CN209865627U - Wave spiral type spray desulfurization dust-removing device - Google Patents
Wave spiral type spray desulfurization dust-removing device Download PDFInfo
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- CN209865627U CN209865627U CN201920586351.3U CN201920586351U CN209865627U CN 209865627 U CN209865627 U CN 209865627U CN 201920586351 U CN201920586351 U CN 201920586351U CN 209865627 U CN209865627 U CN 209865627U
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- wave
- spiral
- bath room
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- room
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Abstract
The utility model discloses a wave spiral type spray desulfurization dust removal device, which comprises a shell, a wave bath room, a spiral bath room and a transfer drying room which are sequentially arranged in the shell, wherein the bottom of the shell is also provided with an ash settling area, a tower type sprayer is arranged in the wave bath room, a wave type baffle I is arranged on the side wall in the wave bath room, a column type sprayer is arranged in the spiral bath room, a spiral type baffle II is arranged on the side wall of the spiral bath room, the upper ends of the wave bath room and the spiral bath room are communicated, the lower ends of the spiral bath room and the transfer drying room are communicated, the lower end of the shell is provided with a water outlet pipe communicated with the ash settling area, a sedimentation tank and a water pump are sequentially arranged on the water outlet pipe, one end of the water outlet pipe close to the water pump is, the column type sprayers are communicated, the transfer drying chamber is internally provided with a drying device, and one side of the transfer drying chamber is provided with a tail treatment area. The utility model discloses the appearance is simple, and the shaping is makeed easily, reduces equipment cost of manufacture, the energy saving, the environmental protection, the low carbon.
Description
Technical Field
The utility model relates to a desulfurization dust collector technical field, concretely relates to spiral desulfurization dust collector that sprays of wave.
Background
Common wet desulfurization dust removal purification equipment is of a spray type, a cyclone type, a water storage impact water bath type, a tower plate type, a venturi and the like. However, the flue gas generally contains sulfur, so that the dust removing equipment is easy to corrode after the flue gas is contacted with water. Secondly, due to the limitation of various factors, the dust removal efficiency of a single dust remover is not very high.
Disclosure of Invention
The utility model discloses the problem that will solve is: the wave spiral type spraying desulfurization dust removal device can improve the purification efficiency of coal-fired flue gas, effectively achieves the purpose of desulfurization and dust removal, is simple in appearance, easy to manufacture and form, capable of reducing the manufacturing cost of equipment, energy-saving, environment-friendly and low-carbon.
The utility model discloses a solve the technical scheme that above-mentioned problem provided and do: the utility model provides a spiral desulfurization dust collector that sprays of wave, includes the shell and sets gradually the inside wave of shell is bathed bathroom, spiral and is bathed bathroom and transfer drying chamber, be close to on the shell one side that the wave was bathed the bathroom is equipped with the air inlet, the bottom of shell still is equipped with the heavy grey district, heavy grey district with the wave is bathed the bathroom, the spiral lower extreme that bathes the bathroom communicates with each other, be equipped with tower sprayer in the wave shower room, be equipped with the baffle of wave formula one on the indoor lateral wall of wave shower, be equipped with the column type sprayer in the spiral shower room, be equipped with spiral baffle two on the lateral wall of spiral shower bathroom, the wave is bathed the bathroom and the spiral upper end that bathes the bathroom communicates with each other, the spiral is bathed the lower extreme of bathroom and transfer drying chamber and is communicated with each other, the lower extreme of shell is equipped with the communicating outlet pipe of heavy grey district, be equipped, one end of the water outlet pipe, which is close to the water pump, is respectively communicated with the tower type sprayer and the column type sprayer, a drying device is arranged in the transfer drying chamber, and a tail treatment area is arranged on one side of the transfer drying chamber.
Preferably, the tail treatment chamber comprises a treatment chamber, and a tail residual ash water outlet and an air outlet which are arranged on the treatment chamber.
Preferably, a vertical partition plate is arranged in the transfer drying chamber.
Preferably, the separator is made of stainless steel.
Preferably, a side shower head is arranged on the side wall of the upper end of the wave shower room.
Preferably, the upper end of the spiral shower room is provided with an upper shower head.
Preferably, the first baffle plate and the second baffle plate are both made of stainless steel.
Compared with the prior art, the utility model has the advantages that: the utility model discloses combined fountain, wave plate and spiral, this purification dust collection efficiency who has just improved the coal-fired flue gas that contains sulphur effectively, equipment appearance simple structure has reduced equipment cost of manufacture, reduces the energy consumption in the use, low carbon environmental protection.
Drawings
The accompanying drawings, which are described herein, serve to provide a further understanding of the invention and constitute a part of this specification, and the exemplary embodiments and descriptions thereof are provided for explaining the invention without unduly limiting it.
Fig. 1 is a schematic view of the overall structure of the present invention;
the attached drawings are marked as follows: 1. the device comprises an upper bath head, a side bath head, a wave bath chamber, a 4 air inlet, a 5 ash settling zone, a 6 spiral bath chamber, a 7 transfer drying chamber, a 8 tower type sprayer, a 9 column type sprayer, a 10 tail residual ash outlet, a 11 treatment chamber, a 12 air outlet, a 13 sedimentation tank, a 14 drying device, a 15 baffle, a 16 water outlet pipe, a 17 water pump, a 18 baffle I, a 19 baffle I, a shell, a 20 baffle II, a water outlet pipe, a water pump, a.
Detailed Description
The following detailed description will be made with reference to the accompanying drawings and examples, so that how to implement the technical means of the present invention to solve the technical problems and achieve the technical effects can be fully understood and implemented.
The specific embodiment of the utility model is shown in fig. 1, a wave spiral type spray desulfurization dust removal device, comprises a shell 19, and a wave bath 3, a spiral bath 6 and a transfer drying chamber 7 which are sequentially arranged in the shell 19, one side of the shell 19 close to the wave bath 3 is provided with an air inlet 4, the bottom of the shell 19 is also provided with an ash settling area 5, the ash settling area 5 is communicated with the lower ends of the wave bath 3 and the spiral bath 6, a tower type sprayer 8 is arranged in the wave bath 3, a wave type baffle I18 is arranged on the side wall in the wave bath 3, a column type sprayer 9 is arranged in the spiral bath 6, a spiral type baffle II 20 is arranged on the side wall of the spiral bath 6, the upper end of the bath 3 is communicated with the upper end of the spiral bath 6, the spiral bath 6 is communicated with the lower end of the transfer drying chamber 7, the lower end of the shell 19 is provided with a water outlet pipe 16 communicated with the ash settling area 5, the water outlet pipe 16 is sequentially provided with a sedimentation tank 13 and a water pump 17, one end of the water outlet pipe 16 close to the water pump 17 is respectively communicated with the tower type sprayer 8 and the column type sprayer 9, the transfer drying chamber 7 is internally provided with a drying device 14, and one side of the transfer drying chamber 7 is provided with a tail treatment area.
The tail treatment area comprises a treatment chamber 11, and a tail residual ash water outlet 10 and an air outlet 12 which are arranged on the treatment chamber 11.
A vertical partition 15 is arranged in the transfer drying chamber 7.
The partition 15 is made of stainless steel.
The side shower head 2 is arranged on the side wall of the upper end of the wave shower room 3.
The upper end of the spiral bath room 6 is provided with an upper bath head 1.
The first baffle plate 18 and the second baffle plate 20 are both made of stainless steel materials.
The utility model discloses a realize like this: gas enters the shell from the gas inlet, then impacts the water surface of the ash settling tank, and enters the wave spraying chamber for spraying to achieve first purification; and then the gas reaches the top end and is secondarily sprayed and purified by the side shower head and the upper shower head, the gas is transferred to the spiral spraying chamber, water mist is sprayed out of the middle steel pipe in the spiral gap to improve the dust wetting efficiency, dust particles and water drops or dust particles and dust particles are condensed to be easier to be trapped, and the effect of secondary purification is achieved. The last structure is that the spiral lower clapboard is directly inserted below the liquid level of the ash settling tank, so that the gas from the lower clapboard continuously impacts the water surface again to achieve the fourth purification. The dust particles in the air flow are captured by a water film of the ash settling tank, the purified air is discharged from the air outlet after being transferred by the transfer drying chamber and being treated by the tail part, the ash settling is discharged from the water outlet, and the discharged waste water can be sprayed for use after being settled, so that the high-efficiency purification is achieved.
The utility model has the advantages that: the utility model discloses combined fountain, wave plate and spiral, this purification dust collection efficiency who has just improved the coal-fired flue gas that contains sulphur effectively, equipment appearance simple structure has reduced equipment cost of manufacture, reduces the energy consumption in the use, low carbon environmental protection.
The foregoing is illustrative of the preferred embodiments of the present invention only, and is not to be construed as limiting the claims. The present invention is not limited to the above embodiments, and the specific structure thereof is allowed to be changed. All changes which come within the scope of the independent claims of the invention are to be embraced within their scope.
Claims (7)
1. The utility model provides a spiral desulfurization dust collector that sprays of wave which characterized in that: comprises a shell (19) and a wave bath room (3), a spiral bath room (6) and a transfer drying chamber (7) which are sequentially arranged inside the shell (19), wherein one side of the shell (19) close to the wave bath room (3) is provided with an air inlet (4), the bottom of the shell (19) is also provided with an ash settling area (5), the ash settling area (5) is communicated with the lower ends of the wave bath room (3) and the spiral bath room (6), a tower type sprayer (8) is arranged in the wave bath room (3), a wave type first baffle (18) is arranged on the side wall in the wave bath room (3), a column type sprayer (9) is arranged in the spiral bath room (6), a spiral second baffle (20) is arranged on the side wall of the spiral bath room (6), the upper ends of the wave bath room (3) and the spiral bath room (6) are communicated, the spiral shower room (6) is communicated with the lower end of the transfer drying chamber (7), a water outlet pipe (16) communicated with the ash settling area (5) is arranged at the lower end of the shell (19), a sedimentation tank (13) and a water pump (17) are sequentially arranged on the water outlet pipe (16), one end of the water pump (17) is close to the water outlet pipe (16) and communicated with the tower type sprayer (8) and the column type sprayer (9) respectively, a drying device (14) is arranged in the transfer drying chamber (7), and a tail treatment area is arranged on one side of the transfer drying chamber (7).
2. The wave spiral type spray desulfurization dust removal device of claim 1, characterized in that: the tail treatment area comprises a treatment chamber (11), and a tail residual ash water outlet (10) and an air outlet (12) which are arranged on the treatment chamber (11).
3. The wave spiral type spray desulfurization dust removal device of claim 1, characterized in that: a vertical clapboard (15) is arranged in the transfer drying chamber (7).
4. The wave spiral type spray desulfurization dust removal device of claim 3, characterized in that: the partition plate (15) is made of stainless steel.
5. The wave spiral type spray desulfurization dust removal device of claim 1, characterized in that: the side shower head (2) is arranged on the side wall of the upper end of the wave shower room (3).
6. The wave spiral type spray desulfurization dust removal device of claim 1, characterized in that: the upper end of the spiral bath room (6) is provided with an upper bath head (1).
7. The wave spiral type spray desulfurization dust removal device of claim 1, characterized in that: the first baffle plate (18) and the second baffle plate (20) are both made of stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920586351.3U CN209865627U (en) | 2019-04-26 | 2019-04-26 | Wave spiral type spray desulfurization dust-removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920586351.3U CN209865627U (en) | 2019-04-26 | 2019-04-26 | Wave spiral type spray desulfurization dust-removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209865627U true CN209865627U (en) | 2019-12-31 |
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ID=68962369
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920586351.3U Expired - Fee Related CN209865627U (en) | 2019-04-26 | 2019-04-26 | Wave spiral type spray desulfurization dust-removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209865627U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115364602A (en) * | 2022-07-28 | 2022-11-22 | 陕西彩虹工业智能科技有限公司 | Dust collection box and method for TFT glass kiln flue gas treatment |
-
2019
- 2019-04-26 CN CN201920586351.3U patent/CN209865627U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115364602A (en) * | 2022-07-28 | 2022-11-22 | 陕西彩虹工业智能科技有限公司 | Dust collection box and method for TFT glass kiln flue gas treatment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200916 Address after: 335500 chemical industry zone, Wannian Industrial Park, Shangrao City, Jiangxi Province Patentee after: Jiangxi Yinhai Pharmaceutical Chemical Co.,Ltd. Address before: 330000 Nanchang, Jiangxi province and South Road, No. 696 Patentee before: Nanchang Hangkong University (NCHU) |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191231 Termination date: 20210426 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |