CN2635187Y - Large flux high efficiency cyclone plate tower desulfur dust eliminating device - Google Patents
Large flux high efficiency cyclone plate tower desulfur dust eliminating device Download PDFInfo
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- CN2635187Y CN2635187Y CN 03256144 CN03256144U CN2635187Y CN 2635187 Y CN2635187 Y CN 2635187Y CN 03256144 CN03256144 CN 03256144 CN 03256144 U CN03256144 U CN 03256144U CN 2635187 Y CN2635187 Y CN 2635187Y
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- rotating stream
- stream tray
- dust
- scrubber
- swirl vane
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Abstract
The utility model discloses a high-flux efficient rotating stream tray tower desulfuration and dedusting device, which comprises a water-film separator, and a multi-layer rotating stream tray tower in the cylinder which consists of a blind plate, a swirl blade which is closely connected with the blind plate and a ring bearer for fixing the swirl blade. On the ring bearer are provided a plurality of liquid leakage holes, the lower part of which are connected with the inclined downcomers. The ratio of the space area between the swirl blades to the sectional area of the cylinder is 20 to 50 percent, the swirl blades quantity of the rotating stream tray tower is 80 to 200 pieces, and the rotation angle between the swirl blades and the horizontal plane is 15 degrees to 50 degrees. The utility model can be applied to double-alkali method, lime/limestone method, alkaline waste method and the various desulfuration and dedusting processing, and the dedusting efficiency can reach 99.8 percent. The utility model can also be used for directly modifying the existing water-film separator device, without increasing the desulfurization absorbing towers, changing the cylinders, changing the fans and increasing the occupied areas, and improves the desulfuration and dedusting efficiency, saves the reformation investment and reduces the operating cost.
Description
Technical field
The utility model belongs to environmental protection and resource technical field, relates to a kind of desulfation dust-extraction device of prevention and control of air pollution.
Background technology
Dust arrester commonly used has mechanical collector, wet scrubber, filtration dust catcher and electric cleaner.The wet scrubber of imitating during water film dust removal device belongs to, main structure comprises cylindrical shell, spray equipment, demister etc., and efficiency of dust collection is 85-90%, and desulfuration efficiency only is 10-15%.Along with people to improving constantly that atmosphere quality requires, the control of sulfur dioxide is required also progressively to improve.At present, general on the basis of original dust arrester in order to control the discharge capacity of sulfur dioxide, add desulfurizer again thereafter, to reach the target of desulfurization and dedusting.
Though this technical method can reach the purpose of desulfurization and dedusting, newly-built absorption tower has increased floor space in order to desulfurization, is not suitable for the smaller situation in place, and must increase investment and operating cost.
The utility model patent of patent No. ZL98243156.2 discloses a kind of high-efficient desulfation dust-extraction device, this device includes a venturi water film dust arrester, also has a concentric circles water mist desulfurized dust collector, in the middle of this device is smoke-intake pipe, outer periphery several layers concentric drums, the top is provided with water injector, have smoke uptake at smoke-intake pipe and each layer concentric drums, the outlet flue of concentric drums is connected with the inlet flue duct of venturi water film dust arrester by a middle flue, is provided with the hydrolock overflow mechanism in the bottom of concentric circles water mist desulfurized dust collector.But its flux is little, thereby barrel diameter is big, and floor space is big, and having relatively high expectations to basic load-bearing.
The utility model patent of patent No. ZL01263901.X discloses a kind of whirlwind water film type desulfurizing dust-collector, and it comprises all parts such as desulfurization dust separation chamber, indoor spray head settling tank, administration liquid device, centrifuge dehumidifier.Bottom, desulfurization dust separation chamber is provided with spiral scroll casing shape smoke-intake pipe, it advances mouth and connects boiler boiler exhaust gas road, its outlet flue communicates with the desulfurization dust separation chamber, the above clean room's microbody inwall of spiral case smoke-intake pipe is welded with the polylith spiral deflector, spiral deflector is above to be fixed with the water film dedusting net near clean room's tube inwall, seedpod of the lotus shape shower nozzle has the nozzle of a plurality of sensing oblique uppers in the clean room, and the clean room establishes centrifuge dehumidifier in the top, and the clean room establishes primary sedimentation basin in the bottom.But its inner barrel complex structure, nozzle and filter screen all stop up easily.
Summary of the invention
The utility model provides a kind of big flux high-efficiency cyclone plate tower desulfurizing and dust removing unit, and water film dust removal device and desulfation dust-extraction device is integrated, improves desulfuration efficiency greatly, and further obviously improves efficiency of dust collection.
The technical method that the utility model rotating stream tray scrubber desulfation dust-extraction device is adopted is:
A kind of big flux high-efficiency cyclone plate tower desulfurizing and dust removing unit comprises water dust scrubber, and the inner barrel of water dust scrubber adds the multi-layer rotational flow column plate, rotating stream tray by blind plate, be close to the swirl vane of blind plate and fixedly the ring support of swirl vane form.
Described ring support is provided with several liquid-leaking nozzles, and the liquid-leaking nozzle below is connected with the downspout of inclination.
The ratio of interval area between the described swirl vane and cylindrical shell sectional area is 20-50%.
The swirl vane quantity of described rotating stream tray is the 8-200 sheet, and the anglec of rotation of swirl vane and horizontal plane is 15-50 °.
The utility model device can be used for various desulfurization dust-removing techniques such as two alkaline process, lime/lime stone method, alkaline waste method.
Generally, the empty tower gas velocity of common rotating stream tray scrubber is 2.5-3m/s, and adopts the empty tower gas velocity through improved rotating stream tray of the present utility model can be up to 3.1-6m/s.Gap between the swirl vane of rotating stream tray scrubber of the present utility model is bigger, and the ratio of interval area and cylindrical shell sectional area is up to 20-50%, thereby the assurance low pressure drop prevents that simultaneously column plate from stopping up; Adopt suitable swirl vane angle (15-50 °), guarantee the fully effect of atomizing, can make mist droplet granularity reach tens microns (common rotating stream tray scrubber droplet reaches the hundreds of micron), thereby guarantee high desulfurization dust-removing efficiency; Efficiency of dust collection of the present utility model can reach more than 99.8%, and desulfuration efficiency can reach 70-99%, and the pressure drop that increases (or claiming resistance drop) only is 500-1000Pa.
The utility model also can be used for transforming original water film dust removal device, need not increase and build desulfuration absorbing tower, not change water dust scrubber cylindrical shell, ventilating fan not, not increase floor space, only in tower, add rotating stream tray to increase the gas-liquid contact area, improve desulfurization dust-removing efficiency.The device internal structure is simple, less scaling, and investment for trnasforming urban land is little, and operating cost is low.
Description of drawings
Fig. 1 is a kind of embodiment structural representation of rotating stream tray scrubber desulfation dust-extraction device;
Fig. 2 is the rotating stream tray vertical view among Fig. 1;
Fig. 3 is the another kind of embodiment structural representation of rotating stream tray scrubber desulfation dust-extraction device.
The specific embodiment
As Fig. 1, Fig. 2, the sulfur-bearing ash-laden gas is entered in the water dust scrubber 2 by gas approach 1 by tangential direction, rotation is risen, rise through the multi-layer rotational flow column plate, column plate by blind plate 8, the anglec of rotation be 15-50 ° swirl vane 6 and fixedly the ring support 7 of swirl vane 6 form, size and treating capacity that swirl vane 6 is looked water dust scrubber 2 can be the 8-200 sheet, ring support 7 is fixed on Ta Bishang, support 7 is provided with several liquid-leaking nozzles 9, the hole that liquid-leaking nozzle (9) can adopt different shape.Flue gas is under the guide effect of swirl vane 6, and rotation is strengthened; Absorption liquid sprays from top to bottom by shower 5, the high velocity air that is risen after blind plate 8 zones in the middle of rotating stream tray evenly distribute is dispersed into drop, atomizing, be absorbed after sulfur in smoke and the droplet reaction, grit in the flue gas and droplet are under action of centrifugal force, be thrown toward the tower wall, grit in the flue gas is under action of centrifugal force, be thrown toward the tower wall, collision is fallen, the absorption liquid that gathers after dirty along the tower wall is dirty by liquid-leaking nozzle 9, is discharged by overfall 10 at last, enters ash settling basin, the gas of atomizing is through demister 4, discharges from exporting 3 after removing droplet.
As Fig. 3, liquid-leaking nozzle 9 belows of ring support 7 are connected with from the circumferential centroclinal downspout 11 of tower, and downspout (11) can adopt the pipe of different shape.Flue gas is under the guide effect of swirl vane 6, and rotation is strengthened; Absorption liquid sprays from top to bottom by shower 5, the high velocity air that is risen after blind plate 8 zones in the middle of rotating stream tray evenly distribute is dispersed into drop, atomizing, be absorbed after sulfur in smoke and the droplet reaction, grit in the flue gas and droplet are under action of centrifugal force, be thrown toward the tower wall, grit in the flue gas is under action of centrifugal force, be thrown toward the tower wall, collision is fallen, and the absorption liquid that gathers after Yan Tabi is dirty falls to entering down the blind plate district of one deck column plate by downspout 7, and absorption liquid absorbs repeatedly, discharge by overfall 11 at last, enter ash settling basin, the gas of atomizing is through demister 4, discharges from exporting 3 after removing droplet.
Handle by this device, efficiency of dust collection can reach 99.8%, and desulfuration efficiency can reach 99%.
Claims (6)
1. one kind big flux high-efficiency cyclone plate tower desulfurizing and dust removing unit, comprise water dust scrubber, it is characterized in that: the inner barrel of water dust scrubber adds the multi-layer rotational flow column plate, rotating stream tray by blind plate (8), be close to the swirl vane (6) of blind plate and fixedly the ring support (7) of swirl vane (6) form.
2. rotating stream tray scrubber desulfation dust-extraction device according to claim 1 is characterized in that: described ring support (7) is provided with several liquid-leaking nozzles (9).
3. rotating stream tray scrubber desulfation dust-extraction device according to claim 1 is characterized in that: described liquid-leaking nozzle (9) below is connected with the downspout (11) of inclination.
4. rotating stream tray scrubber desulfation dust-extraction device according to claim 1 and 2 is characterized in that: the interval area between the described swirl vane (6) and the ratio of cylindrical shell sectional area are 20-50%.
5. rotating stream tray scrubber desulfation dust-extraction device according to claim 1 and 2 is characterized in that: the swirl vane of described rotating stream tray (6) quantity is the 8-200 sheet.
6. rotating stream tray scrubber desulfation dust-extraction device according to claim 1 and 2 is characterized in that: described swirl vane (6) is 15-50 ° with the anglec of rotation of horizontal plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03256144 CN2635187Y (en) | 2003-07-28 | 2003-07-28 | Large flux high efficiency cyclone plate tower desulfur dust eliminating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03256144 CN2635187Y (en) | 2003-07-28 | 2003-07-28 | Large flux high efficiency cyclone plate tower desulfur dust eliminating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2635187Y true CN2635187Y (en) | 2004-08-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03256144 Expired - Lifetime CN2635187Y (en) | 2003-07-28 | 2003-07-28 | Large flux high efficiency cyclone plate tower desulfur dust eliminating device |
Country Status (1)
| Country | Link |
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| CN (1) | CN2635187Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502649A (en) * | 2011-09-28 | 2012-06-20 | 陆飞飞 | Heat and mass transfer device with rotational flow boards in process of producing polycrystalline silicon |
| CN102921288A (en) * | 2012-10-31 | 2013-02-13 | 浙江天蓝环保技术股份有限公司 | Y-shaped absorption tower and method for performing flue gas desulfurization by using Y-shaped absorption tower |
| CN103285702A (en) * | 2013-06-09 | 2013-09-11 | 史汉祥 | Dust removal mist purifier |
| CN107497249A (en) * | 2017-10-13 | 2017-12-22 | 山东佩森环保科技股份有限公司 | A kind of ship tail gas scrubbing tower |
| CN110530162A (en) * | 2018-07-13 | 2019-12-03 | 韶关市力高机械制造有限公司 | Dust pelletizing system applied to furnace cupola |
-
2003
- 2003-07-28 CN CN 03256144 patent/CN2635187Y/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102502649A (en) * | 2011-09-28 | 2012-06-20 | 陆飞飞 | Heat and mass transfer device with rotational flow boards in process of producing polycrystalline silicon |
| CN102502649B (en) * | 2011-09-28 | 2014-05-14 | 陆飞飞 | Heat and mass transfer device with rotational flow boards in process of producing polycrystalline silicon |
| CN102921288A (en) * | 2012-10-31 | 2013-02-13 | 浙江天蓝环保技术股份有限公司 | Y-shaped absorption tower and method for performing flue gas desulfurization by using Y-shaped absorption tower |
| CN102921288B (en) * | 2012-10-31 | 2014-07-16 | 浙江天蓝环保技术股份有限公司 | Y-shaped absorption tower and method for performing flue gas desulfurization by using Y-shaped absorption tower |
| CN103285702A (en) * | 2013-06-09 | 2013-09-11 | 史汉祥 | Dust removal mist purifier |
| CN103285702B (en) * | 2013-06-09 | 2015-03-25 | 宁波太极环保设备有限公司 | Dust removal mist purifier |
| CN107497249A (en) * | 2017-10-13 | 2017-12-22 | 山东佩森环保科技股份有限公司 | A kind of ship tail gas scrubbing tower |
| CN110530162A (en) * | 2018-07-13 | 2019-12-03 | 韶关市力高机械制造有限公司 | Dust pelletizing system applied to furnace cupola |
| CN110530162B (en) * | 2018-07-13 | 2024-04-16 | 韶关市力高机械制造有限公司 | Dust removing system applied to cupola furnace |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLO Free format text: FORMER OWNER: ZHEJIANG UNIVERSITY Effective date: 20110225 Free format text: FORMER OWNER: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. WU ZHONGBIAO |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| C56 | Change in the name or address of the patentee | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 310027 NO.38, ZHEDA ROAD, HANGZHOU CITY, ZHEJIANG PROVINCE TO: 311202 XINGYI VILLAGE, BEIGAN SUBDISTRICT, XIAOSHAN DISTRICT, HANGZHOU CITY, ZHEJIANG PROVINCE |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 310027 Hangzhou, Zhejiang Province, Zhejiang Road, No. 38 Co-patentee after: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Patentee after: ZHEJIANG University Co-patentee after: Wu Zhongbiao Address before: 310027 Hangzhou, Zhejiang Province, Zhejiang Road, No. 38 Co-patentee before: Zhejiang Tianlan Desulphurization & Dust-Removal Co.,Ltd. Patentee before: Zhejiang University Co-patentee before: Wu Zhongbiao |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110225 Address after: Hangzhou City, Zhejiang province Xiaoshan District 311202 North Street Xingyi Village Patentee after: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 310027 Hangzhou, Zhejiang Province, Zhejiang Road, No. 38 Co-patentee before: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Patentee before: Zhejiang University Co-patentee before: Wu Zhongbiao |
|
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang province Xiaoshan District 311202 North Street Xingyi Village Patentee after: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: Hangzhou City, Zhejiang province Xiaoshan District 311202 North Street Xingyi Village Patentee before: ZHEJIANG TIANLAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
|
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20130728 Granted publication date: 20040825 |