieve many things at one stroke.
Description
Technical field
The utility model belongs to solid particle（Hereinafter referred to as particle）Classification（Size particles separate）Technical field, it is applied to
Industry, the field for separating solid particle are needed, such as（It is not limited only to this）：Cement, steel, fertilizer, grain, feed, building materials, energy
Source etc..
Background technology
The utility model is solid particle（Hereinafter referred to as particle）Classification（Size particles separate）Technology, be applicable to by
The industry of solid particle separation, field, such as（It is not limited only to this）：Cement, steel, fertilizer, feed, building materials, energy etc..
In above-mentioned field, solid particle is given by particle size during generally requiring involved physics, chemistry
Separation, traditional method are carried out by the way of screening or special external seperator, and shortcoming is：Long flow path, investment are big, energy consumption
Height, process are relative complex.And it is larger by pellet moisture levels, viscosity influence, cause use range and effect to be restricted.
By taking traditional fertiliser granulates production as an example：In production different size of particle the comminutor of revolving body, drying machine,
For cooler to outlet end motion, it is necessary to which the solid particle of classification by screening, it is necessary to be put into next procedure, process is a series of
Subsequent handling obtains grain products.
Refer to the attached drawing 1, it is necessary to the particle of processing enters from particle process equipment one end, gas with holding addition, in particle plus
Processed needed for being carried out in construction equipment rotary body 1, such as：Be granulated, dry, cooling down, drying etc., the particle of the mixing particle diameter after processing
Into mixing particles discharge bucket 2, screening machine 3 is entered back into, is separated large or fine granule by the screen cloth of screening machine, fine grained enters
Enter fine grained hopper 4 as material return system is returned, re-worked from the beginning together with raw material, coarse granule enters following process
The tail gas that process comes out up to the product to need, particle process equipment, into exhaust treatment system, until qualified discharge.
The shortcomings that technology：1st, the particle of the mixing particle diameter without classification is set from revolutions such as comminutor, drying machine, coolers
After being come out in standby, it is necessary to increase external device, increase is invested, increase energy consumption, increase is taken up an area, increase dust when by sieving
Effusion, increase noise；Because mesh size is tiny when the 2nd, due to screening fine powder, cause fine-powder bed net efficiency to decline, cause to life
The influence of production；3rd, when sieving surface moisture or there are the granule materials of viscosity, screen cloth is easily pasted, is generally required granule materials
Pre-processed, for example, cool, surface face powder etc., adds additional energy consumption and process.
The content of the invention
The purpose of this utility model is to be directed to drawbacks described above, and a kind of gas method solid particle separator proposed, i.e.,
Increase and change the purpose that partial component can reaches separation and classification among process device.
The utility model mainly solve it is above-mentioned by need separate mixing particle diameter particle surface dry, have certain humidity,
There are the screening problem of certain viscosity, such as hot screening problems faced：Necessary component will be set in turn-around machine, utilize gas
With the effect of material curtain, the fine grained separation of most of off grade size is directly completed in the said equipment, it is directly returned to life
Production system, to solve problem present in above-mentioned conventional method.
Main technical schemes of the present utility model：Gas method solid particle separator, including the rotation of particle process equipment
Body, it is characterized in that the material upstream end in rotary body is provided with gas feed, some lifting flights, rotation are set in the cylinder of rotary body
The port of export of swivel is provided with discharge component.
Preferably, the utility model a rotating body is additionally provided with inner barrel, and inner barrel is provided with inner barrel lifting flight.
Further, the utility model can be provided with cone of the material by function, circle in the front end of inner barrel
Baffle plate or several piece circle baffle plate or several piece spiral plate, material set some tiltedly flight or spiral flights by locating.
Preferably, discharge component of the present utility model can be received from and the hopper of dropping material, including coarse granule go out
Hopper and fine grained discharge bucket.
Further, discharge component of the present utility model can also carry lifting function to change discharging direction and position
Component, the component is made up of the cavity of several quantity, is fed by side or inner side top surface, passes through and is discharged on the outside of rotary body.
The utility model kicks up granule materials using the rotation and flight of apparatus for rotating in revolution, is existed according to large or fine granule
Move distance is different in gas, and granule materials are acted on by the kinetic energy of gas, so as to realize that large or fine granule is big in apparatus for rotating
It is partially separated, so as to meet to produce needs.
The beneficial effects of the utility model：
1st, because large or fine granule separation is completed in equipment, it is not necessary to screening plant, do not increase power-equipment, simple flow
With reduction equipment, so as to reduce investment outlay and not take up an area, the energy is saved, while it also avoid the noise and airborne dust of screening plant,
Achieve many things at one stroke.
2nd, the method separated using gas, it is ensured that the primary characteristic of material is constant, than if maintaining temperature-resistant.
3rd, using the method separated in gas apparatus, without screen cloth, the blocking of screen cloth mesh especially dusting cover mesh is avoided,
It is suitable for the separation of fine particle.
4th, using the method separated in gas apparatus, sieve problem is pasted without screen cloth, is adapted to the particle of certain wetness
There are necessarily viscous feed separation, better adaptability with surface.
Brief description of the drawings
Fig. 1 is the process units schematic diagram of existing fertiliser granulates.
Fig. 2 is the schematic diagram of the separator of the utility model embodiment 1.
Fig. 3 is the schematic diagram of the separator of the utility model embodiment 2.
Fig. 4 is the A-A of inner barrel lifting flight in Fig. 3 to structural representation.
Fig. 5 is the B-B direction structural representation of rotary body lifting flight in Fig. 2, Fig. 3.
Fig. 6 is the K of discharge component in Fig. 2, Fig. 3 to structural representation.
In figure, 1- rotary bodies；2- mixing particles discharge buckets；3- screening machines；4- discharge buckets；5- cones or circle gear
Plate；6- inner barrels；7- discharge components；8- coarse granule discharge buckets；9- fine grained discharge buckets；10- inner barrel lifting flights；11- revolves
Turn lifting flight；The oblique flights of 12- or spiral flight.
Embodiment
The utility model is described in detail in reference to embodiment and accompanying drawing.
Embodiment 1
Gas method solid particle separator refer to the attached drawing 2, mainly include particle process equipment rotary body 1, it improves it
Place is to be provided with gas feed in the material upstream end of rotary body 1, and some rotary body lifting flights 11 are set in the cylinder of rotary body 1
（Refer to the attached drawing 5）, the port of export of rotary body 1 is provided with discharge component 7, the component be with lifting function with change discharging direction and
The component of position（Refer to the attached drawing 6）, component is made up of the cavity of several quantity, is fed by side or inner side top surface, passes through rotation
Swivel outside discharges.
The discharge component 7 of the present embodiment also include can received from upper the hopper of dropping material, i.e. coarse granule discharge bucket 8 and thin
Particle discharge bucket 9.
Embodiment 2
Gas method solid particle separator refer to the attached drawing 3, mainly include particle process equipment rotary body 1, it improves it
Place is to be provided with gas feed in the material upstream end of rotary body 1, and some rotary body lifting flights 11 are set in the cylinder of rotary body 1
（Refer to the attached drawing 5）, the port of export of rotary body is provided with discharge component 7.
In the present embodiment, inner barrel 6 is additionally provided with rotary body 1, inner barrel 6 is provided with inner barrel lifting flight 10（With reference to
Accompanying drawing 4）, cone or circle baffle plate 5 of the material by function are provided with the front end of inner barrel 6.
In the present embodiment, discharge component 7 is to carry lifting function to change the component in discharging direction and position（Refer to the attached drawing
6）, component is made up of the cavity of several quantity, fed by side or inner side top surface, by being discharged on the outside of rotary body；Discharging group
Part 7 also include can received from upper the hopper of dropping material, i.e. coarse granule discharge bucket 8 and fine grained discharge bucket 9.
It should be noted that above-described embodiment is only technical solutions of the utility model separate embodiment, the utility model
Innovative point be：Granule materials are kicked up in revolution using the rotation and lifting flight of apparatus for rotating, are existed according to large or fine granule
Move distance is different in gas, and granule materials are acted on by the kinetic energy of gas, so as to realize large or fine granule in apparatus for rotating
Most separation, so as to meet to produce needs.
Therefore, including but not limited to following combination, all in the scope of protection of the utility model：
Cone or circle baffle plate can also be with the several piece circle baffle plate or several piece spiral by material function.
Inner barrel, length are unlimited.
Oblique flight or spiral flight, can set to be not provided with.
Under inner barrel and miscellaneous part, the mainly particle of adaptation different specific weight and different air quantity in various apparatus for rotating
Particle separates, and therefore, even if without this part, can also reach the separation target of certain demand.
With lifting function with change discharging direction and position discharge component be according under factory's different situations because of ground
Suiting measures to different conditions design part, whether there is this part.
Claims (5)
1. a kind of gas method solid particle separator, including particle process equipment rotary body, it is characterized in that in the thing of rotary body
Material upstream end is provided with gas feed, sets some lifting flights in the cylinder of rotary body, the port of export of rotary body is provided with discharging group
Part.
2. gas method solid particle separator according to claim 1, it is characterized in that a rotating body is additionally provided with inner barrel,
Inner barrel is provided with inner barrel lifting flight.
3. gas method solid particle separator according to claim 1 or 2, it is characterized in that being set in the front end of inner barrel
With material by the cone of function, circle baffle plate or several piece circle baffle plate or several piece spiral plate, if material is set by locating
Do oblique flight or spiral flight.
4. gas method solid particle separator according to claim 1, it is characterised in that the discharge component is to receive
The hopper of blanking from top to bottom, including coarse granule discharge bucket and fine grained discharge bucket.
5. the gas method solid particle separator according to claim 1 or 4, its feature is to carry in the discharge component
Lifting function is to change the component in discharging direction and position, and the component is made up of the cavity of several quantity, by side or inner side
Top surface is fed, by being discharged on the outside of rotary body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720149971.1U CN206643006U (en) | 2017-02-20 | 2017-02-20 | Gas method solid particle separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720149971.1U CN206643006U (en) | 2017-02-20 | 2017-02-20 | Gas method solid particle separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206643006U true CN206643006U (en) | 2017-11-17 |
Family
ID=60280268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720149971.1U Expired - Fee Related CN206643006U (en) | 2017-02-20 | 2017-02-20 | Gas method solid particle separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206643006U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114322489A (en) * | 2021-12-20 | 2022-04-12 | 湖南中医药大学 | Traditional Chinese medicine drying device capable of realizing weight separation |
-
2017
- 2017-02-20 CN CN201720149971.1U patent/CN206643006U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114322489A (en) * | 2021-12-20 | 2022-04-12 | 湖南中医药大学 | Traditional Chinese medicine drying device capable of realizing weight separation |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171117 Termination date: 20200220 |