CN202538581U - Double water-wheel reciprocating down-flow desulfuration dust remover - Google Patents
Double water-wheel reciprocating down-flow desulfuration dust remover Download PDFInfo
- Publication number
- CN202538581U CN202538581U CN2012200954533U CN201220095453U CN202538581U CN 202538581 U CN202538581 U CN 202538581U CN 2012200954533 U CN2012200954533 U CN 2012200954533U CN 201220095453 U CN201220095453 U CN 201220095453U CN 202538581 U CN202538581 U CN 202538581U
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- air
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- inlet
- flow
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- 239000000428 dust Substances 0.000 title claims abstract description 26
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 230000023556 desulfurization Effects 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims 4
- 238000005192 partition Methods 0.000 claims 3
- 238000000746 purification Methods 0.000 abstract description 6
- 229910052717 sulfur Inorganic materials 0.000 abstract description 3
- 239000011593 sulfur Substances 0.000 abstract description 3
- 239000010438 granite Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 22
- 230000003009 desulfurizing effect Effects 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
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- Separation Of Particles Using Liquids (AREA)
- Treating Waste Gases (AREA)
Abstract
Provided is a double water-wheel reciprocating down-flow desulfuration dust remover. Air is directly sprayed by a water inlet sprayer arranged on the top end after flowing in from an air inlet, and is primarily purified, and the air is taken into an air return chamber. Water in the water inlet sprayer flows together to form water flow through a flow guide separating plate arranged on the upper portion of the air return chamber to directly impact a waterpower vane wheel to rotate, the waterpower vane wheel drives the air to flow continuously between an upper water film and a lower water film in order to achieve repeated and multidirectional water-air contact, and therefore efficiency of off-sulfur and dust removal is greatly improved. After second purification, the air flows into a desulfurization and dedusting chamber, and is carried out to a third purification in the dedusting and desulfurization chamber. Dust particles flows into an ash sump, and the water level is adjusted by a water level tank. Purified air is exhausted through an air outlet. The dedusting chamber adopts a granite structure. The double water-wheel reciprocating straight-flow desulfuration dust remover has the advantages of being corrosion-resisting and good in efficiency of off-sulfur and dust removal.
Description
Technical field
The utility model relates to a kind of deduster, relates in particular to a kind of pair of reciprocal following current desulfurizing dust-collector of water wheels.
Background technology
Common wet method sulphur removing and dust removing cleaning equipment has atomizing, cyclone type, water storage impact water bath formula, column plate type, venturi etc.But, and after contacting, water make cleaner corrode easily usually because sulfur-bearing in the flue gas.Secondly owing to receive the restriction of various factors, the efficiency of dust collection of single deduster is not very high.
Summary of the invention
The purpose of the utility model has been to provide a kind of two water wheels corrosion-resistant, the dust-removal and desulfurizing excellent in efficiency reciprocal following current desulfurizing dust-collector.
The utility model is realized like this; It comprises housing, inlet, air inlet, waterpower impeller, return-air chamber, gas outlet, water inlet shower nozzle, diaphragm, dividing plate, desulfurization dust chamber, water level case, ash settling basin; It is characterized in that being provided with successively from the top down in the housing inlet, air inlet, return-air chamber, desulfurization dust chamber, ash settling basin; One side lower part of housing is provided with the water level case, and opposite side is provided with the gas outlet; The end outlet of inlet and air inlet all is positioned at the central axis place of housing; The end outlet of inlet is connected with into water shower nozzle; The return-air chamber is arranged with diaphragm, waterpower impeller, diaphragm from the top down successively along the housing axis, the middle part of desulfurization dust chamber is provided with the dividing plate of horizontal groove shape, and the bottom of desulfurization dust chamber is provided with diaphragm; One end of said diaphragm is connected on the housing; The other end all is positioned at the side of waterpower impeller near the housing axis, and said diaphragm sinks near a side of housing axis, is provided with some tilt clapboards in the body of gas outlet.Dirt pocket adopts the granite structure.
The technique effect of the utility model is: directly by the water inlet shower nozzle on top spray, reach preliminary purification, and take gas to the return-air chamber after gas gets into from air inlet; The diaphragm on top, water cooled via return air chamber of the water inlet shower nozzle back of confluxing forms current and directly impacts the waterpower impeller and make its rotation, and the waterpower impeller drives gas and constantly circulates in up and down between the moisture film, reaches repeatedly multi-faceted aqueous vapor contact; Desulfurization dust-removing efficiency is improved greatly; Gas gets into desulfurization dust chamber after purifying double purification, desulfurization dust chamber carries out three times to gas and purifies, and grit flows into ash settling basin; The water level case is regulated the water level of ash settling basin, and purified gas is discharged by the gas outlet.
Description of drawings
Fig. 1 is the structural representation of the utility model.
The specific embodiment
As shown in Figure 1; The utility model is realized like this; It comprises housing 1, inlet 2, air inlet 12, waterpower impeller 5, return-air chamber 4, gas outlet 10, water inlet shower nozzle 3, diaphragm 11, dividing plate 7, desulfurization dust chamber 6, water level case 8, ash settling basin 9; Be provided with inlet 2, air inlet 12, return-air chamber 4, desulfurization dust chamber 6, ash settling basin 9 in the housing 1 from the top down successively, a side lower part of housing 1 is provided with water level case 8, and opposite side is provided with gas outlet 10; The end outlet of inlet 2 and air inlet 12 all is positioned at the central axis place of housing 1; The end outlet of inlet 2 is connected with into water shower nozzle 3; Return-air chamber 4 is arranged with diaphragm 11, waterpower impeller 5, diaphragm 11 along housing 1 axis from the top down successively, and the middle part of desulfurization dust chamber 6 is provided with the dividing plate 7 of horizontal groove shape, the diaphragm 11 that the bottom of desulfurization dust chamber 6 is provided with; One end of said diaphragm 11 is connected on the housing 1; The other end all is positioned at the side of waterpower impeller 5 near housing 1 axis, and said diaphragm 11 sinks near a side of housing 1 axis, is provided with some tilt clapboards 7 in the body of gas outlet 10.Directly by water inlet shower nozzle 3 sprays on top, reach preliminary purification, and take gas to return-air chamber 4 after gas gets into from air inlet 12; Form current after the diaphragm 11 on 4 tops, water cooled via return air chamber of water inlet shower nozzle 3 ejections confluxes and directly impact waterpower impeller 5 and make its rotation, because waterpower impeller 5 all has deflector 11 up and down, water forms moisture film on deflector 11; Therefore waterpower impeller 5 drives gases and constantly circulates in up and down between the moisture film, reaches repeatedly multi-faceted aqueous vapor contact, and desulfurization dust-removing efficiency is improved greatly; Gas gets into desulfurization dust chamber 6 after purifying double purification; The middle part of desulfurization dust chamber 6 is provided with the dividing plate 7 of horizontal groove shape, and diaphragm 11 is arranged at the bottom, the further Purge gas of moisture film that forms on dividing plate 7 and the diaphragm 11; After 6 pairs of gases of desulfurization dust chamber carry out purifying for three times; Grit flows into ash settling basin 9, and water level case 8 is regulated the water level of ash settling basin 9, and purified gas is discharged by the gas outlet.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200954533U CN202538581U (en) | 2012-03-15 | 2012-03-15 | Double water-wheel reciprocating down-flow desulfuration dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200954533U CN202538581U (en) | 2012-03-15 | 2012-03-15 | Double water-wheel reciprocating down-flow desulfuration dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202538581U true CN202538581U (en) | 2012-11-21 |
Family
ID=47159275
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200954533U Expired - Fee Related CN202538581U (en) | 2012-03-15 | 2012-03-15 | Double water-wheel reciprocating down-flow desulfuration dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202538581U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107321158A (en) * | 2017-07-31 | 2017-11-07 | 泉州泉港灿鹏机械设备有限公司 | A kind of energy-saving and high efficient acid mist purifying tower based on Internet of Things |
| WO2018055348A1 (en) * | 2016-09-23 | 2018-03-29 | Scotstream Generation Limited | Water energy apparatus |
| CN110404361A (en) * | 2019-08-06 | 2019-11-05 | 李哲 | A kind of revolving desulfurizing tower sweetening process spray equipment |
| CN118904058A (en) * | 2024-08-28 | 2024-11-08 | 中国核工业华兴建设有限公司 | Petrochemical waste gas multistage deodorization device and application method thereof |
-
2012
- 2012-03-15 CN CN2012200954533U patent/CN202538581U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018055348A1 (en) * | 2016-09-23 | 2018-03-29 | Scotstream Generation Limited | Water energy apparatus |
| CN107321158A (en) * | 2017-07-31 | 2017-11-07 | 泉州泉港灿鹏机械设备有限公司 | A kind of energy-saving and high efficient acid mist purifying tower based on Internet of Things |
| CN107321158B (en) * | 2017-07-31 | 2019-11-08 | 荆门市拓达科技有限公司 | A kind of energy-saving and high efficient acid mist purifying tower based on Internet of Things |
| CN110404361A (en) * | 2019-08-06 | 2019-11-05 | 李哲 | A kind of revolving desulfurizing tower sweetening process spray equipment |
| CN118904058A (en) * | 2024-08-28 | 2024-11-08 | 中国核工业华兴建设有限公司 | Petrochemical waste gas multistage deodorization device and application method thereof |
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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: 20121121 Termination date: 20130315 |