CN202497792U - Split type partition plate water film desulfurization dust collector - Google Patents
Split type partition plate water film desulfurization dust collector Download PDFInfo
- Publication number
- CN202497792U CN202497792U CN2012200978504U CN201220097850U CN202497792U CN 202497792 U CN202497792 U CN 202497792U CN 2012200978504 U CN2012200978504 U CN 2012200978504U CN 201220097850 U CN201220097850 U CN 201220097850U CN 202497792 U CN202497792 U CN 202497792U
- Authority
- CN
- China
- Prior art keywords
- chamber
- water
- housing
- desulfurization dust
- dividing plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 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 title claims abstract description 51
- 239000000428 dust Substances 0.000 title claims abstract description 30
- 230000003009 desulfurizing Effects 0.000 title claims abstract description 22
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 21
- 238000005192 partition Methods 0.000 title abstract 6
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 238000010410 dusting Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 15
- 239000000779 smoke Substances 0.000 description 5
- 238000000746 purification Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 2
- 239000010438 granite Substances 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 150000003463 sulfur Chemical group 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Abstract
The utility model discloses a split type partition plate water film desulfurization dust collector which comprises a shell, a water inlet, a gas inlet, a desulfurization dust chamber, a water level box, an overflow groove, partition plates, a defogging chamber, a gas outlet, a liquid hole and an ash settling basin, wherein the water inlet is arranged on the side wall of the top end of the shell; the gas inlet is arranged on the lower side wall of the shell close to the water inlet; the overflow groove is arranged below the partition plate of the water inlet; the desulfurization dust chamber is arranged below the overflow groove; the ash settling basin is arranged at the bottom of the shell; the water level box is arranged on one side of the lower part of the shell, and the defogging chamber is arranged on the other side; the gas outlet is arranged on the defogging chamber; and multiple vertical partition plates are arranged in the defogging chamber. Gas enters from the gas inlet; the dust collection liquid flows in from the water inlet toward the desulfurization dust chamber below the overflow groove and forms a water film on the partition plates of the desulfurization dust chamber; the water film purifies the gas, and a relatively high dust collection efficiency is realized; the dust collection liquid and the dust flow to the ash settling basin together; the water level box adjusts the water level of the ash settling basin; and the purified gas is defogged by the defogging chamber and exhausted from the gas outlet.
Description
Technical field
The utility model relates to a kind of desulfurizing dust-collector, relates in particular to a kind of by-passing type dividing plate water desulfurizing-dusting device.
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 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 simple and practical, by-passing type dividing plate water desulfurizing-dusting device that desulfurization dust-removing efficiency is good.
The utility model realizes that like this it comprises housing, water inlet, air inlet, desulfurization dust chamber, water level case, overflow launder, dividing plate, takes off fog chamber, gas outlet, liquid hole, ash settling basin, it is characterized in that the sidewall top of housing is provided with water inlet; Housing is provided with air inlet near the sidewall of water inlet below; The end that air inlet is positioned at housing is connected with the dividing plate under being tilted to, and the end that water inlet is positioned at housing is connected an end of the dividing plate under being tilted to, and the proper bottom of another of said dividing plate is provided with overflow launder; The below of overflow launder is provided with the desulfurization dust chamber that is made up of the dividing plate under some being tilted to; The bottom of housing is provided with ash settling basin, and lower housing portion one side is provided with the water level case, and opposite side is provided with and takes off the fog chamber; Take off the fog chamber and be provided with the gas outlet; Take off and be provided with some staggered vertical dividing plates of arranging that list down in the fog chamber, be provided with some liquid hole between the wall near the vertical dividing plate of housing bottom and housing, take off the fog chamber and be connected with desulfurization dust chamber.Deduster is the granite structure.
The technique effect of the utility model is: gas gets into from air inlet, and dedusting liquid flows into from water inlet, flows to the desulfurization dust chamber of below through overflow launder; On the dividing plate of desulfurization dust chamber, form moisture film, gas is carried out filtration, purification repeatedly, thereby reach higher efficiency of dust collection; Dedusting liquid and dust flow to ash settling basin together; The water level case is regulated the ash settling basin water level, and purified gas is sloughed water smoke through taking off the fog chamber, discharges from the gas outlet.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Housing 2, water inlet 3, air inlet 4, desulfurization dust chamber 5, water level case in the drawings, 1,
6, ash settling basin 7, take off fog chamber 8, gas outlet 9, dividing plate 10, overflow launder 11, liquid hole.
The specific embodiment
As shown in Figure 1, it comprises housing 1, water inlet 2, air inlet 3, desulfurization dust chamber 4, water level case 5, overflow launder 10, takes off fog chamber 7, dividing plate 9, gas outlet 8, liquid hole 11, ash settling basin 6, and the top sidewall of housing 1 is provided with water inlet 2; Housing 1 is provided with air inlet 3 near the sidewall of water inlet 2 belows; The end that air inlet 3 is positioned at housing 1 is connected with the dividing plate 9 under being tilted to, and the end that water inlet 2 is positioned at housing 1 is connected an end of the dividing plate 9 under being tilted to, and the proper bottom of another of said dividing plate 9 is provided with overflow launder 10; The below of overflow launder 10 is provided with the desulfurization dust chamber 4 that is made up of the dividing plate under some being tilted to 9; The bottom of housing 1 is provided with ash settling basin 6, and housing 1 bottom one side is provided with water level case 5, and opposite side is provided with and takes off fog chamber 7; Take off fog chamber 7 and be provided with gas outlet 8; Take off and be provided with some staggered vertical dividing plates 9 of arranging that list down in the fog chamber 7, be provided with some liquid hole 11 between the wall near the vertical dividing plate 9 of housing 1 bottom and housing 1, take off fog chamber 7 and be connected with desulfurization dust chamber 4.Deduster is the granite structure.Gas gets into from air inlet 3, and dedusting liquid flows into from water inlet 2, after overflow launder 10 shuntings, flows to the desulfurization dust chamber 4 of below; On some dividing plates 9 of desulfurization dust chamber 4, form moisture film, moisture film carries out filtration, purification repeatedly to gas, thereby reaches higher efficiency of dust collection; After the purification, dedusting liquid and dust flow to ash settling basin 6 together, and purified gas is through taking off fog chamber 7; Some vertical dividing plates 9 of arranging that interlock that list down that water smoke is taken off in the fog chamber 7 stop, slough water smoke, and gas is with after water smoke separates; The drop of water smoke flows back to ash settling basin 6 from the liquid hole 11 of bottom, and gas is 8 discharges from the gas outlet, and water level case 5 is regulated ash settling basins 6 water levels.
Claims (1)
1. by-passing type dividing plate water desulfurizing-dusting device, it comprises housing, water inlet, air inlet, desulfurization dust chamber, water level case, overflow launder, dividing plate, takes off fog chamber, gas outlet, liquid hole, ash settling basin, it is characterized in that the sidewall top of housing is provided with water inlet; Housing is provided with air inlet near the sidewall of water inlet below; The end that air inlet is positioned at housing is connected with the dividing plate under being tilted to, and the end that water inlet is positioned at housing is connected an end of the dividing plate under being tilted to, and the proper bottom of another of said dividing plate is provided with overflow launder; The below of overflow launder is provided with the desulfurization dust chamber that is made up of the dividing plate under some being tilted to; The bottom of housing is provided with ash settling basin, and lower housing portion one side is provided with the water level case, and opposite side is provided with and takes off the fog chamber; Take off the fog chamber and be provided with the gas outlet; Take off and be provided with some staggered vertical dividing plates of arranging that list down in the fog chamber, be provided with some liquid hole between the wall near the vertical dividing plate of housing bottom and housing, take off the fog chamber and be connected with desulfurization dust chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200978504U CN202497792U (en) | 2012-03-16 | 2012-03-16 | Split type partition plate water film desulfurization dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200978504U CN202497792U (en) | 2012-03-16 | 2012-03-16 | Split type partition plate water film desulfurization dust collector |
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| Publication Number | Publication Date |
|---|---|
| CN202497792U true CN202497792U (en) | 2012-10-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2012200978504U Expired - Fee Related CN202497792U (en) | 2012-03-16 | 2012-03-16 | Split type partition plate water film desulfurization dust collector |
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| CN (1) | CN202497792U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104083967A (en) * | 2014-07-29 | 2014-10-08 | 广西南宁中嘉环保阀门制造有限公司 | Impact-type water film desulfurization dust remover |
| CN105135448A (en) * | 2015-10-08 | 2015-12-09 | 四川长城环境科学研究院 | Medical three-waste treatment system solving method and device |
-
2012
- 2012-03-16 CN CN2012200978504U patent/CN202497792U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104083967A (en) * | 2014-07-29 | 2014-10-08 | 广西南宁中嘉环保阀门制造有限公司 | Impact-type water film desulfurization dust remover |
| CN105135448A (en) * | 2015-10-08 | 2015-12-09 | 四川长城环境科学研究院 | Medical three-waste treatment system solving method and device |
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| GR01 | Patent grant | ||
| C14 | Grant of patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121024 Termination date: 20130316 |
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| C17 | Cessation of patent right |