CN205965373U - Whirlwind dust removal wet desulfurization device - Google Patents
Whirlwind dust removal wet desulfurization device Download PDFInfo
- Publication number
- CN205965373U CN205965373U CN201620478659.2U CN201620478659U CN205965373U CN 205965373 U CN205965373 U CN 205965373U CN 201620478659 U CN201620478659 U CN 201620478659U CN 205965373 U CN205965373 U CN 205965373U
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- China
- Prior art keywords
- pond
- desulfurizer
- circulatory pool
- flue gas
- water pump
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Abstract
The utility model relates to a whirlwind dust removal wet desulfurization device, it includes desulphurization unit, cyclone, circulatory pool, the desulphurization unit bottom is equipped with flue gas inlet, flue gas inlet is connected with cyclone through flue gas pipeline, desulphurization unit still is equipped with the circulatory pool outward, the circulatory pool includes slurrying pond and water pump pond, the slurrying pond separates through the baffle with the water pump pond, highly being less than of baffle the height of circulatory pool, the slurrying pond is equipped with the agitator, be equipped with spray pump in the water pump pond, still be equipped with atomizing spraying system in the desulphurization unit, atomizing spraying system passes through the spray piping and connects spray pump, atomizing spraying system top still is equipped with the defogging device. The utility model discloses a cyclone purifies the ash -laden gas, has reduced the content of dust in the flue gas, has practiced thrift the also indirect desulfurization effect that has improved of doctor solution, has created the condition for the thorough dust removal of flue gas.
Description
Technical field
This utility model is related to a kind of dust-removing desulfurating apparatus, more particularly, to a kind of cyclone dust removal wet desulfurizer.
Background technology
With the development of Wet Flue Gas Desulfurization Technique, domestic flue gas desulfurization project is using alkaline process, the desulfurization skill of magnesium oxide method at present
Art gets more and more, and wet desulphurization device of the prior art adopts traditional interior circulation, and this method is in operation and there is operation
Trouble, doctor solution such as is difficult to be supplemented in time at the disadvantage, causes desulfurization not thorough；Additionally, wet method sulphur removing and dust removing is difficult to ensure that powder
The thorough removing of dirt, causes dedusting not thorough, affects atmospheric environment.
Utility model content
For the deficiencies in the prior art, this utility model provides a kind of desulfurization dust-removing efficiency height, has multiple dust removing effects
Cyclone dust removal wet desulfurizer.
This utility model solves its technical problem and be employed technical scheme comprise that：Described cyclone dust removal wet desulfurizer bag
Include desulfurizer, described desulfurizer bottom is provided with gas approach, and top is provided with exhanst gas outlet, described desulfurizer takes off for wet type
Sulfur dust arrester, the described gas approach of described desulfurizer is connected with cyclone dust extractor by flue, described fume pipe
Road is provided with air-introduced machine, is additionally provided with circulatory pool outside described desulfurizer, and described circulatory pool includes slurrying pond and water pump pond, described slurrying
Pond is separated by dividing plate with water pump pond, and the height of described dividing plate is less than the height of described circulatory pool, and described slurrying pond is provided with stirring
Device, is provided with feeding spraying pump in described water pump pond, is additionally provided with atomizing sprinkling system in described desulfurizer, described atomizing sprinkling system
Described feeding spraying pump is connected by spray piping, above described atomizing sprinkling system, is additionally provided with demister.
Compared with prior art, the beneficial effect of the cyclone dust removal wet desulfurizer that this utility model provides is：
First, using described cyclone dust extractor, ash-laden gas is purified, reduce the content of dust in flue gas, save
Doctor solution also indirectly improves desulfurized effect, is that the thorough dedusting of flue gas creates condition；
2nd, the described circulatory pool that described desulfurizer is externally provided with, by doctor solution by the way of outer circulation, reduces operation
Difficulty, improves desulfurization and dedusting effect.
Brief description
In order to be illustrated more clearly that the technical scheme in this utility model embodiment, below will be to required in embodiment description
Accompanying drawing to be used be briefly described it should be apparent that, drawings in the following description are only that of the present utility model some are real
Apply example, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to these accompanying drawings
Obtain other accompanying drawings, wherein：
Fig. 1 is the structural representation of the cyclone dust removal wet desulfurizer that this utility model provides.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely description is it is clear that described embodiment is only a part of embodiment of the present utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under the premise of making creative work
The all other embodiment being obtained, broadly falls into the scope of this utility model protection.
Refer to Fig. 1, be the structural representation of the cyclone dust removal wet desulfurizer that this utility model provides.
Described cyclone dust removal wet desulfurizer 1 includes desulfurizer 12, cyclone dust extractor 14, circulatory pool 16.
Described desulfurizer 12 is wet desulfurization dust-removing device, and its bottom is provided with gas approach 121, and top is provided with flue gas and goes out
Mouth 122, described cyclone dust extractor 14 connects the described gas approach 121 of described desulfurizer 12 by flue 10, described
Flue 10 is provided with air-introduced machine 101, and described circulatory pool 16 is outside described desulfurizer 12.
Described circulatory pool 16 includes slurrying pond 161 and water pump pond 162, and dividing plate is passed through in described slurrying pond 161 and water pump pond 162
163 separate, and the height of described dividing plate 163 is less than the height of described circulatory pool 16, and described slurrying pond 161 is provided with agitator 164, institute
State and in water pump pond 162, be provided with feeding spraying pump 165.
It is provided with atomizing sprinkling system 123, described atomizing sprinkling system 123 passes through spray piping in described desulfurizer 12
The 120 described feeding spraying pumps 165 of connection.
It is additionally provided with demister 124 above described atomizing sprinkling system 123.
When being embodied as, the dust in ash-laden gas is in the presence of the centrifugal force of described cyclone dust extractor 14 by dust exhausting hole
Discharge, the flue gas after purification introduces described desulfurizer 12 through described air-introduced machine 101, flue gas passes through described in uphill process
Atomizing sprinkling system 123 carries out desulphurization reaction, again dust is effectively removed simultaneously, then through described demister
124 removing water smokes are discharged by described exhanst gas outlet 122.The doctor solution that wherein said atomizing sprinkling system 123 adopts is using outer
Endless form supplies, and desulfurizing agent puts in described slurrying pond 161, is overflowed to described after described agitator 164 stirring and dissolving
In water pump pond 162, it is to avoid desulfurizing agent enters in described desulfurizer 12 and forms fouling.
Compared with prior art, the beneficial effect of the cyclone dust removal wet desulfurizer that this utility model provides is：
First, using described cyclone dust extractor 14, ash-laden gas is purified, reduce the content of dust in flue gas, save
Doctor solution also indirectly improves desulfurized effect, is the thorough dedusting of flue gas creates condition；
2nd, the described circulatory pool 16 that described desulfurizer 12 is externally provided with, by doctor solution by the way of outer circulation, reduces
Operation easier, improves desulfurization and dedusting effect.
The foregoing is only embodiment of the present utility model, not thereby limit the scope of the claims of the present utility model, every
The equivalent structure made using this utility model description or equivalent flow conversion, or directly or indirectly it is used in other phases
The technical field closed, is all included in the same manner within scope of patent protection of the present utility model.
Claims (1)
1. a kind of cyclone dust removal wet desulfurizer, including desulfurizer, described desulfurizer bottom is provided with gas approach, top
It is provided with exhanst gas outlet it is characterised in that described desulfurizer is wet desulfurization dust-removing device, the described flue gas of described desulfurizer
Import is connected with cyclone dust extractor by flue, and described flue is provided with air-introduced machine, is additionally provided with outside described desulfurizer
Circulatory pool, described circulatory pool includes slurrying pond and water pump pond, and described slurrying pond and water pump pond are separated by dividing plate, described dividing plate
Highly it is less than the height of described circulatory pool, described slurrying pond is provided with agitator, is provided with feeding spraying pump in described water pump pond, described de-
It is additionally provided with atomizing sprinkling system, described atomizing sprinkling system connects described feeding spraying pump by spray piping, described in sulfur device
It is additionally provided with demister above atomizing sprinkling system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620478659.2U CN205965373U (en) | 2016-05-24 | 2016-05-24 | Whirlwind dust removal wet desulfurization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620478659.2U CN205965373U (en) | 2016-05-24 | 2016-05-24 | Whirlwind dust removal wet desulfurization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205965373U true CN205965373U (en) | 2017-02-22 |
Family
ID=58019784
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620478659.2U Expired - Fee Related CN205965373U (en) | 2016-05-24 | 2016-05-24 | Whirlwind dust removal wet desulfurization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205965373U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362646A (en) * | 2017-09-01 | 2017-11-21 | 南京中电环保工程有限公司 | A kind of water mist dust-removing system |
-
2016
- 2016-05-24 CN CN201620478659.2U patent/CN205965373U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362646A (en) * | 2017-09-01 | 2017-11-21 | 南京中电环保工程有限公司 | A kind of water mist dust-removing system |
| CN107362646B (en) * | 2017-09-01 | 2021-04-20 | 南京中电环保固废资源有限公司 | Water smoke dust pelletizing system |
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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: 20170222 Termination date: 20170524 |