CN202122894U - Efficient liquid-surface micro-division desulfurizing and dedusting device - Google Patents
Efficient liquid-surface micro-division desulfurizing and dedusting device Download PDFInfo
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- CN202122894U CN202122894U CN2011202135607U CN201120213560U CN202122894U CN 202122894 U CN202122894 U CN 202122894U CN 2011202135607 U CN2011202135607 U CN 2011202135607U CN 201120213560 U CN201120213560 U CN 201120213560U CN 202122894 U CN202122894 U CN 202122894U
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- 230000003009 desulfurizing Effects 0.000 title abstract description 10
- 239000007788 liquid Substances 0.000 claims description 24
- 238000000605 extraction Methods 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 10
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 238000006477 desulfuration reaction Methods 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000007791 liquid phase Substances 0.000 abstract 1
- 239000012071 phase Substances 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 239000003546 flue gas Substances 0.000 description 7
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound 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O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 6
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- 239000003513 alkali Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 210000004940 Nucleus Anatomy 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- 239000004071 soot Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical group 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
Abstract
The utility model provides an efficient liquid-surface micro-division desulfurizing and dedusting device. The efficient liquid-surface micro-division desulfurizing and dedusting device comprises a tower body, wherein a demister, a spraying device and a module are sequentially arranged in the tower body from top to bottom, and a Venturi tube is also arranged at the bottom of the tower body. The efficient liquid-surface micro-division desulfurizing and dedusting device is mainly suitable for the desulfuration and dedusting of a small-size boiler and has the advantages of low cost, high efficiency and the integration of desulfuration, dedusting and demisting; as a micro-division mechanism is additionally arranged at the inner part of equipment, water resource can be utilized sufficiently and can be sufficiently subdivided and micro-divided among a plurality of layers of grids, so that superficial area is greatly increased, and the contact between liquid phase and gas phase is particularly sufficient; and desulfurizing and dedusting efficiency can reach higher than 98%.
Description
Technical field
The utility model relates to dustless application, is specifically related to a kind of liquid surface differential high-efficient desulfation dust-extraction device.
Background technology
Present sulfur dioxide of China and soot emissions total amount all up to more than 2,000 ten thousand tons, rank first in the world.Sulfur dioxide and smoke contamination have become the key factor of restriction China economy, social sustainable development.Desulfurization and dedusting technology comprises dust-collecting sulfur-removing method at present, the differential method, and venturi granite moisture film method is two, the alkali wet type, cloth-bag type, and limestone-gypsum wet method, the technical characteristic of each process of cleaning specifically sees the following form:
The utility model content
In order to solve the problems of the technologies described above, the utility model provides a kind of liquid surface differential high-efficient desulfation dust-extraction device.
The technical scheme that the utility model adopts: a kind of liquid surface differential high-efficient desulfation dust-extraction device, comprise tower body, be disposed with demister in the said tower body from top to bottom, spray equipment, module, the bottom of said tower body also is provided with Venturi tube.
As the further improvement of technique scheme, above-mentioned Venturi tube is a rectangle.
As the further improvement of technique scheme, said module is netted module.
As the further improvement of technique scheme, said module is a multilayer.
As the further improvement of technique scheme, said module is the differential module.
As the further improvement of technique scheme, said module is selected stainless steel or polymer composite for use.
As the further improvement of technique scheme, the said module aperture is the 10-30 order.
As the further improvement of technique scheme, said module thickness is 150-200mm.
As the further improvement of technique scheme, above-mentioned spray equipment is many groups.
Enforcement the utlity model has following advantage:
1, this device mainly is applicable to the medium small boiler desulfurization and dedusting, and it is with low cost, instant effect, with desulfurization in the dedusting demist in one, efficient is higher; Because device interior has added differential mechanism, can make full use of only water resource, and it can fully be segmented and differential between multi-layer net, surface area has increase, and the gas-liquid two-phase contact is abundant especially, and its desulfurization dust-removing efficiency reaches more than 98%.
2, the absorption solute in the absorption liquid is sheet alkali (NaOH), and absorption liquid can recycle for a long time, does not have the crystalline hydrate solute to separate out, and lye pump, pipeline, nozzle do not have clogging, need not safeguard.
3, combine venturi, wet type whirlwind, differential mechanism and spray etc., thereby realized the incorporate function of desulfurization and dedusting demist, operating cost and resistance are little, operate also easier.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 is the front view of module in the utility model;
Fig. 3 is the structural representation of Venturi tube in the utility model.
Description of reference numerals
Tower body 1; Demister 2; Spray equipment 3; Module 4; Venturi tube 5; Collapsible tube 501, trunnion 502, convergent divergent channel 503; Outer comb 6.
The specific embodiment
The liquid surface differential high-efficient desulfation dust-extraction device that the utility model provides comprises tower body 1, is disposed with demister 2 in the tower body 1 from top to bottom, organizes spray equipment 3 more, module 4, and the bottom of tower body 1 also is provided with the Venturi tube 5 of rectangle.Module 4 is netted, and is multilayer differential module, and its material adopts stainless steel or other metal materials to process, and also can use the polymer composite of resistant to elevated temperatures alkali resistance corrosion to replace, and it is shaped as cylindrical or elliposoidal or other shapes.Module 4 apertures are the 10-30 order, and whole module thickness is 150-200mm, and individual layer module thickness is 2-4mm, and each works as a layer module gap is 20-30mm, and whole module has the 6-10 layer approximately.
The operation principle of the utility model is following:
The sulfur-bearing ash-laden gas of discharging from boiler gets into by collapsible tube 501 along flue with the speed of 15-18m/s, and the rectangle Venturi tube of trunnion 502 and convergent divergent channel 503 can be transformed into kinetic energy with gas-static gradually through collapsible tube 501; Speed raises gradually, mixes at collapsible tube 501 terminal spray atomizing absorption liquids, and the speed that has arrived trunnion 502 position flue dust reaches 40-60m/s; Fluid is in stronger turbulence state, impels two of gas-liquids fully to mix, after the preliminary treatment; Behind convergent divergent channel 503,, after air inlet pipe 6 rotations, get into tower body 1 through the design of flowing backwards; Remove to clash into the netted module 4 of stainless steel multilayer, the module hole size is controlled between the 10-30 order, and multilayer module thickness is at 150-200mm; Individual layer module thickness is 2-4mm, and each individual layer module gap is 20-30mm, and whole module has the 6-10 layer approximately.Spray the absorption liquid that gets off from tower body 1 top when running into module 4, it can fully be segmented with differential between multi-layer net become little water curtain, liquid surface gathers increase.Improved the probability that flue gas contacts with absorption liquid greatly, flue dust is dispelling water curtain simultaneously, because the surface tension effects of liquid; Dust in the flue gas is abundant or dissolved absorption of sulfur dioxide and reaction by water and since flue gas in dust caught by water after, become nucleus; Impel water smoke sharply to condense and become drop; Under the flue gas that is rotated drives, do centrifugal motion, be thrown to inner wall of tower, discharge through outer comb 7 at the bottom of the inflow tower; This process is followed the absorption and the reaction of sulfide simultaneously, and efficient is up to more than 98%.After this flue gas continues to be handled step by step by vaporific spray liquid facility in uphill process, and the flue gas after multistage is handled is taken off most of moisture in the flue gas through demister, final row's mark.
The foregoing description, just the preferred embodiment of the utility model is not to be used for limiting the utility model practical range, so all equivalences of being done with the said content of the utility model claim change, all should be included within the utility model claim scope.
Claims (9)
1. a liquid surface differential high-efficient desulfation dust-extraction device comprises tower body, it is characterized in that: be disposed with demister in the said tower body from top to bottom, and spray equipment, module, the bottom of said tower body also is provided with Venturi tube.
2. liquid surface differential high-efficient desulfation dust-extraction device according to claim 1 is characterized in that: said Venturi tube is a rectangle.
3. liquid surface differential high-efficient desulfation dust-extraction device according to claim 1 is characterized in that: said module is netted module.
4. liquid surface differential high-efficient desulfation dust-extraction device according to claim 2 is characterized in that: said module is a multilayer.
5. liquid surface differential high-efficient desulfation dust-extraction device according to claim 4 is characterized in that: said module is the differential module.
6. liquid surface differential high-efficient desulfation dust-extraction device according to claim 5, it is characterized in that: said module is selected stainless steel or polymer composite for use.
7. liquid surface differential high-efficient desulfation dust-extraction device according to claim 6 is characterized in that: said module aperture is the 10-30 order.
8. liquid surface differential high-efficient desulfation dust-extraction device according to claim 7 is characterized in that: said module gross thickness is 150-200mm.
9. liquid surface differential high-efficient desulfation dust-extraction device according to claim 1 is characterized in that: said spray equipment is many groups.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202135607U CN202122894U (en) | 2011-06-22 | 2011-06-22 | Efficient liquid-surface micro-division desulfurizing and dedusting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202135607U CN202122894U (en) | 2011-06-22 | 2011-06-22 | Efficient liquid-surface micro-division desulfurizing and dedusting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202122894U true CN202122894U (en) | 2012-01-25 |
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| CN2011202135607U Expired - Fee Related CN202122894U (en) | 2011-06-22 | 2011-06-22 | Efficient liquid-surface micro-division desulfurizing and dedusting device |
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| CN (1) | CN202122894U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474870A (en) * | 2014-12-08 | 2015-04-01 | 冯学岭 | Novel desulfurization dust remover |
| CN109276978A (en) * | 2018-11-30 | 2019-01-29 | 单林祥 | A kind of efficient tail gas wet method desulfurizer |
-
2011
- 2011-06-22 CN CN2011202135607U patent/CN202122894U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474870A (en) * | 2014-12-08 | 2015-04-01 | 冯学岭 | Novel desulfurization dust remover |
| CN109276978A (en) * | 2018-11-30 | 2019-01-29 | 单林祥 | A kind of efficient tail gas wet method desulfurizer |
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