CN201894904U - Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device - Google Patents
Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device Download PDFInfo
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- CN201894904U CN201894904U CN201020225305XU CN201020225305U CN201894904U CN 201894904 U CN201894904 U CN 201894904U CN 201020225305X U CN201020225305X U CN 201020225305XU CN 201020225305 U CN201020225305 U CN 201020225305U CN 201894904 U CN201894904 U CN 201894904U
- Authority
- CN
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- Prior art keywords
- eddy flow
- gas
- provided
- urceolus
- removal
- Prior art date
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- 230000003009 desulfurizing Effects 0.000 title claims abstract description 19
- 239000007789 gases Substances 0.000 title claims abstract description 18
- 238000007789 sealing Methods 0.000 claims abstract description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 17
- 239000003546 flue gas Substances 0.000 claims description 16
- 239000000779 smoke Substances 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 238000005507 spraying Methods 0.000 abstract description 3
- 239000000126 substances Substances 0.000 abstract description 3
- 238000000034 methods Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 4
- 239000007788 liquids Substances 0.000 description 4
- 238000005516 engineering processes Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/04—Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour through foam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/04—Regenerating the washing fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/10—Means for removing the washing fluid dispersed in the gas or vapours
- B01D2247/101—Means for removing the washing fluid dispersed in the gas or vapours using a cyclone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/10—Means for removing the washing fluid dispersed in the gas or vapours
- B01D2247/105—Means for removing the washing fluid dispersed in the gas or vapours by gas flow reversal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/10—Means for removing the washing fluid dispersed in the gas or vapours
- B01D2247/106—Means for removing the washing fluid dispersed in the gas or vapours using a structured demister, e.g. tortuous channels
Abstract
Description
Technical field
The utility model provides a kind of flue purifier of boiler, especially a kind of bitubular eddy flow bubbling dust-removal and desulfurizing smoke eliminator.
Background technology
The continuous reinforcement of people's environmental consciousness now, increasing people recognizes the importance of environmental protection, environmental protection equipment also is subject to people's attention more and more and utilizes.The research and development environmental protection equipment, especially smoke pollution abatement equipment not only has positive impetus to the environmental protection development plan of promoting country, and possesses certain market prospect and commercial value.Since electric precipitation that tradition adopts and bag-type dust can only dedusting can not desulfurization, certain defective is arranged on the purification level, also contain harmful substance in the waste gas of discharge.The device structure complexity is not easy to safeguard.
Summary of the invention
The utility model is in order to overcome the defective that above-mentioned prior art exists, but provide a kind of simple in structure, can dedusting the bitubular eddy flow bubbling dust-removal and desulfurizing smoke eliminator of desulfurization again.
The utility model is achieved through the following technical solutions: a kind of bitubular eddy flow bubbling dust-removal and desulfurizing smoke eliminator, it comprises the urceolus that has air inlet and exhanst gas outlet, be provided with inner core in the urceolus, inner core is fixed in the urceolus by upper sealing plate and following shrouding, be provided with helical form eddy flow plate between described urceolus and the inner core, be provided with sprayer unit between eddy flow plate blade, described shrouding down is provided with discharge pipe and playpipe.
Other features of the present utility model also have: be provided with eaves shape baffle plate in the described inner core, can make flue gas along the walking of baffle plate broken line, strengthen removing fog effect.
Described sprayer unit circulating pump connects circulatory pool, helps recycling to dust-removal and desulfurizing solution.
Adopt hollow cone tangent type nozzle in the described sprayer unit, the big spray effect of its unobstructed diameter is good, and can save the water source, makes reaction more thorough.
The top of described urceolus is provided with the flue gas demister, can remove the water smoke in the flue gas of discharge.
The beneficial effect of this programme can be learnt according to the narration to such scheme, described bitubular eddy flow bubbling dust-removal and desulfurizing smoke eliminator, urceolus have air inlet and exhanst gas outlet and in be provided with inner core, inner core is fixed in the urceolus by upper sealing plate and following shrouding, be provided with helical form eddy flow plate between described urceolus and the inner core, flue gas constantly changes direction in rotary course, making it be the eddy current shape moves downward, strengthened the reaction time and the response area of absorbent solution and gas, on the basis of improving its efficient, made its reaction more fully complete.Be provided with sprayer unit between eddy flow plate blade, can spray vaporific aqueous vapor and remove impurity and harmful substance in the flue gas.Spray nozzle adopts hollow cone tangent type nozzle, and its unobstructed diameter ambassador reaction is more thorough.Described shrouding down is provided with discharge pipe and playpipe, and flue gas is through the playpipe bubbling, and the liquid level of solution of tube bottom top forms froth bed outside, and the contact area of gas and liquid and time of contact are increased, and mass-transfer efficiency improves.Eddy flow plate place finishes the purified treatment first time of flue gas in this type of design, the froth bed place of flue gas above solution carries out double purification, the gas cleaning rate is increased substantially, and it uses maintenance very simple, applied range, in use can not occur stopping up or scale formation long service life.The utilization rate of equipment and installations height, operating cost is low, and is energy-saving and cost-reducing.Be applicable to various desulfurization dust-removing technique.This shows that the utility model compared with prior art has substantive distinguishing features and progress, the beneficial effect of its enforcement also is conspicuous.
Description of drawings:
Fig. 1 is the utility model structural representation.
Among the figure: 1. exhanst gas outlet, 2. urceolus, 3. flooding nozzle, 4. demister, 5. air inlet, 6. inner core 7. eddy flow plates, 8. eaves shape baffle plate, 9. discharge pipe, 10. playpipe, 11. sprayer units, 12. circulating pumps, 13. circulatory pools, 14. replenish ponds, 15. sewage draining exits.
The specific embodiment:
For clearly demonstrating the technical characterstic of this programme, with reference to the accompanying drawings the utility model specific embodiment is described further below:
As shown in Figure 1, a kind of bitubular eddy flow bubbling dust-removal and desulfurizing smoke eliminator, it comprises the urceolus 2 that has air inlet 5 and exhanst gas outlet 1, be provided with inner core 6 in the urceolus 2, inner core 6 is fixed in the urceolus 2 by upper sealing plate and following shrouding, be provided with helical form eddy flow plate 7 between described urceolus 2 and the inner core 6, be provided with sprayer unit 11 between eddy flow plate 7 blades, described shrouding down is provided with discharge pipe 9 and playpipe 10.Be provided with eaves shape baffle plate 8 in the described cigarette inner core 6.Series circulation pump 12 and being connected in the circulatory pool 13 on the sprayer unit 11, urceolus 2 bottoms are provided with sewage draining exit 15, and the top of urceolus 2 is provided with flue gas demister 4, and the top of demister is provided with flooding nozzle 3.
Flue gas is entered by the top air inlet 5 of urceolus 2, because the guiding of eddy flow plate 7 makes flue gas move downward by constant pitch rotation, nozzle ejection alkali lye is with gas cleaning between pitch.The flue gas that purifies through spraying enters plenum chamber at the afterbody of eddy flow plate 7 along its tangential direction, is connected to playpipe 10 and discharge pipe 9 on the following shrouding, and flue gas forms froth bed continuously through playpipe 10 bubblings between the upper and lower shrouding of solution district liquid level.Flue gas is through behind the dust-removal and desulfurizing, and the demister 4 on capable baffle plate 8 of the eaves in inner core 6 and cylindrical shell top takes off mist and handles again.Demister 4 tops are provided with the solid flooding nozzle 3 of direct current, and magnetic valve and time controller control flushing is arranged.Liquid after dust in flue gas and reaction absorb is discharged by sewage draining exit 15, is provided with screen pack in circulatory pool 13.Dust is through post precipitation, and periodic cleaning is to the soot.Solution after the absorption can enter in the circulatory pool 13 after filtering and continue to recycle, and the byproduct after the absorption can adopt the recycling method to turn harm into good, and does not cause secondary pollution.Be provided with side by side with circulatory pool and replenish pond 14, can be according to desulfuration solution pH value make-up solution as required.To dust removal efficiency 〉=99% of flue gas, desulfurization degree 〉=95% meets national requirements for environmental protection behind this equipment of use.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020225305XU CN201894904U (en) | 2010-06-13 | 2010-06-13 | Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020225305XU CN201894904U (en) | 2010-06-13 | 2010-06-13 | Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201894904U true CN201894904U (en) | 2011-07-13 |
Family
ID=44252823
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020225305XU CN201894904U (en) | 2010-06-13 | 2010-06-13 | Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201894904U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103170197A (en) * | 2013-04-08 | 2013-06-26 | 安徽理工大学 | Foam gas washing device |
| CN104096434A (en) * | 2013-04-03 | 2014-10-15 | 厦门大学 | Novel technology and novel device for dedusting and desulphurization of flue gas |
| CN104437071A (en) * | 2014-12-17 | 2015-03-25 | 曲堂杰 | Hybrid biphase desulfurization/denitrification/dust removal device and desulfurization/denitrification/dust removal method |
| CN105080274A (en) * | 2015-09-14 | 2015-11-25 | 山东中信钙业有限公司 | Spraying type desulfurization dust catcher |
| CN105498353A (en) * | 2015-11-28 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterworks primary sedimentation tower |
| CN105642097A (en) * | 2016-01-25 | 2016-06-08 | 中国石油大学(北京) | Flue gas desulfurization and dust removal method and device |
| CN106422639A (en) * | 2016-12-07 | 2017-02-22 | 北京中能诺泰节能环保技术有限责任公司 | Dust removal desulfurization augmenter and wet process desulfurization device |
| CN106512616A (en) * | 2016-03-22 | 2017-03-22 | 泓晟鼎（福建）重工科技有限公司 | Scrollwork wet-type gallery dust collection system |
| CN107569983A (en) * | 2017-08-08 | 2018-01-12 | 武汉和尔环保科技有限公司 | Smoke-gas wet desulfurization equipment |
| CN108554107A (en) * | 2018-07-02 | 2018-09-21 | 姜玉欣 | A kind of dusty gas Wet-type spray filter collector |
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2010
- 2010-06-13 CN CN201020225305XU patent/CN201894904U/en not_active IP Right Cessation
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| CN104096434A (en) * | 2013-04-03 | 2014-10-15 | 厦门大学 | Novel technology and novel device for dedusting and desulphurization of flue gas |
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| CN105498353A (en) * | 2015-11-28 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterworks primary sedimentation tower |
| CN105642097A (en) * | 2016-01-25 | 2016-06-08 | 中国石油大学(北京) | Flue gas desulfurization and dust removal method and device |
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| CN106422639A (en) * | 2016-12-07 | 2017-02-22 | 北京中能诺泰节能环保技术有限责任公司 | Dust removal desulfurization augmenter and wet process desulfurization device |
| CN106422639B (en) * | 2016-12-07 | 2020-02-14 | 北京中能诺泰节能环保技术有限责任公司 | Dust removal desulfurization synergist and wet desulphurization device |
| CN107569983A (en) * | 2017-08-08 | 2018-01-12 | 武汉和尔环保科技有限公司 | Smoke-gas wet desulfurization equipment |
| CN107569983B (en) * | 2017-08-08 | 2020-04-03 | 武汉和尔环保科技有限公司 | Wet flue gas desulfurization equipment |
| CN108554107A (en) * | 2018-07-02 | 2018-09-21 | 姜玉欣 | A kind of dusty gas Wet-type spray filter collector |
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