CN220715284U - Spiral-flow type exhaust-gas treatment tower - Google Patents
Spiral-flow type exhaust-gas treatment tower Download PDFInfo
- Publication number
- CN220715284U CN220715284U CN202322479096.1U CN202322479096U CN220715284U CN 220715284 U CN220715284 U CN 220715284U CN 202322479096 U CN202322479096 U CN 202322479096U CN 220715284 U CN220715284 U CN 220715284U
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- China
- Prior art keywords
- cyclone
- tower body
- spray
- washing tower
- pipe
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- 239000007921 spray Substances 0.000 claims abstract description 120
- 238000005406 washing Methods 0.000 claims abstract description 56
- 238000010521 absorption reaction Methods 0.000 claims abstract description 47
- 239000002131 composite material Substances 0.000 claims abstract description 41
- 238000005507 spraying Methods 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims description 42
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 239000000945 filler Substances 0.000 claims description 21
- 238000001914 filtration Methods 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 4
- 239000003546 flue gas Substances 0.000 claims description 4
- 239000002912 waste gas Substances 0.000 abstract description 55
- 238000000746 purification Methods 0.000 abstract description 11
- 239000012535 impurity Substances 0.000 description 26
- 239000000428 dust Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 6
- 239000002250 absorbent Substances 0.000 description 5
- 230000002745 absorbent Effects 0.000 description 5
- 238000012856 packing Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 239000010815 organic waste Substances 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model belongs to the technical field of waste gas treatment, and particularly discloses a cyclone waste gas treatment tower, which comprises a cyclone spray washing tower body; the top of the cyclone spray washing tower body is connected with the bottom of the spray absorption composite tower body through a first air pipe; the top of the spray absorption composite tower body is connected with the filter device body through a second air pipe; a first spray assembly and a cyclone separator are arranged in the cyclone spray washing tower body; the air inlet pipe of the cyclone separator is connected with the air inlet pipeline, and the air outlet pipe is connected with the first air pipe; the cyclone separator is connected with a first calandria of the cyclone spray washing tower body; a first filter plate is arranged below the cyclone separator; a first water tank is arranged on the inner side of the bottom of the cyclone spray washing tower body; the first water tank is connected with the first spraying assembly through a first circulating water pipe. The utility model can realize good purification of waste gas.
Description
Technical Field
The utility model particularly relates to the technical field of waste gas treatment, in particular to a spiral-flow type waste gas treatment tower.
Background
The traditional method for treating the organic waste gas comprises the methods such as an adsorption method, an absorption method, an oxidation method, biological treatment and the like, and when the traditional method is used for treating the organic waste gas, the treatment time of the organic waste gas is shorter, so that the waste gas cannot be effectively adsorbed and separated, the treatment effect is not ideal, the emission standard of the waste gas is easily caused to be substandard, and the waste gas is treated for multiple times, so that the production cost of enterprises is increased.
Patent document CN2902422Y discloses a swirling exhaust gas treatment device; including containing flue gas import, heart fan, flue gas import's front end is equipped with centrifugal fan, and flue gas import's the other end is connected the dust remover end storehouse, and the top in dust remover end storehouse is connected the dust remover and is gone up the storehouse, and the dust remover end storehouse is equipped with the whirl board with the dust remover junction of going up the storehouse, goes up the connecting pipe outward of the upper surface of whirl board, is equipped with the several shower nozzle on the connecting pipe. When the treatment device in the above patent is used for treating waste gas, the blowing of the waste gas is realized through the two cyclone blades arranged in the middle bin of the dust remover, so that the removal of impurities in the waste gas is realized, but the waste gas is subjected to larger resistance when being upwards transferred, so that the waste gas cannot be effectively transferred to the cyclone blades above for treating the waste gas again, the treatment method in the above patent is lower in efficiency, and the spraying device in the above patent simply sprays the waste gas in the dust remover through clean water, so that the effective adsorption of the impurities in the waste gas cannot be realized.
Accordingly, there is a need for an exhaust treatment device that at least partially addresses the above-described problems.
Disclosure of Invention
The utility model aims to provide a cyclone waste gas treatment tower, wherein a filtering device body is further arranged in the cyclone waste gas treatment tower, active carbon is filled in the filtering device body, and the active carbon is effectively adsorbed to ensure the purification rate of waste gas; to solve the problems set forth in the background art.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
a cyclone type waste gas treatment tower comprises a cyclone spray washing tower body; the bottom of the cyclone spray washing tower body is provided with a supporting frame; the top of the cyclone spray washing tower body is connected with the bottom of the spray absorption composite tower body through a first air pipe; the top of the spray absorption composite tower body is connected with the filtering device body through a second air pipe; one end of the filter device body, which is far away from the spray absorption composite tower body, is connected with an output pipeline through a third air pipe, and a main fan is arranged on the side surface of the output pipeline; the cyclone spray washing tower body is internally provided with a first spray assembly; a cyclone separator is arranged below the first spraying assembly; the air inlet pipe of the cyclone separator is connected with the air inlet pipeline; the air outlet pipe of the cyclone separator is connected with the first air pipe; the cyclone separator is connected with a first calandria arranged on the cyclone spray washing tower body; a first filter plate is arranged below the cyclone separator; the inner side of the bottom of the cyclone spray washing tower body is provided with a first water tank; the first water tank is connected with the first spraying assembly through a first circulating water pipe.
As a further technical scheme of the utility model, a second spraying component is arranged at the top end inside the spraying absorption composite tower body; a filler is arranged below the second spraying assembly; the filler is provided with a plurality of layers; a filter plate is arranged below the filler; a second water tank is arranged between the filter plate and the bottom of the spray absorption composite tower body; the bottom of the spray absorption composite tower body is provided with a second calandria; the outer side of the bottom of the spray absorption composite tower body is provided with a supporting frame.
As a further technical scheme of the utility model, a filtering device body is arranged on one side of the spray absorption composite tower body far away from the cyclone spray washing tower body; the filter device body is internally provided with active carbon; the outer side of the bottom of the filtering device body is provided with a bracket; the filtering device body is connected with the pipeline through a third air pipe at one end far away from the second air pipe.
As a further technical scheme of the utility model, the bottom of the pipeline is provided with a supporting piece.
As a further technical scheme of the utility model, the second water tank is connected with the second spraying assembly through a second circulating water pipe.
As a further technical scheme of the utility model, a flow dividing plate is arranged between the filter plate and the cyclone separator.
In this device, waste gas first choice gets into the whirl spray washing tower body, realize having lower separation to the impurity of waste gas inside through the inside cyclone separator of whirl spray washing tower body, great granule or volumetric impurity are discharged downwards, the waste gas that the separation was accomplished upwards transmits, be provided with first spray subassembly above the whirl spray washing tower body, handle waste gas again, it is originally internal that the gas that the spraying was accomplished gets into the spray absorption composite tower through first tuber pipe, be provided with the filter in spray absorption composite tower body inside, gas passes through the even transmission of filter in the filler, adsorb the impurity that realizes the waste gas inside through the filler, be provided with the second spray subassembly above the filler, add the absorbent in the second spray subassembly, realize carrying out great limited effective desorption to the impurity in the waste gas, the purification rate to the waste gas reaches more than 80%, the treatment through whirl spray washing tower body + spray absorption composite tower body makes the purification rate of waste gas reach more than 90%.
Compared with the prior art, the utility model has the beneficial effects that:
1. when the cyclone combined purification device is used, waste gas is conveyed to the cyclone spray washing tower body through the air inlet pipeline, impurities or larger particles in the waste gas are separated through the cyclone separator in the cyclone spray washing tower body, the waste gas enters the bottom of the spray absorption combined tower body through the first air pipe, the filler is arranged in the spray absorption combined tower body, the waste gas is adsorbed through the filler, and the adsorbed gas is sprayed through the filler, so that the combined purification rate of the spray washing tower and the spray absorption combined tower is ensured to be more than 90%;
2. according to the cyclone spray washing tower, during spray washing, waste gas enters an air inlet of the cyclone separator through an air inlet pipeline, so that the waste gas and impurities in the waste gas are effectively separated, the waste gas is discharged into the cyclone spray washing tower body through an outlet of the cyclone separator, the impurities are discharged through connection of the bottom of the cyclone separator and a first calandria, the discharged gas is purified again through spraying of a first spraying assembly, and the first spraying assembly is connected with a first water tank at the bottom of the cyclone spray washing tower body through a first circulating water pipe, so that circulating spraying is realized;
3. according to the utility model, gas purified by the cyclone spray washing tower body enters the bottom of the spray absorption composite tower body through the first air pipe, the filter plate is arranged in the spray absorption composite tower body, the gas is uniformly transferred into the filler through the filter plate, the filler is used for adsorbing impurities in the gas, the top of the spray absorption composite tower body is provided with the second spray assembly, the absorbent is added in the second spray assembly, and the absorbent is contacted with waste gas, so that the impurities in the gas are removed to a greater extent;
4. according to the utility model, the treated gas is transmitted into the filter device body through the second air pipe, activated carbon is filled in the filter device body, the effective absorption of impurities which are not adsorbed is realized through the activated carbon, the purified gas enters a pipeline through the third air pipe, a main fan is arranged at one side of the pipeline, and the main fan drives the extraction to realize the discharge of the gas by the pipeline;
drawings
Fig. 1 is a schematic perspective view of the present utility model.
Fig. 2 is a side view of fig. 1 in accordance with the present utility model.
Fig. 3 is a bottom schematic view of fig. 1 in accordance with the present utility model.
Fig. 4 is an internal structural view of the spray scrubber of fig. 1 in accordance with the present utility model.
Fig. 5 is an internal structural view of the spray absorption composite tower of fig. 1 in the present utility model.
Fig. 6 is a view showing the internal structure of the filter body of fig. 1 according to the present utility model.
In the figure: the cyclone spray washing tower comprises a 1-cyclone spray washing tower body, a 10-first spray assembly, a 11-cyclone separator, a 12-first filter plate, a 13-first water tank, a 14-first calandria, a 15-support frame, a 16-first circulating water pipe, a 17-first air pipe, a 18-splitter plate, a 2-spray absorption composite tower body, a 20-second spray assembly, a 21-filler, a 22-second filter plate, a 23-second water tank, a 24-second circulating water pipe, a 25-second air pipe, a 26-support frame, a 27-second calandria, a 3-filter device body, a 31-support frame, 32-activated carbon, a 33-third air pipe, a 4-pipeline, a 5-main fan and a 6-air inlet pipeline.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-6, in an embodiment of the present utility model, a cyclone type exhaust gas treatment tower includes a cyclone spray scrubber body 1; the bottom of the cyclone spray washing tower body 1 is provided with a supporting frame 15; the top of the cyclone spray washing tower body 1 is connected with the bottom of the spray absorption composite tower body 2 through a first air pipe 17; the top of the spray absorption composite tower body 2 is connected with the filter device body 3 through a second air pipe 25; one end of the filtering device body 3 far away from the spray absorption composite tower body 2 is connected with the output pipeline 4 through a third air pipe 33;
the cyclone spray washing tower body 1 is internally provided with a first spray assembly 10 which can comprise a plurality of nozzles; a cyclone 11 (a cyclone is a device for separating a gas-solid system or a liquid-solid system, which is commercially available from a tin-free city oil chemical plant limited company) is arranged below the first spray assembly 10; the air inlet pipe of the cyclone separator 11 is connected with an air inlet pipeline 6 for conveying waste gas; the air outlet pipe of the cyclone separator 11 is connected with a first air pipe 17 for conveying treated gas; the cyclone separator 11 is connected with a first calandria 14 arranged on the cyclone spray washing tower body 1 to receive larger solid impurities; a first filter plate 12 is arranged below the cyclone separator 11; the inner side of the bottom of the cyclone spray washing tower body 1 is provided with a first water tank 13; the first water tank 13 is connected with the first spray assembly 10 through a first circulating water pipe 16;
the top end of the inner part of the spray absorption composite tower body 2 is provided with a second spray assembly 20 which can be provided with a plurality of nozzles; a packing 21 (such as silica gel, alumina, zeolite molecular sieve and other adsorbents for gas) is arranged below the second spraying assembly 20; the filler 21 may be provided with multiple layers; a second filter plate 22 with a plurality of holes is arranged below the filler 21; a second water tank 23 is arranged between the second filter plate 22 and the bottom of the spray absorption composite tower body 2; the bottom of the spray absorption composite tower body 2 is provided with a second calandria 27; the outer side of the bottom of the spray absorption composite tower body 2 is provided with a bracket 26;
through adopting above-mentioned technical scheme, when using, carry waste gas to whirl spray washing tower body 1 through air inlet pipe 6, through the separation of the inside cyclone 11 realization impurity or the great granule in the waste gas of whirl spray washing tower body 1, waste gas gets into and sprays the compound tower body 2 bottom of absorption through first tuber pipe 17, be provided with packing 21 in spraying the inside of absorbing compound tower body 2, realize the absorption to waste gas impurity through packing 21, rethread second spray assembly 20 sprays the gas that the absorption was accomplished, guarantee to spray washing tower and spray the compound tower combination purification rate of absorbing more than 90%.
The spray absorption composite tower body 2 is provided with a filtering device body 3 at one side far away from the cyclone spray washing tower body 1; the filter device body 3 is internally provided with activated carbon 32; the outer side of the bottom of the filtering device body 3 is provided with a bracket 31; the filtering device body 3 is connected with the output pipeline 4 through a third air pipe 33 at one end far away from the second air pipe 25;
the bottom of the output pipeline 4 is provided with a support, and one side of the output pipeline 4 is provided with a main fan 5.
Through adopting above-mentioned technical scheme, when spraying the washing, waste gas passes through air inlet pipe 6 and gets into cyclone 11's air intake, realizes the effectual separation of gaseous and solid impurity in the waste gas, and the waste gas passes through cyclone 11's export and discharges to cyclone spray the washing tower body 1 inside, and impurity passes through cyclone 11 bottom and is connected realization to impurity of first calandria 14, and the gas that is discharged realizes purifying once more through the spraying of first spray assembly 10, and first spray assembly 10 passes through first circulating water pipe 16 and is connected with cyclone spray the first water tank 13 of washing tower body 1 bottom, realizes the circulation and sprays.
In this embodiment, the second water tank 23 is connected to the second spray assembly 20 through a second circulating water pipe 24.
Specifically, a diverter plate 18 for guiding the gas flow is arranged between the first filter plate 12 and the cyclone separator 11.
Through adopting above-mentioned technical scheme, the gas that the purification of spraying the washing tower body 1 is accomplished gets into and sprays the compound tower body 2 bottom through first tuber pipe 17, is provided with second filter 22 in spraying the inside of absorbing compound tower body 2, and gas passes through in the even transmission of second filter 22 to packing 21, realizes packing 21 adsorbs the impurity in the gas, is provided with second spraying assembly 20 at spraying the compound tower body 2 top of absorbing, and through spraying washing + spraying absorption complex guarantee to reach more than 90% to the purification rate of waste gas.
Still further, the gas after being treated is transmitted to the inside of the filtering device body 3 through the second air pipe 25, activated carbon 32 is filled in the filtering device body 3, the impurities which are not adsorbed are effectively absorbed through the activated carbon 32, the purified gas enters the output pipeline 4 through the third air pipe 33, a main fan 5 is arranged on one side of the output pipeline 4, and the main fan 5 drives the extraction to realize the discharge of the gas through the pipeline.
The working principle of the utility model is as follows: when the cyclone spraying and washing device is used, waste gas is conveyed to the cyclone spraying and washing tower body 1 through the air inlet pipeline 6, impurities or larger particles in the waste gas are separated through the cyclone separator 11 in the cyclone spraying and washing tower body 1, the waste gas enters the bottom of the spraying and absorbing composite tower body 2 through the first air pipe 17, the filler 21 is arranged in the spraying and absorbing composite tower body 2, the waste gas is adsorbed through the filler 21, and the adsorbed gas is sprayed through the filler 21, so that the combined purification rate of the spraying and washing tower and the spraying and absorbing composite tower is ensured to reach more than 90%;
during spray washing, waste gas enters an air inlet of a cyclone separator 11 through an air inlet pipeline 6, so that effective separation of impurities in the waste gas is realized, the waste gas is discharged into a cyclone spray washing tower body 1 through an outlet of the cyclone separator 11, the impurities are discharged through connection of the bottom of the cyclone separator 11 and a first calandria 14, the discharged gas is purified again through spraying of a first spray assembly 10, and the first spray assembly 10 is connected with a first water tank 13 at the bottom of the cyclone spray washing tower body 1 through a first circulating water pipe 16, so that circulating spraying is realized;
the gas purified by the cyclone spray washing tower body 1 enters the bottom of the spray absorption composite tower body 2 through the first air pipe 17, the second filter plate 22 is arranged in the spray absorption composite tower body 2, the gas is uniformly transferred into the filler 21 through the second filter plate 22, the filler 21 is used for adsorbing impurities in the gas, the second spray assembly 20 is arranged at the top of the spray absorption composite tower body 2, an absorbent can be added at the position of the second spray assembly 20, the absorbent is contacted with waste gas, the impurities in the gas are removed to a greater extent, and the purification rate of the waste gas is ensured to be more than 90% through spray washing and spray absorption composite;
the gas after being processed is transmitted to the inside of the filter device body 3 through the second air pipe 25, activated carbon 32 is filled in the filter device body 3, the impurities which are not adsorbed are effectively absorbed through the activated carbon 32, the gas after being purified enters the output pipeline 4 through the third air pipe 33, a main fan 5 is arranged on one side of the output pipeline 4, and the main fan 5 drives the extraction to realize the discharge of the gas through the pipeline.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present disclosure describes embodiments, not every embodiment is provided with a separate embodiment, and that this description is provided for clarity only, and that the disclosure is not limited to the embodiments described in detail below, and that the embodiments described in the examples may be combined as appropriate to form other embodiments that will be apparent to those skilled in the art.
Claims (6)
1. A spiral-flow type exhaust gas treatment tower, characterized in that: comprises a cyclone spray washing tower body (1); the bottom of the cyclone spray washing tower body (1) is provided with a supporting frame (15); the top of the cyclone spray washing tower body (1) is connected with the bottom of the spray absorption composite tower body (2) through a first air pipe (17); the top of the spray absorption composite tower body (2) is connected with the filtering device body (3) through a second air pipe (25); one end, far away from the spray absorption composite tower body (2), of the filtering device body (3) is connected with an output pipeline (4) through a third air pipe (33), and a main fan (5) is arranged on the side surface of the output pipeline (4);
a first spray assembly (10) is arranged in the cyclone spray washing tower body (1); a cyclone separator (11) is arranged below the first spraying assembly (10); an air inlet pipe of the cyclone separator (11) is connected with an air inlet pipeline (6); the air outlet pipe of the cyclone separator (11) is connected with a first air pipe (17); the cyclone separator (11) is connected with a first calandria (14) arranged on the cyclone spray washing tower body (1); a first filter plate (12) is arranged below the cyclone separator (11); a first water tank (13) is arranged on the inner side of the bottom of the cyclone spray washing tower body (1); the first water tank (13) is connected with the first spraying assembly (10) through a first circulating water pipe (16).
2. The cyclone exhaust gas treatment tower according to claim 1, wherein: the top end of the inner part of the spray absorption composite tower body (2) is provided with a second spray assembly (20); a filler (21) is arranged below the second spraying assembly (20); a second filter plate (22) is arranged below the filler (21); a second water tank (23) is arranged between the second filter plate (22) and the bottom of the spray absorption composite tower body (2); the bottom of the spray absorption composite tower body (2) is provided with a second calandria (27); and a supporting frame (26) is arranged on the outer side of the bottom of the spray absorption composite tower body (2).
3. The cyclone exhaust gas treatment tower according to claim 2, wherein: the spray absorption composite tower body (2) is provided with a filtering device body (3) at one side far away from the cyclone spray washing tower body (1); an activated carbon (32) is arranged in the filter device body (3); a bracket (31) is arranged at the outer side of the bottom of the filtering device body (3); the filter device body (3) is connected with the output pipeline (4) through a third air pipe (33) at one end far away from the second air pipe (25).
4. A spiral-flow flue gas treatment tower according to claim 3, wherein: the bottom of the output pipeline (4) is provided with a supporting piece.
5. The cyclone exhaust gas treatment tower according to claim 2, wherein: the second water tank (23) is connected with the second spraying assembly (20) through a second circulating water pipe (24).
6. The cyclone exhaust gas treatment tower according to claim 1, wherein: a splitter plate (18) is arranged between the first filter plate (12) and the cyclone separator (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322479096.1U CN220715284U (en) | 2023-09-12 | 2023-09-12 | Spiral-flow type exhaust-gas treatment tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322479096.1U CN220715284U (en) | 2023-09-12 | 2023-09-12 | Spiral-flow type exhaust-gas treatment tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220715284U true CN220715284U (en) | 2024-04-05 |
Family
ID=90487579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322479096.1U Active CN220715284U (en) | 2023-09-12 | 2023-09-12 | Spiral-flow type exhaust-gas treatment tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220715284U (en) |
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2023
- 2023-09-12 CN CN202322479096.1U patent/CN220715284U/en active Active
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