CN201454332U - High-efficiency dust-removing chamber in desulfurizing equipment - Google Patents
High-efficiency dust-removing chamber in desulfurizing equipment Download PDFInfo
- Publication number
- CN201454332U CN201454332U CN2009201244722U CN200920124472U CN201454332U CN 201454332 U CN201454332 U CN 201454332U CN 2009201244722 U CN2009201244722 U CN 2009201244722U CN 200920124472 U CN200920124472 U CN 200920124472U CN 201454332 U CN201454332 U CN 201454332U
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- waste gas
- chamber
- dust
- chamber body
- access port
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- Separation Of Particles Using Liquids (AREA)
Abstract
The utility model relates to a high-efficiency dust-removing chamber in desulfurizing equipment, comprising a chamber body; the chamber body is provided with a waste gas access port and a waste gas exhaust port which are respectively arranged at two sides of the chamber body; the top part of the chamber body between the waste gas access port and the waste gas exhaust port is provided with a spraying device which comprises a high-pressure liquid chamber and a collision-type nozzle oppositely arranged on the high-pressure liquid chamber; and the width of the spraying device is larger than that of the waste gas access port and the waste gas exhaust port. The high-efficiency dust-removing chamber overcomes the defects the in the prior art, desulfurization and dust removing are carried out on the boiler waste gas simultaneously in a desulfurizing tower, the dust-removing efficiency is low, the phenomena of scaling and blocking of the desulfurizing tower are easy to occur, and the service life of the desulfurizing tower is seriously influenced; and by the design, the dust removing is carried out on the waste gas from top to bottom by highly-atomized water drops, thus greatly improving dust-removing efficiency, reducing the consumption of electric energy and prolonging the service life of the desulfurizing tower. The high-efficiency dust-removing chamber has the advantages of simple structure, hard scaling in the dust-removing chamber, little resistance of waste gas flowing and strong reliability.
Description
Technical field
The utility model relates to the high-effective dust-removing chamber in a kind of desulphurization plant.
Background technology
Boiler is at essential heating equipments in field such as industrial production, service, medical treatment, because boiler can produce the waste gas of a large amount of sulfur-bearings when burning, is the environmental protection purpose, and above-mentioned waste gas must carry out desulfurization and handle before discharging.Desulfurization is handled and generally to be carried out in desulfurizing tower, desulfurizing tower in desulfurization, the dedusting of also spraying water, this structural design is stopped up the easy fouling of desulfurizing tower, has a strong impact on the service life of desulfurizing tower.
Summary of the invention
Boiler waste gas carries out desulfurization and dust removal process simultaneously in the prior art in desulfurizing tower in order to overcome, its efficiency of dust collection lowly, easily causes the desulfurizing tower fouling to be stopped up, have a strong impact on the desulfurizing tower problem in service life, the utility model provides the chamber of the high-effective dust-removing in a kind of desulphurization plant, the high-effective dust-removing chamber in this desulphurization plant simple in structure, efficiency of dust collection is high, less scaling, little, the energy saving of exhaust-gas flow resistance.
The technical scheme that its technical problem that solves the utility model adopts is: comprise the chamber body, on the body of chamber, be provided with waste gas access port and outlet port, waste gas access port and outlet port branch are located at body both sides, chamber, and the body top, chamber between waste gas access port and outlet port is provided with spray equipment.
Sprayer unit comprises the collision type nozzle that is oppositely arranged on high pressure liquid chamber and the high pressure liquid chamber.
Waste gas access port and outlet port are provided with between two parties along the width of chamber body, and the width of chamber body is greater than the width of waste gas access port and outlet port.
Sprayer unit is arranged on body top, chamber with the width that approaches the chamber body, the collision type nozzle tape angle design that is oppositely arranged in the sprayer unit, and its atomizing width is greater than the width of waste gas access port and outlet port.
The utility model is by above-mentioned specific design, waste gas advances in dirt pocket and by the globule dedusting from top to bottom of high atomisation, improved efficiency of dust collection greatly, reduced power consumption, prolonged the service life of desulfurizing tower, have less scaling in simple in structure, the dirt pocket, the exhaust-gas flow resistance is little, the advantage of good reliability.
Description of drawings
Below in conjunction with drawings and Examples detailed content of the present utility model is described.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the plan structure schematic diagram of Fig. 1;
Fig. 3 is a collision type structure of nozzle schematic diagram.
The specific embodiment
As shown in the figure; the utility model comprises chamber body 1; on chamber body 1, be provided with waste gas access port 2 and outlet port 3; waste gas access port 2 and outlet port were located at chamber body 1 both sides in 3 minutes; outlet port 3 tangentially inserts desulfurizing tower 7. waste gas access ports 2 and outlet port 3 and is provided with between two parties along the width of chamber body 1; the width of chamber body 1 is greater than the width of waste gas access port 2 and outlet port 3; waste gas passes through from dirt pocket along straight line or camber line; the flow resistance of waste gas is less; reduced power consumption. chamber body 1 top between waste gas access port 2 and outlet port 3 is provided with sprayer unit 4; sprayer unit 4 comprises the collision type nozzle 5 that is oppositely arranged on high pressure liquid chamber 6 and the high pressure liquid chamber 6; highly pressurised liquid sprays the collision of liquid liquid with identical pressure from relative nozzle; has extremely strong atomizing effect; improved efficiency of dust collection; having desulfidation simultaneously concurrently. sprayer unit 4 is arranged on chamber body 1 top with the width that approaches chamber body 1; the collision type nozzle 5 band angle design that are oppositely arranged in the sprayer unit 4; its atomizing width is greater than the width of waste gas access port 2 and outlet port 3; this design; make waste gas from dirt pocket by the time because the effect of atomizing water curtain can not contact the locular wall of dirt pocket; therefore also less scaling in the dirt pocket. above-described embodiment only is that the preferred implementation to the high-effective dust-removing chamber in the utility model desulphurization plant is described; be not that design and scope to utility model limits; under the prerequisite that does not break away from the utility model scheme; various external form modification and improvement that those skilled in the art make the technical solution of the utility model all should fall into the protection domain of the high-effective dust-removing chamber of the utility model desulphurization plant.
Claims (4)
1. the high-effective dust-removing chamber in the desulphurization plant, comprise the chamber body, on the body of chamber, be provided with waste gas access port and outlet port, it is characterized in that waste gas access port (2) and outlet port (3) branch is located at chamber body (1) both sides, chamber body (1) top between waste gas access port (2) and outlet port (3) is provided with sprayer unit (4).
2. the high-effective dust-removing chamber in the desulphurization plant according to claim 1 is characterized in that sprayer unit (4) comprises the collision type nozzle (5) that is oppositely arranged on high pressure liquid chamber (6) and the high pressure liquid chamber (6).
3. the high-effective dust-removing chamber in the desulphurization plant according to claim 1 and 2, it is characterized in that waste gas access port (2) and outlet port (3) are provided with between two parties along the width of chamber body (1), the width of chamber body (1) is greater than the width of waste gas access port (2) and outlet port (3).
4. the high-effective dust-removing chamber in the desulphurization plant according to claim 3, it is characterized in that sprayer unit (4) is arranged on chamber body (1) top with the width that approaches chamber body (1), collision type nozzle (5) the band angle design that is oppositely arranged in the sprayer unit (4), its atomizing width is greater than the width of waste gas access port (2) and outlet port (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201244722U CN201454332U (en) | 2009-07-11 | 2009-07-11 | High-efficiency dust-removing chamber in desulfurizing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201244722U CN201454332U (en) | 2009-07-11 | 2009-07-11 | High-efficiency dust-removing chamber in desulfurizing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201454332U true CN201454332U (en) | 2010-05-12 |
Family
ID=42381676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201244722U Expired - Fee Related CN201454332U (en) | 2009-07-11 | 2009-07-11 | High-efficiency dust-removing chamber in desulfurizing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201454332U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102512894A (en) * | 2011-12-29 | 2012-06-27 | 绍兴文理学院 | Spray-method setting machine waste gas and dust cleaning device and method thereof |
| CN102512900A (en) * | 2011-12-29 | 2012-06-27 | 绍兴文理学院 | Setting machine waste gas treatment method |
| CN104368204A (en) * | 2014-10-29 | 2015-02-25 | 苏州盟通利机电设备有限公司 | Water spraying device for air purifier |
| CN104383772A (en) * | 2014-10-29 | 2015-03-04 | 苏州盟通利机电设备有限公司 | Washing and filtering air purifier |
-
2009
- 2009-07-11 CN CN2009201244722U patent/CN201454332U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102512894A (en) * | 2011-12-29 | 2012-06-27 | 绍兴文理学院 | Spray-method setting machine waste gas and dust cleaning device and method thereof |
| CN102512900A (en) * | 2011-12-29 | 2012-06-27 | 绍兴文理学院 | Setting machine waste gas treatment method |
| CN104368204A (en) * | 2014-10-29 | 2015-02-25 | 苏州盟通利机电设备有限公司 | Water spraying device for air purifier |
| CN104383772A (en) * | 2014-10-29 | 2015-03-04 | 苏州盟通利机电设备有限公司 | Washing and filtering air purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100512 Termination date: 20120711 |