CN104043320A - Method for treatment of indoor air pollution by combination of photocatalytic plasma and ultrasonic - Google Patents
Method for treatment of indoor air pollution by combination of photocatalytic plasma and ultrasonic Download PDFInfo
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- CN104043320A CN104043320A CN201410194933.9A CN201410194933A CN104043320A CN 104043320 A CN104043320 A CN 104043320A CN 201410194933 A CN201410194933 A CN 201410194933A CN 104043320 A CN104043320 A CN 104043320A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The invention discloses a method for treatment of indoor air pollution by combination of photocatalytic plasma and ultrasonic. The method includes the following steps: 1, a plasma discharge reactor is used to produce plasma free radicals, a strong electric field and ultraviolet light; 2, PM2.5 is absorbed through the strong electric; 3, the plasma free radicals are harmlessly treated by reaction of the plasma free radicals and VOCs (volatile organic chemcials) in the air; 4, incompletely reacted VOCs is further reacted in the presence of a TiO2 photocatalyst; 5, by-products NOx and O3 produced by the reaction are decomposed by a safe catalyst; 6, water or non-toxic organic absorbent and tail gas are mixed fully by an ultrasonic reactor, and fully react in a filling area, and remaining particles and VOCs are left in the organic absorbent; and 7, a tourmaline loaded nano titanium dioxide filler is used in the filling area. The method has the advantages of low energy consumption, small occupation of land, low noise, wide application range, and safe and reliable operation.
Description
Technical field
The present invention relates to a kind of nano-photo catalytic corona plasma and process the method for indoor air pollutants in conjunction with ultrasonic wave organic matter absorption techniques, belong to atmosphere and administer technical field.
Background technology
Along with the air pollution day by day increasing the weight of, the degree that haze occurs is more and more higher, and frequency is more and more faster, and the duration is more and more longer, and PM2.5, as the important indicator of haze, directly affects people's living safety and quality.PM2.5 refers to that the particle of diameter≤2.5 in atmosphere micron is also referred to as entering lung particle.It has a significant impact air quality and visibility etc.PM2.5 because particle diameter is little, specific area greatly, is easily adhered to various hazardous contaminants, can directly enter in human body alveolar, therefore health is produced to serious threat.Because PM2.5 particle diameter is little, be difficult to fall from sedimentation or by rain drop erosion, therefore in air, be difficult to be removed.
Volatile organic matter VOCs is equally also one of major reason of haze generation, and airborne VOCs produces reaction and forms secondary pollution generation photochemical fog under the irradiation of sunshine, has strong impulse, toxicity, carcinogenicity.
Present stage only has 2 kinds in the indoor method that can effectively process PM2.5, and one is to use HEPA to filter; Another kind is to utilize anion to make PM2.5 particle form heavy ion sedimentation.But these two kinds of methods respectively have drawback.
1, use HEPA to filter, need the frequent HEPA of replacing, therefore cost of use costliness, HEPA changes and can cause not in time filter opening to stop up, and the HEPA simultaneously polluting can grow a large amount of microorganisms, becomes new pollution sources.
2, use anion to remove PM2.5, PM2.5 particle does not eliminate from environment, but is adsorbed in a large number indoor body surface, causes house dust to increase, and easily causes the other diseases such as allergy, asthma.
The VOCs treatment technology that present stage can be used in indoor environment only has charcoal absorption and photocatalysis technology, when long-time use, adsorption effect of activated carbon in water is poor, photocatalysis technology is because catalyst mainly activates and produces free electron and electron hole by ultraviolet light, and therefore degradation efficiency is very low.
Summary of the invention
The object of the invention is to propose a kind of air pollution treatment technology that is applicable to indoor environment.By using DC high voltage electric field that PM2.5 particle is collected on electrode, use the free radical of high pressure streamer discharge generation to process indoor VOCs, and carry out photocatalytic degradation by the ultraviolet light of discharge generation, to after water or the atomization of organic matter absorbent, mix with pollutant by ultrasonic wave, fully react at tourmaline load nano-titanium dioxide filling surface, the static behaviour that utilizes tourmaline to have, fully adsorbs residual contamination thing, and carries out catalytic oxidation.Accessory substance NOx and the O of exoelectrical reaction
3pass through MnO
2safe catalyst is removed.It is high that this method overcomes prior art cost of use, easily causes secondary pollution, the problem of poor processing effect.
A kind of improvement method of room air pollution, it is characterized in that comprising the following steps: blower fan is introduced air in discharge reactor, the module composition that discharge reactor is made up of bipolar needle electrode and nano titanic oxide catalyst net, air passes through MnO in discharge reactor outlet
2safe catalyst, then after mixing with the water smoke of ultrasonic wave formation, enter fully reaction in filler, finally get back to indoor.
(1)use high direct voltage alternating expression bipolar needle electrode streamer-discahrge reactor, contaminated air is passed in discharge reactor, regulation voltage makes the anodal stable streamer that forms.
(2)the high energy electron bombardment air molecule that electrion produces makes gas band electric forming plasma, thereby being combined with plasma, contaminant particle (particularly PM2.5 particle) forms heavy ion, heavy ion moves to electrode under the effect of highfield, be attracted on electrode, needle plate electrode, due in the electric discharge of pin end, can be avoided the impact of electrode dust stratification.
(3)air is by rear plasma, hydroxyl radical free radical and the ozone etc. of forming of high energy electron bombardment, and VOCs can react and be eliminated with these materials.
(4)high pressure streamer-discahrge can produce strong ultraviolet light, and VOCs is subject to UV-irradiation after being adsorbed to photocatalyst surface, and photocatalyst surface forms electron hole, has strong oxidizing property, can oxidation Decomposition VOCs.
(5)owing to there being a large amount of nitrogen in air, when electric discharge, also can form NO
2and O
3, these accessory substances pass through MnO
2safe catalyst is eliminated.
(6)remain untreated fall PM2.5 particle and after the organic solvent water smoke that produces of VOCs and ultrasound reactor mixes, enter packing area and react.Tourmaline appendix nano titanium oxide filler has very strong surface electrostatic, and adsorptivity is strong, and therefore residual contamination thing and water smoke are adsorbed to filling surface and fully react.
Brief description of the drawings
Fig. 1 is discharge reactor electrode pack module front view.
Fig. 2 is that the axles such as discharge reactor electrode pack module are surveyed view.
Detailed description of the invention
Air is introduced in streamer-discahrge reactor by blower fan, and reactor uses high-voltage DC power supply, and both positive and negative polarity is needle plate electrode, and the pin of both positive and negative polarity is staggered.Needle point 3 is 2 ~ 5cm to the distance of another utmost point pole plate 1, needle point 3 spacing 2 ~ 4cm on same electrode, and voltage swing is for being as the criterion the anodal streamer-discahrge that occurs.
Discharge reactor has modularization, and each module is made up of multi-group electrode plate, and what wherein pin number was more is positive plate 1, and what pin number was less is negative plate 2, and module is imported and exported two ends nano titanic oxide catalyst net 4.
In the time that air passes through discharge reactor, air molecule is by the rear plasma that forms of high energy electron bombardment, these high energy particle positively chargeds or negative point, can attract the particle of opposed polarity to form heavy ion, PM2.5 particle volume is increased, electric charge strengthens, and moves on other end electrode and settle down under the effect of highfield.
On the plate of needle plate electrode 1,2, have layer of titanium dioxide coating, the ultraviolet light that can absorb exoelectrical reaction generation carries out photocatalysis oxidation reaction, imports and exports and all has one deck nano titanium dioxide photocatalyst net at each group of electrode.
VOCs can be subject to exoelectrical reaction generation-OH base ,-O base, O after entering reactor
3effect Deng strong oxidizer is decomposed, and due to the ultraviolet ray excited photochemical catalyst of discharge generation, forms electron hole on catalyst gauze simultaneously, and electron hole has strong oxidizing property, can decompose VOCs.
Owing to also there being N in air
2and NOx, therefore also can produce side reaction
3O
2(high pressure) → 2O
3
N
2+O
2→2NO
2NO+O
2→2NO
2
NO+O
3→NO
2+O
2
O
3and NO
2it is all harmful material.
When air passes through MnO in discharge reactor exit
2safe catalysis net, MnO
2can be by O
3be converted into O
2, by NO
2be converted into NO
3 -.
When air mixes by the organic matter absorbent water smoke producing with ultrasound reactor after safe catalysis net, enter packing area, tourmaline appendix nano titanium oxide filler has very strong surface electrostatic meeting adsorbing metal ions, charged dust etc., therefore pollutant fully reacts at filling surface with absorbent, remaining PM2.5 particulate and VOCs is absorbed after agent absorbs and is retained down by filler.
Claims (8)
1. photocatalysis plasma body, in conjunction with an air-polluting method in ultrasonic wave process chamber, is characterized in that: comprise the following steps,
(1) utilize DC bipolar pin electrode discharge of plasma in low temperature reactor to produce plasma free radical, highfield and ultraviolet light;
(2) the high energy electron bombardment air molecule while utilizing discharge reactor to produce streamer, makes air molecule ionization, forms plasma, also can form a large amount of-OH, H simultaneously
2o
2, O
3strong free radical;
(3) utilize the strong oxidizing property that the strong free radical of discharge generation has to decompose VOCs;
(4) ionized air and the PM2.5 particle formation heavy ion that can attract each other, heavy ion is finally caught by electrode to electrode movement under highfield effect, thereby separates from air;
(5) when discharge reactor produces streamer, can produce ultraviolet light, ultraviolet light meeting exciting light catalyst, forms electron hole, and the electron hole of formation has strong oxidizing property;
(6) after a part of VOCs is adsorbed by nano-photocatalyst, on catalyst, be degraded into harmless carbon dioxide and water;
(7) exoelectrical reaction also can form accessory substance NOx and O
3, at MnO
2under the effect of safe catalyst, be broken off;
(8) ultrasound reactor, by mixing with tail gas after water or the atomization of organic matter absorbent, enters packing area jointly, after the abundant mixed dissolution of filling surface, is held back and separates by filler, finally makes to export emission compliance.
2. in method according to claim 1, it is characterized in that discharge reactor uses DC high-voltage power supply, positive source connects anode plate, power cathode connects negative plates, and pole plate is needle plate electrode, and positive and negative pin electrode is staggered.
3. in method according to claim 1, it is characterized in that supply voltage just makes anodal streamer-discahrge, the just very more battery lead plate of pin number of forming.
4. according to claim 1 in method, it is characterized in that being coated with nano titanic oxide catalyst on both positive and negative polarity battery lead plate.
5. in method according to claim 1, it is characterized in that discharge reactor is made up of several equirotal electrode pack modules, modular electrode group is by several staggered to positive and negative needle plate electrode, and photochemical catalyst net is equipped with at electrode group two ends.
6. in method according to claim 1, it is characterized in that discharge reactor outlet is equipped with MnO
2catalyst.
7. in method according to claim 1, it is characterized in that mixing with air after ultrasonic atomized water or organic matter absorbent.
8. in method according to claim 1, it is characterized in that the filler using is granular tourmaline appendix nano titanium oxide.
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Cited By (14)
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CN103968466A (en) * | 2014-05-20 | 2014-08-06 | 郑巍 | Indoor air processing technology and device |
CN104923060A (en) * | 2015-04-21 | 2015-09-23 | 江苏大学 | VOCs removing method based on free radical advanced oxidation |
CN105130046A (en) * | 2015-08-13 | 2015-12-09 | 南通河海大学海洋与近海工程研究院 | Plasma and ultrasonic and catalysis combined cascading style water treatment device |
CN105233641A (en) * | 2015-10-21 | 2016-01-13 | 中国科学院北京综合研究中心 | Deep purifying method and device for dioxin and mercury which are generated in waste incineration |
CN106051918A (en) * | 2016-07-05 | 2016-10-26 | 北京航天爱锐科技有限责任公司 | Plasma air purification device |
CN106422699A (en) * | 2016-08-29 | 2017-02-22 | 浙江工业大学 | Method and device for coupling and biologically purifying VOCs under optical/thermal double-driving catalysis |
CN106890552A (en) * | 2017-03-13 | 2017-06-27 | 苏州盟力环境科技有限公司 | A kind of plasma gas processing unit |
CN107149857A (en) * | 2016-03-02 | 2017-09-12 | 北京大学 | Multi-layer planar corona low temperature plasma air cleaning unit |
CN107174879A (en) * | 2017-04-18 | 2017-09-19 | 上海英宇环保科技有限公司 | A kind of plasma air purifier |
CN109882878A (en) * | 2018-04-14 | 2019-06-14 | 青岛科技大学 | A kind of intelligent flue gas UTILIZATION OF VESIDUAL HEAT IN and its flue gas pollutant processing system |
CN109882877A (en) * | 2018-04-14 | 2019-06-14 | 青岛科技大学 | A kind of fume afterheat utilizes and its automatically controls pollutant system |
CN111111442A (en) * | 2019-12-30 | 2020-05-08 | 长安大学 | Long-afterglow automobile exhaust purification coating and preparation method and application thereof |
CN112413784A (en) * | 2020-11-27 | 2021-02-26 | 上海交通大学 | Portable multifunctional air purification method and device |
CN117628629A (en) * | 2024-01-24 | 2024-03-01 | 泉州市奔腾科技有限责任公司 | Air purifying equipment |
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JP2008194670A (en) * | 2007-01-15 | 2008-08-28 | Yamatake Corp | Gas treatment apparatus |
CN101367031A (en) * | 2008-09-12 | 2009-02-18 | 江苏大学 | Apparatus and method for generating hydroxyl radical with supersonic wave cooperated dense ionization electric discharge |
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Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103968466A (en) * | 2014-05-20 | 2014-08-06 | 郑巍 | Indoor air processing technology and device |
CN104923060A (en) * | 2015-04-21 | 2015-09-23 | 江苏大学 | VOCs removing method based on free radical advanced oxidation |
CN105130046A (en) * | 2015-08-13 | 2015-12-09 | 南通河海大学海洋与近海工程研究院 | Plasma and ultrasonic and catalysis combined cascading style water treatment device |
CN105233641A (en) * | 2015-10-21 | 2016-01-13 | 中国科学院北京综合研究中心 | Deep purifying method and device for dioxin and mercury which are generated in waste incineration |
CN107149857A (en) * | 2016-03-02 | 2017-09-12 | 北京大学 | Multi-layer planar corona low temperature plasma air cleaning unit |
CN106051918B (en) * | 2016-07-05 | 2022-05-20 | 北京航天爱锐科技有限责任公司 | Plasma air purification device |
CN106051918A (en) * | 2016-07-05 | 2016-10-26 | 北京航天爱锐科技有限责任公司 | Plasma air purification device |
CN106422699A (en) * | 2016-08-29 | 2017-02-22 | 浙江工业大学 | Method and device for coupling and biologically purifying VOCs under optical/thermal double-driving catalysis |
CN106890552A (en) * | 2017-03-13 | 2017-06-27 | 苏州盟力环境科技有限公司 | A kind of plasma gas processing unit |
CN107174879A (en) * | 2017-04-18 | 2017-09-19 | 上海英宇环保科技有限公司 | A kind of plasma air purifier |
CN109882877A (en) * | 2018-04-14 | 2019-06-14 | 青岛科技大学 | A kind of fume afterheat utilizes and its automatically controls pollutant system |
CN109882878A (en) * | 2018-04-14 | 2019-06-14 | 青岛科技大学 | A kind of intelligent flue gas UTILIZATION OF VESIDUAL HEAT IN and its flue gas pollutant processing system |
CN111111442A (en) * | 2019-12-30 | 2020-05-08 | 长安大学 | Long-afterglow automobile exhaust purification coating and preparation method and application thereof |
CN112413784A (en) * | 2020-11-27 | 2021-02-26 | 上海交通大学 | Portable multifunctional air purification method and device |
CN117628629A (en) * | 2024-01-24 | 2024-03-01 | 泉州市奔腾科技有限责任公司 | Air purifying equipment |
CN117628629B (en) * | 2024-01-24 | 2024-04-02 | 泉州市奔腾科技有限责任公司 | Air purifying equipment |
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Inventor after: Zheng Wei Inventor after: Zhao Ning Inventor after: Xiao Ling Inventor after: Li Changguo Inventor before: Zheng Wei Inventor before: Xiao Ling Inventor before: Li Changguo |
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