CN2693335Y - Poly-swash type desulfurization dust separator - Google Patents
Poly-swash type desulfurization dust separator Download PDFInfo
- Publication number
- CN2693335Y CN2693335Y CN 200420031426 CN200420031426U CN2693335Y CN 2693335 Y CN2693335 Y CN 2693335Y CN 200420031426 CN200420031426 CN 200420031426 CN 200420031426 U CN200420031426 U CN 200420031426U CN 2693335 Y CN2693335 Y CN 2693335Y
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- flue gas
- water
- plate
- guiding plate
- particles
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Abstract
The utility model discloses a poly-swash type desulfurization dust separator, belonging to the design and manufacture technical field of boiler dust-separating equipments. The poly-swash type desulfurization dust separator is cube-shaped. A circumferential baffle, inside which a decline air-guiding plate is provided, is arranged inside a box; an intermediate spacing plate is provided between the decline air-guiding plate and the circumferential baffle. The decline air-guiding plate and the spacing plate are all provided with edge folds forming included angles. While in use, the utility model is seated above a water storage tank. Entering from a flue gas inlet, flue gas directly impacts the oblique plane of the air-guiding plate, turning to downward impact the water surface of the water storage tank, water drops and foams being blown to rise up, and a majority of particles in the flue gas being caught to fall into the water; then, the flue gas continues to move to impact the oblique plane of the spacing plate, turning to downward move to impact the water surface, and a part of the particles in the flue gas being caught to fall into the water; the impaction being repeated, the particles in the flue gas are caught for multiple times, the flue gas coming up to the exhaust standard. The utility model is provided with simple structure and professional design. Due to the edge fold angles of the air-guiding plate and the spacing plate, the moving speed of the flue gas is expedited, and the flue gas is provided with great strength of the impaction to the water, the effect of the catching of the particles in the flue gas being good.
Description
Technical field
What the utility model was announced is the device that is used for smoke elimination, dedusting and the desulfurization of coal-burning boiler and Industrial Stoves discharging flue gas.Can with 1～40 ton of supporting use of various boiler.
Background technology
At present, at the flue gas desulfurization and dedusting equipment that is used for medium small boiler self-excitation Swashing type, whirlwind water film type, spray washing formula etc. are arranged.These several equipment are in operation and have drawback in varying degrees.The mass transfer that equipment operation is general to be relied on pump to circulate to carry out gas, liquid mixes, and just with pump the water ejection is gone, and catches dust granule in the flue gas by the water droplet of whereabouts and fog.Because work under bad environment, the obstruction of dust and the corrosiveness of sulphur make equipment very easily impaired." S " plate place of auto-excitation type because passage is narrow, very easily results in blockage for another example, influences the work effect.So these equipment are not very desirable.
Summary of the invention
The purpose of this utility model provides a kind of difficult obstruction and corrosive wear equipment, and reliable desulfurizing dust-collector is to overcome the practical problem that existing product exists.
Structure of the present utility model is as shown in drawings: casing is a cube.In casing one side into mouth is arranged, advancing in correspondence on the cabinet wall of mouth has a coaming plate.Deflector and central dividing plate have a down dip in coaming plate.Having a down dip has flanging on deflector and the central dividing plate, forms angle with deflector and dividing plate.One terrace with edge shape box cover is arranged at casing top.One outlet flue is arranged in the middle of the box cover.The use of this product is that it is located on the storage cistern.Storage cistern can be used cement masonry.The method of work and the process of this product are: after ash-laden gas is in air inlet enters into the deduster casing, because flue gas self has kinetic energy, directly impact the deflector inclined-plane that has a down dip, and turn to downward operation impulse to the storage cistern water surface, liquid level is blown afloat water droplet and the foam that splashes.At this moment water droplet that most of particle just falls into the water or quilt is splashed in the flue gas and foam are caught and are fallen into the water.Flue gas continues the inclined-plane that operation impacts dividing plate again, and the operation downwards that turns again impacts the water surface again, again a part of particle in the flue gas is stayed in the water, evokes water droplet and foam and catches the part particle.The water droplet that sticks on the dividing plate falls into storage cistern with gravity.Flue gas continues operation again and impacts the coaming plate front again, still changes to be directed downwards operation, repeats preceding secondary action again.Dust is captured to fall into the water.Flue gas through upwards operation of casing, is walked around the V-arrangement baffle plate and is discharged from outlet flue at last.In discharge process, some grit is attracted on the cabinet wall again, falls into storage cistern again.The utility model is simple in structure, and is reasonable in design, is to utilize the flue gas self kinetic energy, finishes gas cleaning by repeatedly impacting the water surface.Flue gas is repeatedly mixed with water contact, repeatedly catch grit in the flue gas.In addition,, the flue gas operation is put more effort, impact water surface great efforts, flue gas is contacted with the water mixing owing to the angle that the flanging of have a down dip deflector and central dividing plate forms.The dust removing effects ideal reaches discharge standard fully.
Description of drawings
Accompanying drawing is the utility model structural representation
1-casing 2-advances the mouth 3-deflector 4-central dividing plate 5-coaming plate 6-terrace with edge shape box cover 7-V shape baffle plate 8-outlet flue 9-angle bar base that has a down dip
Arrow is the flue gas traffic direction
The specific embodiment
Structure of the present utility model is as shown in drawings: casing (1) is a cube, has angle bar base (9) at bottom half.Base is welded on bottom half.In casing one side into mouth (2) is arranged.Enter the mouth place in the cabinet wall correspondence one coaming plate (5) is arranged.The coaming plate periphery is welded on the cabinet wall.One deflector (3) that has a down dip is arranged in coaming plate.One flanging is arranged at the deflector bottom, and flanging and deflector are 90 ° of angles.Deflector and coaming plate loam cake are 70～80 ° of angles.Have a down dip a central dividing plate (4) is arranged between deflector and the coaming plate.One flanging is arranged at central dividing plate top, and flanging and central dividing plate are 130 ° of angles.Have a down dip deflector and central dividing plate periphery is welded on coaming plate and the cabinet wall.One terrace with edge shape Box Cover (6) is arranged on casing top.One air outlet (8) is arranged in the middle of the Box Cover top.One V-arrangement baffle plate (7) is arranged in Box Cover.V-arrangement baffle plate two ends are fixed on the cabinet wall.
Claims (3)
1, many impact desulfurations deduster, it is characterized in that casing (1) inwall correspondence enters the mouth place one coaming plate (5) is arranged, one deflector (3) that has a down dip is arranged in coaming plate, and having a down dip has a central dividing plate (4) between deflector and the coaming plate, a V-arrangement baffle plate (7) is arranged in terrace with edge shape Box Cover.
2, deduster according to claim 1 is characterized in that a flanging is arranged at the said deflector bottom that has a down dip, and flanging and deflector are 90 ° of angles, and deflector and coaming plate loam cake are 70～80 ° of angles.
3, deduster according to claim 1 is characterized in that a flanging is arranged at central dividing plate top, and flanging and dividing plate are 130 ° of angles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420031426 CN2693335Y (en) | 2004-04-30 | 2004-04-30 | Poly-swash type desulfurization dust separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420031426 CN2693335Y (en) | 2004-04-30 | 2004-04-30 | Poly-swash type desulfurization dust separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2693335Y true CN2693335Y (en) | 2005-04-20 |
Family
ID=34772437
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420031426 Expired - Fee Related CN2693335Y (en) | 2004-04-30 | 2004-04-30 | Poly-swash type desulfurization dust separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2693335Y (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101920160A (en) * | 2010-09-25 | 2010-12-22 | 山西新聚星锅炉有限公司 | Impact desulfuration dust collection device |
| CN102179123A (en) * | 2011-05-12 | 2011-09-14 | 卓卫民 | Gas-liquid exchange device based on gas throttling |
| CN101450292B (en) * | 2008-12-05 | 2011-10-05 | 卓卫民 | Gas-liquid alternation method and device |
| CN105498496A (en) * | 2015-12-31 | 2016-04-20 | 王建华 | Waste gas purification system |
| CN106345231A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Intelligent waste gas treatment device for preparation of carbon nanotube |
| CN106345230A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Waste gas treatment device for production of carbon nanotube |
| CN106617259A (en) * | 2017-02-22 | 2017-05-10 | 广东中烟工业有限责任公司 | Dust-removal and fire-retardance device of negative-pressure pipeline |
| CN107875775A (en) * | 2017-12-13 | 2018-04-06 | 宜兴市江华环保科技有限公司 | A kind of high-temperature vacuum wet dust collector |
| CN108568176A (en) * | 2018-05-16 | 2018-09-25 | 乐清市德亮抛光设备有限公司 | A kind of dust-extraction unit |
| CN114405239A (en) * | 2022-03-28 | 2022-04-29 | 浙江百能科技有限公司 | Wet-type waste gas treatment device |
| CN115282713A (en) * | 2022-09-05 | 2022-11-04 | 辽宁欣海弘业航空科技有限公司 | Dust pelletizing system in workshop of polishing |
-
2004
- 2004-04-30 CN CN 200420031426 patent/CN2693335Y/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101450292B (en) * | 2008-12-05 | 2011-10-05 | 卓卫民 | Gas-liquid alternation method and device |
| CN101920160A (en) * | 2010-09-25 | 2010-12-22 | 山西新聚星锅炉有限公司 | Impact desulfuration dust collection device |
| CN102179123A (en) * | 2011-05-12 | 2011-09-14 | 卓卫民 | Gas-liquid exchange device based on gas throttling |
| CN102179123B (en) * | 2011-05-12 | 2013-06-19 | 卓卫民 | Gas-liquid exchange device based on gas throttling |
| CN105498496A (en) * | 2015-12-31 | 2016-04-20 | 王建华 | Waste gas purification system |
| CN105498496B (en) * | 2015-12-31 | 2017-12-26 | 王建华 | Waste gas cleaning system |
| CN106345230A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Waste gas treatment device for production of carbon nanotube |
| CN106345231A (en) * | 2016-08-31 | 2017-01-25 | 无锡东恒新能源科技有限公司 | Intelligent waste gas treatment device for preparation of carbon nanotube |
| CN106617259A (en) * | 2017-02-22 | 2017-05-10 | 广东中烟工业有限责任公司 | Dust-removal and fire-retardance device of negative-pressure pipeline |
| CN107875775A (en) * | 2017-12-13 | 2018-04-06 | 宜兴市江华环保科技有限公司 | A kind of high-temperature vacuum wet dust collector |
| CN108568176A (en) * | 2018-05-16 | 2018-09-25 | 乐清市德亮抛光设备有限公司 | A kind of dust-extraction unit |
| CN114405239A (en) * | 2022-03-28 | 2022-04-29 | 浙江百能科技有限公司 | Wet-type waste gas treatment device |
| CN115282713A (en) * | 2022-09-05 | 2022-11-04 | 辽宁欣海弘业航空科技有限公司 | Dust pelletizing system in workshop of polishing |
| CN115282713B (en) * | 2022-09-05 | 2024-03-26 | 辽宁欣海弘业航空科技有限公司 | Dust pelletizing system in workshop polishes |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |