CN204034549U - A kind of equipment for denitrifying flue gas - Google Patents
A kind of equipment for denitrifying flue gas Download PDFInfo
- Publication number
- CN204034549U CN204034549U CN201420455764.5U CN201420455764U CN204034549U CN 204034549 U CN204034549 U CN 204034549U CN 201420455764 U CN201420455764 U CN 201420455764U CN 204034549 U CN204034549 U CN 204034549U
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- nozzle
- pipe
- flue gas
- air inlet
- inlet pipe
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Abstract
The utility model belongs to fume treatment technical field, specifically a kind of equipment for denitrifying flue gas.The utility model comprises tank used for storing ammonia, dilution water tank, mixing weighing module, atomizing steam air inlet pipe, dried compressed air inlet pipe and ammonia spray nozzle; Ammonia spray nozzle comprises pipe and nozzle outer tube in nozzle; The inlet communication of ammonium hydroxide delivery pump, dilution water conveying delivery side of pump and mixing weighing module, pipe in the outlet nozzle of mixing weighing module.In described nozzle, pipe is communicated with atomizing steam air inlet pipe; The compressed air control valve of cavity between nozzle outer tube with pipe in nozzle is communicated with dried compressed air inlet pipe.The utility model is mixed with ammoniacal liquor weak solution by atomizing steam, accomplishes ammonia atomization, improves the mixed effect of ammoniacal liquor weak solution and flue gas, and improve denitrating flue gas efficiency, denitration efficiency can reach more than 50%.In addition, the utility model is practical, and production cost is not high, and this product is adapted at promoting the use of in like product.
Description
Technical field
The utility model belongs to fume treatment technical field, specifically a kind of equipment for denitrifying flue gas.
Background technology
Chemism research shows: when good mixing, and the reaction of reducing agent and NOx substantially reached balanced reaction denitration rate and is greater than 90% in 0.3 second.Therefore, for practical application, mixing of reducing agent and flue gas is the core of SNCR technology.It is good that reducing agent mixes with flue gas, and just fully, system denitration rate is just high for chemical reaction, and it is just few that unreacted reducing agent leaks into the secondary pollution caused in air; Otherwise the difference that reducing agent mixes with flue gas, chemical reaction is just insufficient, and the denitration rate of system is just low, and it is just large that unreacted reducing agent leaks into the secondary pollution caused in air.
Utility model content
The purpose of this utility model is to solve deficiency of the prior art, provides a kind of equipment for denitrifying flue gas.
The utility model comprises tank used for storing ammonia, dilution water tank, mixing weighing module, atomizing steam air inlet pipe, dried compressed air inlet pipe and ammonia spray nozzle; Ammonia spray nozzle comprises pipe and nozzle outer tube in nozzle; The inlet communication of ammonium hydroxide delivery pump, dilution water conveying delivery side of pump and mixing weighing module, pipe in the outlet nozzle of mixing weighing module.
Preferably, in described nozzle, pipe is communicated with atomizing steam air inlet pipe; The compressed air control valve of cavity between nozzle outer tube with pipe in nozzle is communicated with dried compressed air inlet pipe.
Preferably, described dilution water delivery pump is arranged on the bottom of dilution water tank.
Preferably, described ammonia spray nozzle extend into the top of burner hearth, is provided with burner in burner hearth.
The utility model has the following advantages: mixed with ammoniacal liquor weak solution by atomizing steam, accomplish ammonia atomization, improves the mixed effect of ammoniacal liquor weak solution and flue gas, and improve denitrating flue gas efficiency, denitration efficiency can reach more than 50%; Nozzle arrangements is reasonable, and penetration performance is good, and reducing agent mixes with flue gas, passes into dry compressed air, can prevent spray nozzle clogging in nozzle between pipe, nozzle outer tube.In addition, the utility model is practical, and production cost is not high, and this product is adapted at promoting the use of in like product.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure, 1. tank used for storing ammonia; 2. dilute water tank; 3. mixing weighing module; 4. atomizing steam air inlet pipe; 5. dried compressed air inlet pipe; 6. ammonia spray nozzle; 7. ammonium hydroxide delivery pump; 8. dilution water delivery pump; 9. burner hearth.
Detailed description of the invention
For making the technical solution of the utility model and feature clearly, below in conjunction with embodiment, the utility model is described in further detail.At this, following examples for illustration of the utility model, but are not used for limiting scope of the present utility model.
As shown in Figure 1, the utility model comprises tank used for storing ammonia 1, dilution water tank 2, mixing weighing module 3, atomizing steam air inlet pipe 4, dried compressed air inlet pipe 5 and ammonia spray nozzle 6; Ammonia spray nozzle 6 comprises pipe and nozzle outer tube in nozzle; The outlet of ammonium hydroxide delivery pump 7, dilution water delivery pump 8 and the inlet communication of mixing weighing module 3, pipe in the outlet nozzle of mixing weighing module 3.
This structural design is key structure of the present utility model, effectively achieves flue gas desulfurization technique, and flue gas desulfurization is more thorough.
In nozzle of the present utility model, pipe is communicated with atomizing steam air inlet pipe 4; The compressed air control valve of cavity between nozzle outer tube with pipe in nozzle is communicated with dried compressed air inlet pipe.
Described dilution water delivery pump 8 is arranged on the bottom of dilution water tank.
The utility model ammonia spray nozzle 6 extend into the top of burner hearth 9, is provided with burner in burner hearth 9.
Obviously, above-described embodiment of the present utility model is only for the utility model example is clearly described, and is not the restriction to embodiment of the present utility model.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here cannot give exhaustive to all embodiments.Every belong to the technical solution of the utility model the apparent change of extending out or variation be still in the row of protection domain of the present utility model.
Claims (4)
1. an equipment for denitrifying flue gas, is characterized in that: described equipment for denitrifying flue gas comprises tank used for storing ammonia, dilution water tank, mixing weighing module, atomizing steam air inlet pipe, dried compressed air inlet pipe and ammonia spray nozzle; Ammonia spray nozzle comprises pipe and nozzle outer tube in nozzle; The inlet communication of ammonium hydroxide delivery pump, dilution water conveying delivery side of pump and mixing weighing module, pipe in the outlet nozzle of mixing weighing module.
2. a kind of equipment for denitrifying flue gas according to claim 1, is characterized in that: in described nozzle, pipe is communicated with atomizing steam air inlet pipe; The compressed air control valve of cavity between nozzle outer tube with pipe in nozzle is communicated with dried compressed air inlet pipe.
3. a kind of equipment for denitrifying flue gas according to claim 1, is characterized in that: described dilution water delivery pump is arranged on the bottom of dilution water tank.
4. a kind of equipment for denitrifying flue gas according to claim 1, is characterized in that: described ammonia spray nozzle extend into the top of burner hearth, is provided with burner in burner hearth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420455764.5U CN204034549U (en) | 2014-08-13 | 2014-08-13 | A kind of equipment for denitrifying flue gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420455764.5U CN204034549U (en) | 2014-08-13 | 2014-08-13 | A kind of equipment for denitrifying flue gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204034549U true CN204034549U (en) | 2014-12-24 |
Family
ID=52235259
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420455764.5U Expired - Fee Related CN204034549U (en) | 2014-08-13 | 2014-08-13 | A kind of equipment for denitrifying flue gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204034549U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051169A (en) * | 2017-04-07 | 2017-08-18 | 大唐环境产业集团股份有限公司 | A kind of SNCR denitration device |
| CN110404325A (en) * | 2019-08-25 | 2019-11-05 | 湖北强达环保科技股份有限公司 | Integrated conveying device based on out of stock waste water |
-
2014
- 2014-08-13 CN CN201420455764.5U patent/CN204034549U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051169A (en) * | 2017-04-07 | 2017-08-18 | 大唐环境产业集团股份有限公司 | A kind of SNCR denitration device |
| CN110404325A (en) * | 2019-08-25 | 2019-11-05 | 湖北强达环保科技股份有限公司 | Integrated conveying device based on out of stock waste water |
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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: 20141224 Termination date: 20180813 |