CN211886047U - Vortex type dust processor - Google Patents
Vortex type dust processor Download PDFInfo
- Publication number
- CN211886047U CN211886047U CN202020102331.7U CN202020102331U CN211886047U CN 211886047 U CN211886047 U CN 211886047U CN 202020102331 U CN202020102331 U CN 202020102331U CN 211886047 U CN211886047 U CN 211886047U
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- CN
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- Prior art keywords
- reaction
- water
- cabin
- reaction cabin
- pond
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- Expired - Fee Related
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- 239000000428 dust Substances 0.000 title claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 70
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 238000000926 separation method Methods 0.000 claims abstract description 19
- 230000004888 barrier function Effects 0.000 claims description 12
- 238000004891 communication Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000009471 action Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- -1 steam separation Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model provides an eddy current type dust processor belongs to mechanical technical field. This eddy current type dust processor includes the frame, surround through the bounding wall on frame upper portion and form the reaction cabin, the reaction cabin opening is seted up at the top, be equipped with the steam separation that a plurality of levels were placed in the reaction cabin and separate the net, it has the communicating drum formula reaction barrel with the reaction cabin to set firmly at the reaction cabin lower extreme, lateral part at the reaction barrel is equipped with and the inside communicating wind direction water conservancy diversion passageway of reaction barrel, surround through the bounding wall at the frame bottom and be formed with the circulation pond, be equipped with the baffle of placing the filter screen above the circulation pond, the filter screen is just to the export of reaction barrel, it has the auxiliary water pond to communicate at circulation pond lateral part, the suction pump has been placed in the auxiliary water pond, seted up the water inlet at the reaction cabin lateral part and water. The utility model has the advantages of simple structure and good filtering effect.
Description
Technical Field
The utility model belongs to the technical field of machinery, concretely relates to eddy current type dust processor.
Background
At present water filtration formula dust treatment equipment, generally adopt water curtain formula filtration and fountain to filter as leading direction, water curtain formula and fountain dust are little with water contact surface, and the contact time is short can not be effectual all precipitate the dust dissolve to the water the inside, leads to the dust to arrange outdoor influence environment.
Disclosure of Invention
The utility model aims at having the above-mentioned problem to current technique, provided an eddy current type dust processor that simple structure, filter effect are good.
The purpose of the utility model can be realized by the following technical proposal: the utility model provides an eddy current type dust processor, which comprises a frame, a serial communication port, it forms the reaction cabin to surround through the bounding wall on frame upper portion, the top is seted up to the reaction cabin opening, be equipped with the steam separation barrier net that a plurality of levels were placed in the reaction cabin, set firmly at the reaction cabin lower extreme with the communicating drum formula reaction tube in reaction cabin, lateral part at the reaction tube be equipped with the inside communicating wind direction water conservancy diversion passageway of reaction tube, it has circulating water pond to surround through the bounding wall in frame bottom, be equipped with the baffle of placing the filter screen above circulating water pond, the filter screen is just to the export of reaction barrel, circulating water pond lateral part intercommunication has the auxiliary water pond, the suction pump has been placed in the auxiliary water pond, water inlet and water inlet pass through pipeline and suction pump UNICOM have been seted.
In the vortex type dust processor, a plurality of fixed supports are arranged in the reaction chamber, the fixed supports are divided into two groups and are arranged in parallel up and down, two cabin doors are arranged on the side part of the reaction chamber, each cabin door corresponds to one group of fixed supports, and the water-vapor separation barrier net is placed on each fixed support.
Compared with the prior art, the utility model has the advantages of it is following: the reaction chamber is provided with the reaction cylinder below, the side part of the reaction cylinder is provided with the wind direction diversion channel communicated with the inside of the reaction cylinder, when steam and dust enter the reaction chamber from the opening of the reaction chamber, the water in the circulating water tank is pumped into the reaction chamber by the water pump to form spraying, the wind direction diversion channel is externally connected with the exhaust fan, the exhaust fan conveys outside air into the reaction cylinder and forms vortex in the reaction cylinder, at the moment, the water, the steam and the dust are mixed together while forming the vortex, the dust is fused into the water and moves downwards under the action of gravity, the steam moves upwards along with the action of the vortex and is adsorbed on the water-vapor separation barrier net under the action of the water-vapor separation barrier net, so that the water and the steam are separated, the water containing the dust flows onto the filter net through the outlet of the reaction cylinder, the water after the dust is filtered and intercepted by the filter screen enters the circulating water tank again, the water is pumped into the reaction chamber again by the water pump for recycling, and only the dust filtered by the filter screen is collected and cleaned after the recovery is finished, so that the dust purification rate is better, and the water source does not need to be frequently replaced
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic view of a partial structure of the present invention.
Fig. 3 is a schematic sectional structure diagram of the present invention.
In the figure, 1, a frame; 2. a reaction chamber; 3. a water-vapor separation barrier net; 4. a wind direction diversion channel; 5. a reaction cylinder; 6. a circulating water tank; 7. a filter screen; 8. a partition plate; 9. a secondary water pool; 10. a water inlet; 11. fixing a bracket; 12. a hatch door.
Detailed Description
The following are specific embodiments of the present invention and the accompanying drawings are used to further describe the technical solution of the present invention, but the present invention is not limited to these embodiments.
As shown in fig. 1 to 3, the vortex type dust processor comprises a frame 1, a reaction chamber 2 is formed on the upper portion of the frame 1 through surrounding plates, an opening of the reaction chamber 2 is arranged at the top, a plurality of horizontally arranged water-vapor separation blocking nets 3 are arranged in the reaction chamber 2, a cylindrical reaction barrel 5 communicated with the reaction chamber 2 is fixedly arranged at the lower end of the reaction chamber 2, a wind direction diversion channel 4 communicated with the inside of the reaction barrel 5 is arranged on the lateral portion of the reaction barrel 5, a circulating water tank 6 is formed at the bottom of the frame 1 through surrounding plates, a partition plate 8 provided with a filter screen 7 is arranged above the circulating water tank 6, the filter screen 7 is opposite to an outlet of the reaction barrel 5, a secondary water tank 9 is communicated with the lateral portion of the circulating water tank 6, a water suction pump is arranged in the secondary water tank 9, a water inlet 10 is arranged on the lateral portion of the reaction.
The steam referred to in the present application is specifically waste gas generated in industrial production, a reaction cylinder 5 is arranged below a reaction chamber, a wind direction diversion channel 4 communicated with the inside of the reaction cylinder 5 is arranged on the side part of the reaction cylinder 5, an opening of a reaction chamber 2 is externally connected with a steam inlet pipeline, when steam and dust enter the reaction chamber 2 from the opening of the reaction chamber 2, a water pump (not shown in the figure) pumps water in a circulating water pool 6 into the reaction chamber 2 to form spraying, meanwhile, wind is externally connected with an exhaust fan from the diversion channel 4, the exhaust fan conveys external air into the reaction cylinder 5 and forms vortex in the reaction chamber 5, at the moment, the water, the steam and the dust are mixed together while forming the vortex, the dust is fused into the water and moves downwards under the action of gravity, the steam moves upwards under the action of the vortex and is adsorbed on a water-vapor separation and separation net 3 under the action of the water-vapor separation and separation net 3, thereby make water, steam separation, water that contains the dust flows through to filter screen 7 through the export of reaction section of thick bamboo 5 on, water reenters circulating water pond 6 after filter screen 7 filters the interception dust to pump water to reaction chamber internal recycle once more by the suction pump, and after retrieving the completion only need filter screen 7 down the dust collect the clearance can, dust purification rate is better, need not frequently to change the water source.
The wind direction flow guide channel 4 is an arc-shaped channel, and the outlet tangent line is tangent to the inner wall of the reaction cylinder 5, so that air can better and faster enter the vortex device to form a vortex, and water, gas and dust can be better fused together.
Be equipped with a plurality of fixed bolsters 11 in reaction chamber, fixed bolster 11 divide into two sets ofly and same group's fixed bolster 11 parallel arrangement from top to bottom, install two hatch doors 12 and every hatch door 12 corresponds a set of fixed bolster 11 at reaction chamber 2's lateral part, foretell steam separation barrier net 3 has all been placed on every fixed bolster 11, steam separation barrier net 3 adopts the multiplate structure, make that vapour can be better by the interception on steam separation barrier net 3, every hatch door 12 corresponds a set of fixed bolster 11 simultaneously, when needing to be changed steam separation barrier net 3, only need open hatch door 12 with corresponding steam separation barrier net 3 take out can.
The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications, additions and substitutions for the specific embodiments described herein may be made by those skilled in the art without departing from the spirit of the invention or exceeding the scope of the invention as defined in the accompanying claims.
Claims (2)
1. The utility model provides an eddy current type dust processor, which comprises a frame, a serial communication port, it forms the reaction cabin to surround through the bounding wall on frame upper portion, the top is seted up to the reaction cabin opening, be equipped with the steam separation barrier net that a plurality of levels were placed in the reaction cabin, set firmly at the reaction cabin lower extreme with the communicating drum formula reaction tube in reaction cabin, lateral part at the reaction tube be equipped with the inside communicating wind direction water conservancy diversion passageway of reaction tube, it has circulating water pond to surround through the bounding wall in frame bottom, be equipped with the baffle of placing the filter screen above circulating water pond, the filter screen is just to the export of reaction barrel, circulating water pond lateral part intercommunication has the auxiliary water pond, the suction pump has been placed in the auxiliary water pond, water inlet and water inlet pass through pipeline and suction pump UNICOM have been seted.
2. The vortex type dust processor as claimed in claim 1, wherein a plurality of fixing brackets are arranged in the reaction chamber, the fixing brackets are divided into two groups, the fixing brackets of the same group are arranged in parallel up and down, two hatches are installed at the side of the reaction chamber, each hatche corresponds to one group of fixing brackets, and the water-vapor separation barrier net is placed on each fixing bracket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020102331.7U CN211886047U (en) | 2020-01-13 | 2020-01-13 | Vortex type dust processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020102331.7U CN211886047U (en) | 2020-01-13 | 2020-01-13 | Vortex type dust processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211886047U true CN211886047U (en) | 2020-11-10 |
Family
ID=73302732
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020102331.7U Expired - Fee Related CN211886047U (en) | 2020-01-13 | 2020-01-13 | Vortex type dust processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211886047U (en) |
-
2020
- 2020-01-13 CN CN202020102331.7U patent/CN211886047U/en not_active Expired - Fee Related
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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: 20201110 |