CN203710845U - Dust removal and desulfuration all-in-one washing tower - Google Patents
Dust removal and desulfuration all-in-one washing tower Download PDFInfo
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- CN203710845U CN203710845U CN201420105393.8U CN201420105393U CN203710845U CN 203710845 U CN203710845 U CN 203710845U CN 201420105393 U CN201420105393 U CN 201420105393U CN 203710845 U CN203710845 U CN 203710845U
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Abstract
The utility model relates to a dust removal and desulfuration all-in-one washing tower, and belongs to the technical field of dust removal and desulfuration washing towers. According to the technical scheme, a flue gas inlet (1) is formed in a tower body (8); a spraying layer (2), a defogging layer (5) and a flue gas outlet (9) are arranged in the tower body on the flue gas inlet in sequence; the spraying layer comprises a water feeding pipe (3) and an atomization nozzle (4); the water feeding pipe is communicated with the atomization nozzle; the defogging layer comprises a defogger (6) and a backwashing pipe (7); the backwashing pipe is communicated with the defogger; a water collection basin (10), an inclined plate sedimentation basin (11) and a pure water basin (14) are arranged below the flue gas inlet in sequence; the water collection basin is communicated with a calcium hydroxide solution feeding pipe (12); the inclined plate sedimentation basin is communicated with the pure water basin through a pure water backflow pipe; the pure water basin is communicated with the water feeding pipe of the spraying layer through a pipeline. Compared with the conventional cloth bag dust removal and electrostatic dust removal, the dust removal and desulfuration all-in-one washing tower has the advantage that dust removal and desulfuration can be realized; furthermore, the investment is small, the occupied space is small, the structure is simple, equipment is convenient to maintain, the cost is low, and the dust removal and desulfuration efficiency is high.
Description
Technical field
The utility model relates to a kind of dedusting and desulphurization integrated scrubbing tower, and the especially spray washing device of industrial circle dust-laden, sulfurous gas belongs to industrial circle dust-removal and desulfurizing scrubbing tower equipment technical field.
Background technology
At present, the discharge of industrial circle dust-laden, sulfurous gas is mainly that gas directly enters in atmosphere by chimney after bag-type dust or electrostatic precipitation, fine particle in gas is difficult for removing, and invest high, take up an area greatly, plant maintenance and operating cost are high, and especially existing dust collecting process cannot be removed the sulphur in waste gas, directly enter after atmosphere, cause air pollution.
Utility model content
The utility model object is to provide a kind of dedusting and desulphurization integrated scrubbing tower, can not only effectively remove the dirt in flue gas, and can effectively remove the sulphur in flue gas, solves the problem existing in background technology.
The technical solution of the utility model is:
A kind of dedusting and desulphurization integrated scrubbing tower, comprise smoke inlet, spraying layer, demist layer, tower body, exhanst gas outlet, collecting-tank, inclined-plate clarifying basin and clear water reserviors, tower body is provided with smoke inlet, above smoke inlet, in tower body, be provided with successively spraying layer, demist layer and exhanst gas outlet, described spraying layer comprises feed pipe and atomizer, feed pipe is communicated with atomizer, described demist layer comprises demister and backwash tube, backwash tube is communicated with demister, below smoke inlet, be provided with successively collecting-tank, inclined-plate clarifying basin and clear water reserviors, collecting-tank adds pipe to be communicated with aqua calcis, inclined-plate clarifying basin is communicated with by clear water return duct with clear water reserviors, clear water reserviors are communicated with the feed pipe of spraying layer by pipeline.
Described collecting-tank, inclined-plate clarifying basin and clear water reserviors are located in tower body, are positioned at below smoke inlet.
Described smoke inlet is located at tower body bottom, and collecting-tank, inclined-plate clarifying basin and clear water reserviors are located at tower body outside, and collecting-tank is communicated with tower body bottom by sewage return pipe, and collecting-tank is communicated with inclined-plate clarifying basin by sewage feed pipe.
The sewage feed pipe that described collecting-tank is communicated with inclined-plate clarifying basin is provided with sewage pump.
Described clear water reserviors are provided with feed pump with the pipeline that the feed pipe of spraying layer is communicated with.
Adopt the utility model, flue gas enters after tower body by smoke inlet, and the γ-ray emission convection current of the atomized water being sprayed by spraying layer and rising also fully contacts, the dust of carrying under one's arms in flue gas due to fully the contacting of water, and taken away by water, with the water (sewage) of dust, be collected together through collecting-tank, particle is effectively precipitated, precipitated by inclined-plate clarifying basin again, make sewage become clear water, enter clear water reserviors, recycle for spraying layer.For reaching better dust removing effects and preventing that water droplet from being taken out of outside tower by gas, demist layer is set above spraying layer, and flue gas is during by demist layer, and demister can effectively catch the water of carrying under one's arms in flue gas get off, thereby make flue gas become cleaner, the clean gas after washing enters atmosphere through exhanst gas outlet.If sulfur-bearing in gas, when spray, in water, add aqua calcis, sulphur in gas generally exists with sulfur dioxide form, sulfur dioxide contacts with water, can form sulfurous acid (or sulfuric acid), and sulfurous acid (or sulfuric acid) is understood rapidly and calcium hydroxide reaction generates calcium sulfite (or calcium sulfate), calcium sulfite (or calcium sulfate) can with together with dust in gas, precipitate through collecting-tank and inclined-plate clarifying basin, thereby the object of desulfurization when reaching dedusting.
The beneficial effects of the utility model are: good dedusting effect compared with traditional bag-type dust, electrostatic precipitation, can dedusting again can desulfurization, accomplish dedusting, desulfurization integrated, and invest low, take up an area little, simple in structure, plant maintenance is convenient, and cost is low, and dedusting, desulfuration efficiency are high.
Brief description of the drawings
Fig. 1 is the utility model embodiment mono-structural representation;
Fig. 2 is the utility model embodiment bis-structural representations;
In figure: smoke inlet 1, spraying layer 2, feed pipe 3, atomizer 4, demist layer 5, demister 6, backwash tube 7, tower body 8, exhanst gas outlet 9, collecting-tank 10, inclined-plate clarifying basin 11, aqua calcis add pipe 12, clear water return duct 13, clear water reserviors 14, feed pump 15, sewage return pipe 16, sewage pump 17, sewage feed pipe 18.
Detailed description of the invention
Below in conjunction with accompanying drawing, by example, the utility model is described in further detail.
Embodiment mono-
With reference to accompanying drawing 1, a kind of dedusting and desulphurization integrated scrubbing tower, comprise smoke inlet 1, spraying layer 2, demist layer 5, tower body 8, exhanst gas outlet 9, collecting-tank 10, inclined-plate clarifying basin 11 and clear water reserviors 14, tower body 8 is by stainless steel, straight carbon steel or concrete are made, tower body 8 diameters are according to the difference of gas flow and difference, tower body 8 is provided with smoke inlet 1, smoke inlet 1 is provided with spraying layer 2 in tower body above successively, demist layer 5 and exhanst gas outlet 9, described spraying layer 2 comprises feed pipe 3 and atomizer 4, feed pipe 3 is communicated with atomizer 4, described demist layer 5 comprises demister 6 and backwash tube 7, backwash tube 7 is communicated with demister 6, smoke inlet 1 is provided with collecting-tank 10 in tower body 8 below successively, inclined-plate clarifying basin 11 and clear water reserviors 14, collecting-tank 10 adopts eddy flow well construction, can make particle effectively precipitate, collecting-tank 10 adds pipe 12 to be communicated with aqua calcis, inclined-plate clarifying basin 11 is communicated with by clear water return duct 13 with clear water reserviors 14, clear water reserviors 14 are communicated with the feed pipe 3 of spraying layer 2 by pipeline, pipeline is provided with feed pump 15.
Embodiment bis-
What dedusting and desulphurization integrated scrubbing tower was different from embodiment mono-is that smoke inlet 1 is located at tower body 8 bottoms, collecting-tank 10, inclined-plate clarifying basin 11 and clear water reserviors 14 are located at tower body 8 outsides, collecting-tank 10 is communicated with tower body 8 bottoms by sewage return pipe 16, collecting-tank 10 is communicated with inclined-plate clarifying basin 11 by sewage feed pipe 18, and sewage feed pipe 18 is provided with sewage pump 17.
Claims (5)
1. a dedusting and desulphurization integrated scrubbing tower, it is characterized in that comprising smoke inlet (1), spraying layer (2), demist layer (5), tower body (8), exhanst gas outlet (9), collecting-tank (10), inclined-plate clarifying basin (11) and clear water reserviors (14), tower body (8) is provided with smoke inlet (1), smoke inlet (1) is provided with spraying layer (2) in tower body above successively, demist layer (5) and exhanst gas outlet (9), described spraying layer (2) comprises feed pipe (3) and atomizer (4), feed pipe (3) is communicated with atomizer (4), described demist layer (5) comprises demister (6) and backwash tube (7), backwash tube (7) is communicated with demister (6), smoke inlet (1) is provided with collecting-tank (10) below successively, inclined-plate clarifying basin (11) and clear water reserviors (14), collecting-tank (10) adds pipe (12) to be communicated with aqua calcis, inclined-plate clarifying basin (11) is communicated with by clear water return duct (13) with clear water reserviors (14), clear water reserviors (14) are communicated with the feed pipe (3) of spraying layer (2) by pipeline.
2. dedusting and desulphurization integrated scrubbing tower according to claim 1, is characterized in that described collecting-tank (10), inclined-plate clarifying basin (11) and clear water reserviors (14) are located in tower body (8), are positioned at smoke inlet (1) below.
3. dedusting and desulphurization integrated scrubbing tower according to claim 1, it is characterized in that described smoke inlet (1) is located at tower body (8) bottom, collecting-tank (10), inclined-plate clarifying basin (11) and clear water reserviors (14) are located at tower body (8) outside, collecting-tank (10) is communicated with tower body (8) bottom by sewage return pipe (16), and collecting-tank (10) is communicated with inclined-plate clarifying basin (11) by sewage feed pipe (18).
4. dedusting and desulphurization integrated scrubbing tower according to claim 3, is characterized in that the sewage feed pipe (18) that described collecting-tank (10) is communicated with inclined-plate clarifying basin (11) is provided with sewage pump (17).
5. dedusting and desulphurization integrated scrubbing tower according to claim 1, is characterized in that described clear water reserviors (14) are provided with feed pump (15) with the pipeline that the feed pipe (3) of spraying layer is communicated with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420105393.8U CN203710845U (en) | 2014-03-10 | 2014-03-10 | Dust removal and desulfuration all-in-one washing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420105393.8U CN203710845U (en) | 2014-03-10 | 2014-03-10 | Dust removal and desulfuration all-in-one washing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203710845U true CN203710845U (en) | 2014-07-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420105393.8U Expired - Fee Related CN203710845U (en) | 2014-03-10 | 2014-03-10 | Dust removal and desulfuration all-in-one washing tower |
Country Status (1)
| Country | Link |
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| CN (1) | CN203710845U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237630A (en) * | 2019-05-23 | 2019-09-17 | 武汉科技大学 | A kind of big liquid-gas ratio multilayer step dedusting demisting packed tower |
| CN110433594A (en) * | 2019-09-12 | 2019-11-12 | 佛山市顺德区东波环保设备有限公司 | A kind of desulphurization denitration environmental protection fume treatment reaction tower |
-
2014
- 2014-03-10 CN CN201420105393.8U patent/CN203710845U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237630A (en) * | 2019-05-23 | 2019-09-17 | 武汉科技大学 | A kind of big liquid-gas ratio multilayer step dedusting demisting packed tower |
| CN110433594A (en) * | 2019-09-12 | 2019-11-12 | 佛山市顺德区东波环保设备有限公司 | A kind of desulphurization denitration environmental protection fume treatment reaction tower |
| CN110433594B (en) * | 2019-09-12 | 2024-03-22 | 佛山市顺德区东波环保设备有限公司 | Desulfurization and denitrification reaction tower for environmental protection flue gas treatment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20140716 Termination date: 20190310 |