CN215085878U - Cyclone dust removal oxidation tower - Google Patents
Cyclone dust removal oxidation tower Download PDFInfo
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- CN215085878U CN215085878U CN202120756320.5U CN202120756320U CN215085878U CN 215085878 U CN215085878 U CN 215085878U CN 202120756320 U CN202120756320 U CN 202120756320U CN 215085878 U CN215085878 U CN 215085878U
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Abstract
The utility model discloses a whirl dust removal oxidation tower mainly relates to environmental protection exhaust-gas treatment equipment technical field, including the tower body installation pivot in the tower body the symmetry is equipped with down whirl board, upward whirl board in the pivot be equipped with turbulent flow board between lower whirl board, the upward whirl board the tower body, top are equipped with spray line, and the shower nozzle evenly sets up on spray line both ends are equipped with the pipeline of giving vent to anger respectively about the tower body side, and inlet duct is through at the whirl board, and it is rotatory to utilize the pivot to drive, forms the rotatory rotational flow bed structure of hypergravity, and gas-liquid mass transfer process can be strengthened greatly to turbulent flow board simultaneously, improves the absorption and separation efficiency, reduces the volume of equipment, reduces equipment and drops into.
Description
Technical Field
The utility model relates to an environmental protection exhaust-gas treatment equipment technical field specifically is a whirl dust removal oxidation tower.
Background
The dust-containing gas is introduced from the lower part of the cylinder body in the tangential direction, rotates and rises, dust particles are separated under the action of centrifugal force, are thrown to the inner wall of the cylinder body, are adsorbed by a water film layer flowing on the inner wall of the cylinder body, flow to the cone at the bottom along with water, and are discharged through the dust discharge port. The water film layer is formed by spraying water to the wall of the cylinder body tangentially through a plurality of nozzles arranged at the upper part of the cylinder body. Therefore, the inner wall of the cylinder is always covered with a layer of thin water film which rotates to flow downwards, and the aim of improving the dust removal effect is fulfilled.
Chinese patent application with patent application number CN201710062444.1 discloses a dust removal absorption tower, and flue gas desulfurization, dust removal technology adopt to spray against the current, pack formula absorption tower design, and the well lower part of absorption tower is equipped with the flue gas inlet, is equipped with water spray cooling device in import flue department, and the absorption tower top is equipped with exhanst gas outlet, and inside top-down is equipped with in proper order: silk screen removes foam section, aerosol washing section, defogging section, absorption section and flue gas equipartition dust removal section, is equipped with oxidation air distribution calandria and pump agitating unit in the oxidation pond at the bottom of the tower inside, and the outside is equipped with compressed air entry, aqueous ammonia entry and absorption circulating pump entry, and the bottom is equipped with ammonium sulfate and arranges thick liquid pump entry.
However, the flue gas flows through the inside of the oxidation tower quickly in the existing device, so that water and dust cannot be effectively adsorbed, the dust treatment efficiency in the flue gas is low, and the flue gas is not thoroughly purified.
SUMMERY OF THE UTILITY MODEL
Thereby leading to water and the unable effective absorption of dust fast in view of the inside circulation of the flue gas that exists among the prior art at the oxidation tower, causing the dust treatment inefficiency in the flue gas, and then cause gas cleaning's not thorough problem, the utility model provides a whirl dust removal oxidation tower.
In order to solve the technical problem, the utility model discloses a following technical scheme: a cyclone dust removal oxidation tower is characterized in that: the tower comprises a tower body, wherein a rotating shaft is arranged in the tower body, a lower rotating flow plate and an upper rotating flow plate are symmetrically arranged on the rotating shaft, a turbulent flow plate is arranged between the lower rotating flow plate and the upper rotating flow plate, a spray pipeline is arranged at the top of the tower body, spray heads are uniformly arranged on the spray pipeline, and an air outlet pipeline and an air inlet pipeline are respectively arranged at the upper end and the lower end of the side surface of the tower body.
As a further improvement of the utility model, the upper end and the lower end of the turbulent flow plate are respectively fixedly connected with the upper cyclone plate and the lower cyclone plate, and the left end and the right end are in close contact with the side wall of the tower body.
As a further improvement of the utility model, the turbulent flow plate is provided with a through hole.
As a further improvement of the utility model, the tower body, the driving motor at top are connected to the pivot.
As a further improvement of the utility model, the bottom of the tower body is provided with a waste liquid outlet.
Compared with the prior art, the utility model discloses the beneficial effect who has does: the rotating shaft is used for driving the rotating plate to rotate to form a super-gravity rotating cyclone bed structure, and meanwhile, the turbulent plate can greatly strengthen the gas-liquid mass transfer process, improve the absorption and separation efficiency, reduce the volume of equipment and reduce the equipment investment.
Drawings
The invention will be further described with reference to the accompanying drawings and specific embodiments:
FIG. 1 is a schematic structural view of a cyclone dust removal oxidation tower of the present invention;
in the figure: 1, a tower body; 2 an air inlet pipeline; 3, a lower vortex plate; 4, rotating the flow plate; 5, a spray pipeline; 6, a spray head; 7, an air outlet pipeline; 8 driving a motor; 9 a rotating shaft; 10 turbulent flow plate; 11 through holes; 12 waste liquid outlet.
Detailed Description
In order to make the technical solution and the advantageous effects of the present invention more clear, the present invention will be further described in detail with reference to the following embodiments.
The utility model discloses a whirl dust removal oxidation tower, refer to figure 1, it includes tower body 1 installation pivot 9 in the tower body 1 the symmetry is equipped with down whirl board 3, last whirl board 4 in pivot 9 be equipped with turbulent flow board 10 down between whirl board 3, the last whirl board 4 tower body 1, top are equipped with spray piping 5, and shower nozzle 6 evenly sets up on spray piping 5 both ends are equipped with air outlet pipe 7, admission line 2 respectively about the tower body 1 side.
In the use process, the driving motor 8 drives the lower vortex plate 3 and the upper vortex plate 4 to rotate through the rotating shaft 9, gas enters from the gas inlet pipeline 2 at the bottom of the tower, liquid enters from the spray pipeline 5 at the top of the tower, the gas and the liquid are in reverse contact, the gas in the tower enters the vortex plates through the gas holes under the action of the upper baffles of the lower vortex plate 3 and the upper vortex plate 4 to form vortexes opposite to the rotating direction of the vortex plates, the liquid in the vortex plates is rapidly mixed with the gas in the whole vortex plates under the combined action of the gas flow and the blades, and the gas is distributed again through the turbulence plates 10 to absorb the gas. The liquid is discharged through a waste outlet 12. The gas is discharged through the gas outlet pipe 7.
The upper end and the lower end of the turbulent flow plate 10 are respectively fixedly connected with an upper turbulent flow plate 4 and a lower turbulent flow plate 3, the left end and the right end are tightly contacted with the side wall of the tower body 1, and the turbulent flow plate 10 is provided with a through hole 11. The rotating shaft 9 is connected with the tower body 1 and the driving motor 8 at the top, and a waste liquid outlet 12 is arranged at the bottom of the tower body 1.
It should be understood that the detailed description and specific examples, while indicating the invention, are given by way of illustration only, not by way of limitation, since other embodiments will become apparent to those skilled in the art upon consideration of the following detailed description of the invention without any creative effort.
Claims (5)
1. A cyclone dust removal oxidation tower is characterized in that: the tower comprises a tower body (1), wherein a rotating shaft (9) is installed in the tower body (1), a lower rotating flow plate (3) and an upper rotating flow plate (4) are symmetrically arranged on the rotating shaft (9), a turbulent flow plate (10) is arranged between the lower rotating flow plate (3) and the upper rotating flow plate (4), a spray pipeline (5) is arranged at the top of the tower body (1), spray heads (6) are uniformly arranged on the spray pipeline (5), and an air outlet pipeline (7) and an air inlet pipeline (2) are respectively arranged at the upper end and the lower end of the side surface of the tower body (1).
2. The cyclone dust removal oxidation tower as claimed in claim 1, wherein: the upper end and the lower end of the turbulent flow plate (10) are respectively fixedly connected with the upper vortex plate (4) and the lower vortex plate (3), and the left end and the right end are tightly contacted with the side wall of the tower body (1).
3. The cyclone dust removal oxidation tower as claimed in claim 1 or 2, wherein: the turbulent flow plate (10) is provided with a through hole (11).
4. The cyclone dust removal oxidation tower as claimed in claim 1, wherein: the rotating shaft (9) is connected with the tower body (1) and the driving motor (8) at the top.
5. The cyclone dust removal oxidation tower as claimed in claim 4, wherein: and a waste liquid outlet (12) is arranged at the bottom of the tower body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120756320.5U CN215085878U (en) | 2021-04-14 | 2021-04-14 | Cyclone dust removal oxidation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120756320.5U CN215085878U (en) | 2021-04-14 | 2021-04-14 | Cyclone dust removal oxidation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215085878U true CN215085878U (en) | 2021-12-10 |
Family
ID=79265439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120756320.5U Active CN215085878U (en) | 2021-04-14 | 2021-04-14 | Cyclone dust removal oxidation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215085878U (en) |
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2021
- 2021-04-14 CN CN202120756320.5U patent/CN215085878U/en active Active
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