CN212596280U - Dust particle separating device - Google Patents
Dust particle separating device Download PDFInfo
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- CN212596280U CN212596280U CN202021090486.XU CN202021090486U CN212596280U CN 212596280 U CN212596280 U CN 212596280U CN 202021090486 U CN202021090486 U CN 202021090486U CN 212596280 U CN212596280 U CN 212596280U
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- container
- dust
- boiling container
- air
- boiling
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- 239000000428 dust Substances 0.000 title claims abstract description 58
- 239000002245 particle Substances 0.000 title claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 93
- 238000009835 boiling Methods 0.000 claims abstract description 80
- 230000007246 mechanism Effects 0.000 claims abstract description 35
- 238000012546 transfer Methods 0.000 claims abstract description 35
- 239000013590 bulk material Substances 0.000 claims description 21
- 238000003756 stirring Methods 0.000 claims description 13
- 230000009471 action Effects 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 230000001681 protective effect Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 8
- 230000008901 benefit Effects 0.000 abstract description 2
- 230000008676 import Effects 0.000 abstract description 2
- 238000012216 screening Methods 0.000 abstract 1
- 239000004576 sand Substances 0.000 description 17
- 239000004575 stone Substances 0.000 description 10
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009440 infrastructure construction Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
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Abstract
The utility model discloses a dirt particle separator relates to material screening equipment field, include the support frame and all be fixed in the boiling container of support frame, dust transfer container, centrifugal force take place mechanism and first atmospheric pressure and take place the mechanism, the upper portion of boiling container with dust transfer container intercommunication, the material import has been seted up to the upper end of boiling container, the material export has been seted up to the lower part of boiling container, the material in the boiling container is in layering about taking place under the effect of centrifugal force take place mechanism, the dust that is located the upper strata is in follow under the effect of first atmospheric pressure takes place the mechanism the boiling container gets into the dust transfer container, the material warp that is located the lower floor the material export falls out, the material export has been seted up to the lower part of dust container, possesses the effectual advantage of dirt particle separation.
Description
Technical Field
The utility model relates to a material separation equipment field especially relates to a dirt particle separator.
Background
Along with the deepening of national infrastructure construction, the demand of sand is huge, and along with the enhancement of environmental awareness, people have realized that sand and stone are non-renewable natural resources, and can not take sand to rivers without limit, and along with the rapid development of concrete technology, the technical requirements of modern concrete on sand and stone are higher and higher, and the natural sand and stone capable of meeting the requirements are fewer and fewer, so machine-made sand and stone become the main source of sand for construction in China. In the mode of machine-made sand, dry-method sand making can reasonably utilize stone powder generated in the production process because the dry-method sand making is not limited by water sources and environment, so that water resources and mineral resources are saved to a certain extent, and no sewage and sludge are discharged, so that the dry-method sand making is more environment-friendly than a wet-method production line, and therefore the dry-method sand making is a mainstream sand making mode at present, but the separation device adopted in the existing sand-stone aiming at the dust particle separation process has the problems of low separation efficiency and poor separation effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome not enough among the prior art, provide a dirt particle separator, possess the effectual advantage of dirt particle separation.
In order to achieve the above purpose, the utility model adopts the following technical scheme: the utility model provides a dirt particle separator, includes the support frame and all is fixed in boiling container, dust transfer container, centrifugal force generation mechanism and the first atmospheric pressure generation mechanism of support frame, wherein:
the upper part of the boiling container is communicated with the dust transfer container, the upper end of the boiling container is provided with a material inlet, the lower part of the boiling container is provided with a material outlet, materials in the boiling container are layered up and down under the action of the centrifugal force generating mechanism, dust on the upper layer enters the dust transfer container from the boiling container under the action of the first air pressure generating mechanism, the materials on the lower layer fall out through the material outlet, and the lower part of the boiling container is provided with a material outlet.
In order to further optimize the utility model discloses, can prefer following technical scheme for use:
preferably, dust transfer container is at least two, dust transfer container evenly arranges in the horizontal plane week side of boiling container, dust transfer container is the whirlwind loading head, guarantees through the dust transfer container of a plurality of equipartitions that the interior dust of boiling container gets into each dust transfer container fast in, has guaranteed that the treatment effeciency has reduced equipment burden simultaneously.
Preferably, the centrifugal force generating mechanism comprises a power unit, a stirring shaft and a bulk material tray, wherein: the power unit is fixed above the boiling container; the stirring shaft is rotatably arranged at the central position in the boiling container under the driving of the power unit, and the stirring shaft is vertically arranged;
the bulk material discs are coaxially arranged on the stirring shaft, the bulk material discs are conical, and the included angle between a bus of the bulk material discs and the horizontal plane is 5-10 degrees; the centrifugal force generating mechanism ensures that the materials falling into the boiling container are uniformly distributed and dispersed, so that the separation effect is improved.
Preferably, a material distributing assembly is installed in the boiling container and located below the material inlet, the material distributing assembly comprises a plurality of triangular pyramid-shaped material distributing units, the material distributing units are parallel to each other, two ends of each material distributing unit are flush, the material distributing units are arranged in an equilateral triangle shape, upper vertex angles of all triangular pyramids are vertically upward, and a material can pass through a distributing channel is kept between any three adjacent material distributing units.
Preferably, a dirt particle separator still includes check fender ring, check fender ring fix in boiling vessel's inner wall, check fender ring's axis with boiling vessel's central line coincidence, check fender ring is located the bulk cargo dish with between the filter screen, the internal surface of check fender ring to the distance of boiling vessel's axis is not more than the edge of bulk cargo dish reaches the distance of boiling vessel's axis.
Preferably, a filter screen is arranged at the communication position of the boiling container and the dust transfer container.
Preferably, the first air pressure generating mechanism comprises an air inlet and a first air extractor, wherein:
the air inlet of the first air pressure generating mechanism is arranged at the lower part of the boiling container;
and the air inlet end of the first air exhaust fan is communicated with the top of the boiling container and the top of the dust transfer container, and the air outlet end of the first air exhaust fan is communicated to the outside of the boiling container and the dust transfer container.
Preferably, a dirt particle separator still includes the kuppe, the kuppe is the taper, the main aspects of kuppe is coaxial to be fixed in the boiling container and lie in the below of bulk cargo dish, the air inlet extends to in the kuppe, guarantees the operating stability of atmospheric pressure generation mechanism through the kuppe.
Preferably, the number of the air inlets of the first air pressure generating mechanism is at least two, and all the air inlets are uniformly arranged on the peripheral side of the material outlet of the boiling container, so that the smoothness of the air inlet process of the equipment is ensured.
The beneficial effects of the utility model reside in that: the utility model is provided with a plurality of dust transfer containers, which improves the dust particle separation effect, and further, the utility model is also provided with a centrifugal force generating mechanism, the centrifugal force generating mechanism comprises a power unit, a stirring shaft and a bulk material disc, which ensures the even flow of the mixed material in the stone and sand separation process, ensures the uniformity of the stone and sand distribution when whirlwind is formed, and further improves the stone and sand separation rate; further, install in the boiling container and divide the material subassembly, divide the material subassembly to be located the below of material import, divide the material subassembly to include a plurality of triangular pyramid's branch material unit, divide the material unit to be parallel to each other and both ends all flush, divide the material unit to be equilateral triangle and arrange, preliminary dispersion when guaranteeing the material to enter, prevent that the material from piling up.
Drawings
FIG. 1 is a schematic view of the overall structure of a dust particle separating apparatus;
FIG. 2 is a perspective view of the boiling vessel;
FIG. 3 is a schematic diagram of the internal structure of the boiling vessel;
fig. 4 is an enlarged view of the structure at a.
The device comprises a raw material crushing bin, a first belt conveyor, a separating device, a cyclone collector IV, a second belt conveyor, a separating container 6, a cyclone collector II, a second air exhaust fan 8, a cyclone collector III, a bag-type dust collector 10, a first air exhaust fan 11, a chimney 12 and a protective cover 13, wherein the raw material crushing bin 2 is connected with the first belt conveyor;
201-frame, 202-power unit, 203-conveyor belt, 204-guide roller assembly, 205-horizontal guide roller, 206-inclined guide roller, 207-limit guide roller, 208-tensioning mechanism, 209-tensioning plate, 210-tensioning nut, 211-tensioning bolt;
301-support frame, 302-boiling container, 303-dust transfer container, 304-material inlet, 305-material outlet, 306-air inlet, 307-conical end, 308-centrifugal force generating mechanism, 309-power unit, 310-stirring shaft, 311-material dispersing disk, 312-first air extractor, 313-air deflector, 314-material separating component, 315-material separating unit, 316-material separating channel, 317-grid baffle ring and 318-filter screen;
601-material inlet, 602-first air outlet, 603-second air outlet, 604-first feed opening, 605-second feed opening, 606-third feed opening, 607-first filter screen, 608-second filter screen, 609-first partition, 610-second partition, 611-air inlet, 612-guide plate and 613-support leg.
Detailed Description
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Example 1:
as shown in fig. 1 to 4, a dust particle separating apparatus includes a separating apparatus 3, the separating apparatus 3 includes a supporting frame 301, a boiling container 302, a dust transfer container 303, a centrifugal force generating mechanism and a first air pressure generating mechanism, which are all fixed on the supporting frame, wherein: the upper part of the boiling container is communicated with a dust transfer container, the upper end of the boiling container is provided with a material inlet 304, the number of the dust transfer containers is at least two, the dust transfer containers are uniformly arranged on the peripheral side of the boiling container in the horizontal plane, the dust transfer containers are cyclone collectors, and a plurality of uniformly distributed dust transfer containers ensure that dust in the boiling container quickly enters each dust transfer container, so that the processing efficiency is ensured, and the equipment burden is reduced; the material outlet has been seted up to the lower part of boiling container 302, and the layering takes place from top to bottom under the effect of centrifugal force generation mechanism in the material in the boiling container 302, and the dust that is located the upper strata gets into the dust transfer container from the boiling container under the effect of first atmospheric pressure generation mechanism, and the material that is located the lower floor falls out through material outlet 305, and material outlet 305 has been seted up to the lower part of boiling container.
Centrifugal force generating mechanism 308 includes power unit, (mixing) shaft and bulk material dish, wherein: the power unit is fixed above the boiling container, and the power unit 309 selects a driving motor; the stirring shaft is rotatably arranged at the central position in the boiling container under the driving of the power unit, and the stirring shaft 310 is vertically arranged; the bulk material tray 311 is coaxially arranged on the stirring shaft, a fixing sleeve is arranged in the middle of the bulk material tray 311, key grooves are formed in the fixing sleeve and the rotating rod in corresponding positions, keys are arranged in the key grooves, and the bulk material tray is fixed through the keys, so that the stability of the bulk material tray in the rotating process is ensured; meanwhile, the material dispersing plate 311 is different from the existing material dispersing plate which is flat, and is conical, and the included angle between the bus of the material dispersing plate and the horizontal plane is 5-10 degrees; the centrifugal force generating mechanism ensures that the materials falling into the boiling container are uniformly distributed and dispersed, so that the separation effect is improved, the driving motor drives the driving shaft to rotate, the driving shaft drives the bulk material disc to rotate, the materials falling from the material inlet fall onto the bulk material disc, and the bulk material disc is driven by the driving motor to rotate so as to scatter and separate the stone sand on the upper surface of the bulk material disc to the periphery; the bulk cargo dish through little inclination can guarantee the abundant even diffusion of material, and first atmospheric pressure takes place the mechanism and includes air inlet 306 and first air extractor 11, wherein: the air inlet of the first air pressure generating mechanism is arranged at the lower part of the boiling container; the inlet end of first air exhaust fan passes through the pipeline and the boiling container, all communicates in dust transfer container top, and the end of giving vent to anger of first air exhaust fan communicates outside boiling container, dust transfer container, still has connected gradually whirlwind loading head four 4 between first air exhaust fan 11 and the boiling container, and whirlwind loading head three 9, sack cleaner 10, further, in order to guarantee the feature of environmental protection of whole equipment, the end of giving vent to anger of first air exhaust fan 11 still is connected with chimney and protection casing, wherein: the chimney 12 is vertically arranged, and the air outlet end of the first air exhaust fan is arranged at the lower end of the chimney 12; the shield 13 is fixed to the upper end of the chimney with a space between the shield and the chimney.
Furthermore, a dust particle separator still includes kuppe 313, and the kuppe is the taper, and the main aspects of kuppe 313 is coaxial to be fixed in boiling container and to be located the below of bulk cargo dish, and air inlet 306 extends to in the kuppe, guarantees the operating stability of atmospheric pressure generation mechanism through the kuppe, and the quantity of the air inlet of first atmospheric pressure generation mechanism is at least two, and all air inlets evenly arrange in the week side of the material export of boiling container, guarantee the smoothness nature of equipment air inlet process. A material distributing assembly is arranged in the boiling container, the material distributing assembly 315 is positioned below the material inlet, the material distributing assembly comprises a plurality of triangular pyramid-shaped material distributing units, the material distributing units are parallel to each other, two ends of the material distributing units are flush, the material distributing units 315 are arranged in an equilateral triangle, the upper vertex angles of all triangular pyramids are vertically upward, a material passing flow distributing channel 316 is kept between any three adjacent material distributing units, further, the number of layers of material distributing cone bodies can be adjusted according to the size and use of equipment, and the number of the material distributing units is sequentially increased from top to bottom; the material is guided through the shunting cone in the shunting assembly, so that the smooth gliding and downward sliding of the material are ensured to be stable, and the phenomenon of material accumulation is prevented. A filter screen 318 is arranged at the position where the boiling container is communicated with the dust transfer container, a grid baffle ring is also arranged in the boiling container, the grid baffle ring is fixed on the inner wall of the boiling container, the axis of the grid baffle ring is superposed with the central line of the boiling container, the grid baffle ring 317 is positioned between the bulk material tray and the filter screen, the distance from the inner surface of the grid baffle ring to the axis of the boiling container is not more than the distance from the edge of the bulk material tray to the axis of the boiling container, and the sharp corner position of the grid baffle ring faces the boiling chamber and extends inwards to the outer edge position of the bulk material tray; the heat-dissipating material is blocked by the check ring, the scattering surface of the material in the boiling chamber is enlarged, the lower part of the boiling container is a conical end, and the air inlet of the boiling container and the material outlet of the boiling container are both arranged at the conical end 307.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications and variations can be made in the embodiments or in part of the technical features of the embodiments without departing from the spirit and the scope of the invention.
Claims (9)
1. The utility model provides a dirt particle separator, its characterized in that, include the support frame and all be fixed in boiling container, dust transfer container, centrifugal force of support frame take place the mechanism and the mechanism takes place for first atmospheric pressure, wherein:
the upper part of the boiling container is communicated with the dust transfer container, a material inlet is formed in the upper end of the boiling container, a material outlet is formed in the lower part of the boiling container, materials in the boiling container are vertically layered under the action of the centrifugal force generating mechanism, dust on the upper layer enters the dust transfer container from the boiling container under the action of the first air pressure generating mechanism, the materials on the lower layer fall out through the material outlet, and a material outlet is formed in the lower part of the boiling container.
2. The dust particle separating device of claim 1, wherein the number of the dust transfer containers is at least two, and the dust transfer containers are uniformly arranged on the peripheral side of the boiling container in a horizontal plane.
3. The dust particle separating apparatus of claim 1, wherein the centrifugal force generating mechanism comprises a power unit, a stirring shaft and a bulk material tray, wherein:
the power unit is fixed above the boiling container;
the stirring shaft is rotatably arranged at the central position in the boiling container under the driving of the power unit, and the stirring shaft is vertically arranged;
the bulk material discs are coaxially arranged on the stirring shaft, the bulk material discs are conical, and the included angle between a bus of the bulk material discs and the horizontal plane is 5-10 degrees.
4. The dust and particle separating device of claim 3, wherein a material distributing assembly is installed in the boiling container, the material distributing assembly is located below the material inlet, the material distributing assembly comprises a plurality of triangular pyramid-shaped material distributing units, the material distributing units are parallel to each other, two ends of each material distributing unit are flush, the material distributing units are arranged in an equilateral triangle, upper vertex angles of all triangular pyramids are vertically upward, and a material distributing channel through which materials can pass is maintained between any three adjacent material distributing units.
5. A dust and particle separating apparatus as claimed in claim 1, wherein a strainer is provided at a position where said boiling vessel communicates with said dust transfer vessel.
6. A dust and particle separating apparatus as claimed in claim 3, wherein said first air pressure generating means comprises an air inlet and a first air extractor, and wherein:
the air inlet of the first air pressure generating mechanism is arranged at the lower part of the boiling container;
and the air inlet end of the first air exhaust fan is communicated with the boiling container and the dust transfer container, and the air outlet end of the first air exhaust fan is communicated to the outside of the boiling container and the dust transfer container.
7. The dust and particle separating device of claim 6, further comprising a conical air guide sleeve, wherein the air guide sleeve is coaxially fixed at a large end thereof in the boiling container and below the material dispersing plate, and the air inlet of the first air pressure generating mechanism extends into the air guide sleeve.
8. A dust and particle separating apparatus as claimed in claim 6, wherein the number of said air inlets of said first air pressure generating means is at least two, and all of said air inlets are uniformly arranged on the peripheral side of the material outlet of the boiling vessel.
9. The dust particle separating apparatus of claim 6, wherein a chimney and a shield are further connected to the air outlet of the first air extractor, wherein: the chimney is vertically arranged, and the air outlet of the first air exhaust fan is communicated to the lower end of the chimney; the protective cover is fixed at the upper end of the chimney, and a distance is kept between the protective cover and the chimney.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021090486.XU CN212596280U (en) | 2020-06-13 | 2020-06-13 | Dust particle separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021090486.XU CN212596280U (en) | 2020-06-13 | 2020-06-13 | Dust particle separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212596280U true CN212596280U (en) | 2021-02-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021090486.XU Expired - Fee Related CN212596280U (en) | 2020-06-13 | 2020-06-13 | Dust particle separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212596280U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113405951A (en) * | 2021-05-07 | 2021-09-17 | 安徽省金标准检测研究院有限公司 | Sample conveying device applied to dust laser detection |
-
2020
- 2020-06-13 CN CN202021090486.XU patent/CN212596280U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113405951A (en) * | 2021-05-07 | 2021-09-17 | 安徽省金标准检测研究院有限公司 | Sample conveying device applied to dust laser detection |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Feng Quanyi Inventor after: Feng Yanzhao Inventor after: Wang Shitou Inventor before: Feng Quanyi Inventor before: Feng Yanzhao |
|
| CB03 | Change of inventor or designer information | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210226 |
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| CF01 | Termination of patent right due to non-payment of annual fee |