CN1308982A - Comprehensive duster able to remove SO2 - Google Patents
Comprehensive duster able to remove SO2 Download PDFInfo
- Publication number
- CN1308982A CN1308982A CN 00102517 CN00102517A CN1308982A CN 1308982 A CN1308982 A CN 1308982A CN 00102517 CN00102517 CN 00102517 CN 00102517 A CN00102517 A CN 00102517A CN 1308982 A CN1308982 A CN 1308982A
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- water
- deduster
- gas
- air
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Abstract
A comprehensive duster able to remove SO2 is composed of a water tank, a duster unit, a draught, an air sucking cap, a water pump, a filter pool and and a water pool, and features that the substances able to react with SO2 or absorb SO2 are added to water and filter layer. Under action of the draught fan and water pump, the dust-containing gas passes through venturi, water membrane, water beating, cyclone and foam duster unit to remove SO2 and dust. Its advantages is high effect on removing dust and SO2.
Description
The invention belongs to the technical field that purifies air, more precisely is to remove SO
2Deduster makes it to be up to state standards.
Belong to big flow or high temperature and remove SO
2Deduster uses sack cleaner or electromagnetism deduster to stop up easily, also easy scaling loss when using high temperature, and the life-span of deduster also is difficult to guarantee.When using the stove deduster, the SO of furnace gas
2Also be difficult to remove.The object of the invention provides a cover dust pelletizing system, can effectively remove various furnace cupolas, boiler, kiln, the dust SO of discharge
2Reach the dust that national secondary discharge standard and other various forms produce and reach national grade ii standard.The name of this deduster claims Wen Shi comprehensively to remove SO
2Deduster.
Wen Shi comprehensively removes SO
2Deduster is made up of water tank (1) deduster (2) ventilation blower (3) clarifier (4) air draught cap (24) water pump (5) filtering ponds (6) ponds (7), Wen Shi comprehensive dust remover dust and SO under the negative pressure of air-introduced machine (3) and water-aspirator pressure effect shown in figure one
2Sucked through Wen Shi jet pipe (10) by the mouth of pipe (8), shower water is supplied with by nozzle (9), and the dust aqueous mixtures sprays into control (11) and carries out water attack, and most of dust enters in the water tank water, all the other dust SO
2And gas, making gas produce rotation, make the centrifugal deduster inwall that is attached to of part dust generation be poured water tank by impeller (12), gas enters filter course (13) again, produces foam at filter course, makes the thin dirt of the overwhelming majority be removed SO
2Gas fully contacts the overwhelming majority with water and is absorbed and produces and react the generation novel substance and poured water tank by shower (14) with medium in filter course.Gas is under the suction function of air-introduced machine (3), enter the upper box of deduster (2), the moisture film that breaks through nozzle (15) enters impeller (16), impeller (16) produces rotation gas, carry out centrifugal dust-removing in pipe (17), enter air-introduced machine (3), air-introduced machine (3) is discharged gas and is entered upward inner chamber of clarifier (4), running water and rotation gas are mixed into filter course (19), further remove dust and SO in filter course
2Superfluous water flows to the pond by the clarifier bottom.The residue aqueous vapor makes gas produce centrifugal force through impeller (20), water is separated dirty, clean gas enters air-breathing cap (23) by pipeline, upper flange (2), (3) are managed (4) up and down down, (5) are formed by blade (1) shown in figure (two), blade (1) produces eddy current and produces suction to discharging gas under the effect of upper air current, the end opening of deduster (2) is to be sealed by water tank (1).The superfluous water of water tank is to have casual water pipe (22) to flow out, and is filtered by filtering ponds (6) and flows into pond (7), and water pump is drawn into deduster (2) to water from the pond in (7) and uses.
For the corrosion the present invention who prevents the deduster inwall scribbles anti-corrosion material at deduster, water tank, clarifier pipeline, ventilation blower inwall, to prolong the life-span of deduster.
The present invention has adopted multistage dedusting method in order to make dust-exhausting quantity reach national dust discharge secondary standard.
The present invention stops up in order to prevent deduster, adopts continuous dedusting method.
The present invention is in order to make SO
2Discharge capacity is up to state standards and does not produce pollution, puts into to absorb SO in filtering material and in the water
2, and can not produce the secondary pollution material with the sulfur dioxide reaction.
Claims (4)
- Deduster1, a kind of Wen Shi comprehensively removes SO 2, shown in figure one, it is characterized in that whole system is by water tank (1) deduster (2) ventilation blower (3) clarifier (4) water pump (5) filtering ponds (7); Air-breathing cap (24) is formed, and removes SO 2Deduster is characterised in that and is provided with air inlet (8) gas through Wen Shi deduster (9), (10) dedusting, enter down control body (11) and carry out the water attack dedusting, carry out cyclone dust removal after entering impeller (12), carry out foam dust-removing after entering filter course (13), water ring (14) spray down supplies water for filter course dedusting and cyclone dust removal, gas rises through nozzle (15) moisture film, carry out water film dedusting, behind impeller (16), carry out cyclone dust removal, behind ventilation blower, produce negative pressure and drive the running of whole system gas, carry out condensation after entering clarifier, foam, cyclone dust removal, condensation are to realize by water ring (18) and running water.Further remove fine dust and SO through filtering layer (19) 2, aqueous vapor separates water, steam through impeller (20), and Purge gas enters air-breathing cap (24) by pipeline (21), enters atmosphere by air-breathing cap (24).The sealing of controlling body (11) down is that the water by water tank (1) is sealed, the water of water pump (5) is supplied by pond (7), the water in pond is supplied with by filtering ponds (6), and the water of filtering ponds (6) is supplied with by the casual water pipe (22) of water tank, and casual water pipe is supplied with by the water of deduster (2) inner nozzle.Slag tap (23) is in order to regular slagging.
- 2, according to right 1, Wen Shi comprehensively removes SO 2The deduster container inner wall is made up of state-of-the-art technology anti-corrosion material epoxy resin.
- 3, according to right 1, Wen Shi comprehensively removes SO 2Deduster removes SO 2Material must have following characteristics, and suction SO must be arranged 2The characteristics of gas must have, have and SO 2The characteristics of reaction must have the stable characteristics of secondary pollution that do not produce that generate.The present invention requires following protection.A, material: putting into filtering material (this patent only appears characteristics and do not appear true thing) has absorption SO 2And and SO 2The characteristics of reaction have absorption and snperoxiaized characteristics.B, material: sodium bicarbonate has absorption SO 2Characteristics, have and SO 2Directly Fan Ying characteristics generate stable sulfide characteristics but have with peroxide and oxygen.C, material: seawater effectively absorbs SO 2Characteristics, and can and SO 2Generate the not characteristics of polluted seawater of stable compound, the absorption SO that can effectively replace sodium bicarbonate and risen 2Effect.
- 4, according to right 1 described shown in figure two air-breathing cap forms in pipeline (4), (5) up and down in upper flange (2), (3) down by blade (1), this structure can be extracted gas in the pipe out, the effect of reduction air-introduced machine power.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00102517 CN1308982A (en) | 2000-02-14 | 2000-02-14 | Comprehensive duster able to remove SO2 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00102517 CN1308982A (en) | 2000-02-14 | 2000-02-14 | Comprehensive duster able to remove SO2 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN1308982A true CN1308982A (en) | 2001-08-22 |
Family
ID=4576440
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 00102517 Pending CN1308982A (en) | 2000-02-14 | 2000-02-14 | Comprehensive duster able to remove SO2 |
Country Status (1)
Country | Link |
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CN (1) | CN1308982A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101721869B (en) * | 2009-12-10 | 2011-12-14 | 四川大学 | Non-exhaust type purification method for air in textile workshop |
CN101732967B (en) * | 2009-12-10 | 2011-12-14 | 四川大学 | Non-emission type purification method for air in organophosphorus pesticide filling workshop |
CN101721870B (en) * | 2009-12-10 | 2012-01-18 | 四川大学 | Air non-discharging purification method in ore crushing plant |
CN101733267B (en) * | 2009-12-10 | 2012-01-18 | 四川大学 | Air purifying method for flour workshops |
CN102985371A (en) * | 2010-08-18 | 2013-03-20 | 三菱重工业株式会社 | Aerator, seawater flue-gas desulfurization system equipped with same, and method for operating the aerator |
CN103566677A (en) * | 2013-11-01 | 2014-02-12 | 陈兴星 | Waste gas purification tower |
CN104492208A (en) * | 2014-11-12 | 2015-04-08 | 山东科技大学 | Wet-type blower fan foam whirling current dedusting treatment device |
CN106799109A (en) * | 2017-03-20 | 2017-06-06 | 林建新 | A kind of high-efficiency energy-saving dust-removing equipment |
CN107335307A (en) * | 2016-05-02 | 2017-11-10 | 广州赛佛科技有限公司 | A kind of atmospheric cleaning method and its purifier |
-
2000
- 2000-02-14 CN CN 00102517 patent/CN1308982A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101721869B (en) * | 2009-12-10 | 2011-12-14 | 四川大学 | Non-exhaust type purification method for air in textile workshop |
CN101732967B (en) * | 2009-12-10 | 2011-12-14 | 四川大学 | Non-emission type purification method for air in organophosphorus pesticide filling workshop |
CN101721870B (en) * | 2009-12-10 | 2012-01-18 | 四川大学 | Air non-discharging purification method in ore crushing plant |
CN101733267B (en) * | 2009-12-10 | 2012-01-18 | 四川大学 | Air purifying method for flour workshops |
CN102985371A (en) * | 2010-08-18 | 2013-03-20 | 三菱重工业株式会社 | Aerator, seawater flue-gas desulfurization system equipped with same, and method for operating the aerator |
CN102985371B (en) * | 2010-08-18 | 2014-08-20 | 三菱重工业株式会社 | Aerator, seawater flue-gas desulfurization system equipped with same, and method for operating the aerator |
CN103566677A (en) * | 2013-11-01 | 2014-02-12 | 陈兴星 | Waste gas purification tower |
CN104492208A (en) * | 2014-11-12 | 2015-04-08 | 山东科技大学 | Wet-type blower fan foam whirling current dedusting treatment device |
CN107335307A (en) * | 2016-05-02 | 2017-11-10 | 广州赛佛科技有限公司 | A kind of atmospheric cleaning method and its purifier |
CN107335307B (en) * | 2016-05-02 | 2019-08-02 | 广州赛佛科技有限公司 | A kind of atmospheric cleaning method and its purification device |
CN106799109A (en) * | 2017-03-20 | 2017-06-06 | 林建新 | A kind of high-efficiency energy-saving dust-removing equipment |
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Legal Events
Date | Code | Title | Description |
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C06 | Publication | ||
PB01 | Publication | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |