CN102698557B - Electrostatic spraying and dust-removing system - Google Patents
Electrostatic spraying and dust-removing system Download PDFInfo
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- CN102698557B CN102698557B CN201210220773.1A CN201210220773A CN102698557B CN 102698557 B CN102698557 B CN 102698557B CN 201210220773 A CN201210220773 A CN 201210220773A CN 102698557 B CN102698557 B CN 102698557B
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Abstract
The invention relates to an electrostatic spraying and dust-removing system. One end of a shell is an inlet of a dust-removing system while the other end of the shell is an outlet of the dust-removing system; an air flow distributor, an electrostatic spraying device, a filtering dust-collecting and washing device and a water separator are arranged in the shell orderly from the inlet to the outlet; at least one atomizing nozzle is connected to a water supply pipe in the electrostatic spraying device, a high pressure static ring is arranged in front of each atomizing nozzle; the high pressure static ring is connected with a high pressure static generator at the outer part of the system through a lead; a filler is arranged in the filtering dust-collecting and washing device, and the upper part of the filler is provided with a water pouring distributor; the water pouring distributor is connected with a system external water supply pipe through a water pipe; and the bottom part of the filler is provided with a water collecting disk, and the water collecting disk is provided with a water draining pipe. The system can satisfy the dust removing requirement of grains in different sizes in air, and has a relatively good effect to filter the powder dust with the grain diameter being more than 0.1 micro meters.
Description
Technical field
The present invention relates to a kind of electrostatic spray dust pelletizing system, relate to air cleaning and filtering and cleaning technique field.
Background technology
Domestic at present, airborne particulate pollutes and day by day causes people to pay close attention to, and also causes country to pay attention to, while bulky grain particle diameter dust removal requirement, the particles thing of PM10, PM2.5 size is in a lot of local introducing Air Quality Evaluation scope, and granule particle diameter filtering requirement is also improving day by day.Epidemiological study shows, crowd's M & M and Atmospheric particulates (PM) concentration exist significant positive correlation.This correlation shows, migration outdoor enters indoor particle has significant impact to health.The a large amount of poisonous and harmful substance of air PM2.5 adsorption is to the health hazard of human body very large.The fine particle of less than 2.5 μm is then not easily stopped, directly can enter bronchus after being inhaled into human body, causes the disease comprising the aspects such as asthma, bronchitis and cardiovascular disease.These particles can also enter blood by bronchus and alveolar, and pernicious gas wherein, heavy metal etc. dissolve in blood, larger to the injury of health.
At present, dedusting generally uses electric precipitation, bag-type dusting and wet dust removal etc., and these devices are each defectiveness also.Easily there is airborne dust in electric precipitation, vibration dust-cleaning easily makes deduster go wrong, and filter efficiency is not high by resistivity effects own for some particle.Bag-type dusting is not suitable for caking property particle filtering and hygroscopicity dust-filtering.Wet dust removal water consumption is comparatively large, undesirable to granule particle diameter filter efficiency.
Summary of the invention
The invention discloses a kind of electrostatic spray dust pelletizing system, effectively can overcome easy airborne dust, the large filter efficiency of wet dust removal water consumption that existing electric precipitation exists low, especially to drawbacks such as granule particle diameter filter efficiency are poorer.The present invention can ensure that particle diameter dusty gas has good efficiency of dust collection on a large scale, not only avoids airborne dust, water consumption little, and also has higher filter efficiency to the small particle being less than PM2.5.
Technical solution of the present invention is achieved in that
A kind of electrostatic spray dust pelletizing system, comprises housing, is provided with air distributor successively in housing by import to outlet, electrostatic atomizer, filter control of dust wash mill and dehydrator, shell one end is set to dust pelletizing system import, the other end is set to dust pelletizing system outlet, it is characterized in that:
A) described electrostatic atomizer: feed pipe is connected with at least one atomizer, atomizer supplies water and is introduced from system by feed pipe, have a high-pressure electrostatic ring in each atomizer front, high-pressure electrostatic ring is connected with the HV generator of its exterior by wire;
B) described filtration control of dust wash mill: filter in control of dust wash mill and arrange filler, arrange trickle distributor above filler, the feed pipe that trickle distributor is introduced with its exterior is connected; Filler bottom is connected with earth connection, has water-collecting tray bottom filler, and water-collecting tray is provided with tapping pipe.
Described air distributor is a kind of airflow-distribution board, comprises orifice plate and shutter type distribution grid.
Described high-pressure electrostatic ring and atomizer spacing are between 10-30mm, and shower nozzle injection flow rate is adjustable, and electrostatic potential is adjustable between 10-50kV.
The distance of 400-1000mm is had between described electrostatic atomizer and filtration control of dust wash mill.
Filter control of dust wash mill trickle to be evenly sprayed on filler according to Action of Gravity Field, dust-contained airflow is trapped by water and filler.
Dust pelletizing system of the present invention can be used for the air cleaning of the aspects such as high temperature fume dust removal, dedusting particle size range is wide, owing to having electrostatic atomizer and filtering control of dust wash mill, by changing the spray amount of high-pressure electrostatic voltage and high-pressure atomization shower nozzle, meet the dust removal requirement of dissimilar particle, native system is not only high to less than 50 μm particles filter efficiencies, and also has higher filter efficiency to the superfine granule of 0.1 μm.This system overcomes the problem that in general electrostatic precipitation, some dust specific resistance is little, system can be in operation automatic pollutant removal, and dedusting can be run continuously.
Accompanying drawing explanation
Fig. 1 is electrostatic spray dust pelletizing system structural representation of the present invention;
Fig. 2 is electrostatic atomizer structural representation of the present invention;
Fig. 3 is that the present invention filters control of dust wash mill structural representation.
1, dust pelletizing system import, 2, housing, 3, air distributor, 4, electrostatic atomizer, 5, filter control of dust wash mill, 6, dehydrator, 7, dust pelletizing system outlet, 8, wire, 9, feed pipe one, 10, feed pipe two, 11, tapping pipe, 12, water-collecting tray, 13, earth connection, 14, spray pipe, 15, trickle distributor, 16, filler, 17, high-pressure electrostatic ring, 18, atomizer.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is described in detail.
A kind of electrostatic spray dust pelletizing system as shown in Figure 1, comprise housing 2, air distributor 3, electrostatic atomizer 4, filter control of dust wash mill 5 and dehydrator 6, shell one end is set to dust pelletizing system import 1, end is set to dust pelletizing system outlet 7, enclosure interior sets gradually air distributor 3, electrostatic atomizer 4, filters control of dust wash mill 5 and dehydrator 6; Electrostatic atomizer as shown in Figure 1 and Figure 2, feed pipe 1 is connected with at least one atomizer 18, atomizer supplies water and is introduced from system by feed pipe 1, have a high-pressure electrostatic ring 17 in each atomizer 18 front, the electrostatic of high-pressure electrostatic ring is connected with its exterior electrostatic generator by wire 8; Filter control of dust wash mill 5 as shown in Figure 1, Figure 3, filter in control of dust wash mill and arrange filler 16, filler bottom is connected with earth connection 13, and filler top is provided with trickle distributor 15, trickle distributor is connected with spray pipe 14, and the feed pipe 2 10 that spray pipe and its exterior are introduced is connected; There is water-collecting tray 12 bottom filler 16, water-collecting tray is provided with tapping pipe 11.Described air distributor is a kind of airflow-distribution board, comprises orifice plate and shutter type distribution grid.The spacing of described high-pressure electrostatic ring 17 and atomizer 18 is between 10-30mm, and shower nozzle injection flow rate is adjustable, and electrostatic potential is adjustable between 10-50kV.The distance of 400-1000mm is had between described electrostatic atomizer 4 and filtration control of dust wash mill 5.Described dehydrator 6 is the one in corrugated baffle, silk screen and Ball-type packing, in order to remove in dust removal process be with water smoke.
The concrete operation step of electrostatic spray dust pelletizing system dedusting is as follows:
1) first open the washing feed pipe 2 10 filtered in control of dust wash mill 5 to supply water, trickle distributor 15 starts to drench filler 16, ensures that filler wettability is good.
2) start high voltage electrostatic equipment, make whole high-pressure electrostatic ring 17 charged, then start spraying nozzle 18, shower nozzle sprays even water smoke, and water smoke covers whole enclosure interior duct cross-section.
3) start up system Fan Equipment, contaminated air is made to enter electrostatic spray dust pelletizing system from dust pelletizing system import 1, through air distributor 3, uniform stream is distributed, through electrostatic atomizer 4 and filtration control of dust wash mill 5, make grit etc. flow into water-collecting tray 12 together with water, discharged by sewage tapping pipe 11, air is through the moisture of dehydrator 6 except deentrainment, and the cleaned air after dust removal and filtration exports 7 transmitting systems from dust pelletizing system.
Claims (1)
1. an electrostatic spray dust pelletizing system, comprises a housing, by import to outlet, successively air distributor is installed in housing, electrostatic atomizer, filters control of dust wash mill and dehydrator, shell one end is set to dust pelletizing system import, and the other end is set to dust pelletizing system outlet, it is characterized in that:
A) described electrostatic atomizer: feed pipe is connected with at least one atomizer, atomizer supplies water and is introduced from system by feed pipe, have a high-pressure electrostatic ring in each atomizer front, high-pressure electrostatic ring is connected with the HV generator of its exterior by wire;
B) described filtration control of dust wash mill: filter in control of dust wash mill and arrange filler, arrange trickle distributor above filler, the feed pipe that trickle distributor is introduced with its exterior is connected; Filler bottom is connected with earth connection, has water-collecting tray bottom filler, and water-collecting tray is provided with tapping pipe;
C) described high-pressure electrostatic ring and atomizer spacing are between 10-30mm, and shower nozzle injection flow rate is adjustable, and electrostatic potential is adjustable between 10-50kV;
D) distance of 400-1000mm is had between described electrostatic atomizer and filtration control of dust wash mill.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210220773.1A CN102698557B (en) | 2012-06-29 | 2012-06-29 | Electrostatic spraying and dust-removing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210220773.1A CN102698557B (en) | 2012-06-29 | 2012-06-29 | Electrostatic spraying and dust-removing system |
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| Publication Number | Publication Date |
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| CN102698557A CN102698557A (en) | 2012-10-03 |
| CN102698557B true CN102698557B (en) | 2015-05-20 |
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| CN201210220773.1A Expired - Fee Related CN102698557B (en) | 2012-06-29 | 2012-06-29 | Electrostatic spraying and dust-removing system |
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Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103623668B (en) * | 2013-12-03 | 2016-04-06 | 湖州纳尼亚实业股份有限公司 | Multiple stage combination inclined tube-type forming machine waste gas wet electrostatic purifier |
| CN104258674B (en) * | 2014-09-22 | 2016-01-27 | 江苏大学 | A kind of array type electrostatic atomization ultra-thin micro-particle coalescence Apparatus and method for |
| CN104990166A (en) * | 2015-06-02 | 2015-10-21 | 陕西优斯达环境科技有限公司 | Efficient purifying and haze-removal fresh air machine |
| CN106678912A (en) * | 2016-12-19 | 2017-05-17 | 东南大学 | Zero-emission lampblack electrostatic coupling catalytic oxidation purification device and method |
| CN108514793B (en) * | 2018-04-09 | 2020-06-23 | 辽宁工程技术大学 | Gas-liquid mixing electrostatic spray dust removal and cooling device |
| CN109453914B (en) * | 2018-11-15 | 2020-12-22 | 李东林 | Box type non-discharge electrostatic fog coating device |
| CN113309600B (en) * | 2021-05-25 | 2022-11-01 | 中国煤炭科工集团太原研究院有限公司 | Tail gas purification device and explosion-proof diesel engine |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101327390A (en) * | 2008-07-21 | 2008-12-24 | 尤今 | Vertical type electrostatic type fume cleaning equipment |
| CN101455929A (en) * | 2008-12-11 | 2009-06-17 | 上海纳米技术及应用国家工程研究中心有限公司 | High wind-speed tunnel air electric dust-collection system |
| CN102416192A (en) * | 2011-09-30 | 2012-04-18 | 江苏大学 | Landfill air-cleaning system |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL1015635C2 (en) * | 2000-07-06 | 2002-01-08 | Korea Clean Air System Co | Air cleaning device for removing air pollution by using a water spray type dust collection system. |
| CN2573057Y (en) * | 2002-08-26 | 2003-09-17 | 胡继杰 | High-pressure water fog and filter screen dust-collecting apparatus |
| CN102179125A (en) * | 2011-01-28 | 2011-09-14 | 清华大学 | Method and device for removing dust in flue gas |
| CN202724945U (en) * | 2012-06-29 | 2013-02-13 | 上海理工大学 | Electrostatic spraying dust removing system |
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- 2012-06-29 CN CN201210220773.1A patent/CN102698557B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101327390A (en) * | 2008-07-21 | 2008-12-24 | 尤今 | Vertical type electrostatic type fume cleaning equipment |
| CN101455929A (en) * | 2008-12-11 | 2009-06-17 | 上海纳米技术及应用国家工程研究中心有限公司 | High wind-speed tunnel air electric dust-collection system |
| CN102416192A (en) * | 2011-09-30 | 2012-04-18 | 江苏大学 | Landfill air-cleaning system |
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| CN102698557A (en) | 2012-10-03 |
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| CB03 | Change of inventor or designer information |
Inventor after: Liu Jianhua Inventor after: Liu Zheng Inventor after: Wang Jinxin Inventor after: Wu Ji Inventor after: Wang Jin Inventor after: Li Zhen Inventor after: Duan Wenshan Inventor after: Zhao Luping Inventor after: Niu Zhen Inventor after: Zhang Zhitong Inventor after: Yang Ning Inventor after: Zhao Kai Inventor before: Liu Jianhua Inventor before: Wang Jin Inventor before: Li Zhen Inventor before: Yuan Huan Inventor before: Guo Wei Inventor before: Li Wei Inventor before: Wang Yasi Inventor before: Shen Xiaobin |
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Free format text: CORRECT: INVENTOR; FROM: LIU JIANHUA WANG JIN LI ZHEN YUAN YUAN GUO WEI LI WEI WANG YASI SHEN XIAOBIN TO: LIU JIANHUA WANG JIN LI ZHEN DUAN WENSHAN ZHAO LUPING NIU ZHEN ZHANG ZHITONG YANG NING ZHAO KAI LIU ZHENG WANG JINXIN WU JI |
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Granted publication date: 20150520 Termination date: 20170629 |