CN206890693U - A kind of integrated combined air air purifying apparatus - Google Patents
A kind of integrated combined air air purifying apparatus Download PDFInfo
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- CN206890693U CN206890693U CN201720464317.XU CN201720464317U CN206890693U CN 206890693 U CN206890693 U CN 206890693U CN 201720464317 U CN201720464317 U CN 201720464317U CN 206890693 U CN206890693 U CN 206890693U
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Abstract
Technical field of air purification is the utility model is related to, especially a kind of integrated combined air air purifying apparatus.It include air-out net cylinder, sleeve in the ozone catalytic net cylinder in air-out net cylinder, sleeve in the net cylinder of gathering dust in ozone catalytic net cylinder, be arranged in and gather dust photochemical catalyst electrode in net cylinder and emergent ray is irradiated in ultraviolet source on photochemical catalyst electrode, activated carbon granule is filled with the gap space that air-out net cylinder is formed with ozone catalytic net cylinder, net cylinder of gathering dust is grounded, and negative high voltage voltage is loaded with photochemical catalyst electrode.The purification techniques such as plasma dedusting, plasma VOCs decomposition, photocatalysis VOCs decomposition and ozone decomposed are integrated and discharged using negative high voltage by the utility model on process structure, the detergent power of whole purifier can not only be strengthened, reduce the generation of harmful substance, and the usage amount for the consumptive material for needing to change and long-term use of maintenance cost are greatly reduced, it is truly realized and transformation of the transfer techniques to purification degradation technique is collected by traditional to pollutant.
Description
Technical field
Technical field of air purification is the utility model is related to, especially a kind of integrated combined air air purifying apparatus.
Background technology
With the deterioration of air quality, haze weather phenomenon occur increasing (such as the northern area of China haze weather
It is presented go out the phenomenon that increasingly aggravates), directly jeopardize the health of people, how to ensure that people can live in an air
It is major issue urgently to be resolved hurrily at present in the preferable environment of quality;And capital equipment of the air purifier as purification air,
Increasingly favored by people.At present, the targeted target contaminant of air purifier mainly has two classes:One kind is tool
There is the particulate matter of certain particle diameter, mainly including PM10, PM2.5, pollen, airborne dust, dust etc.;Another kind of deposited with molecular size
Gaseous contaminant, wherein, be most the formaldehyde distributed in finishing material or furniture by people's attention, meanwhile, also have
Some gaseous inorganic oxides and the VOCs of other compositions etc..In industry, usually using to the particle using PM2.5 as representative
Thing and to by the gaseous contamination that represents of formaldehyde as clean-up effect quantitative assessment is carried out to the performance of a clarifier as index.
In the prior art, mainly there are filtering type and net two kinds of the formula of electricity for the purification style that particulate matter is taken.
Wherein, filtering type is the particulate matter intercepting system formed with coarse filtration, refined filtration, ultrafiltration HEPA films etc.;And the net formula of electricity
Refer to carry out absorption interception to particulate matter using electrostatic dust collection equipment.Filter screen needs generally there are using the clarifier of filtering type
The defects of periodic replacement, its long-term use of cost are higher.And the clarifier of the net formula of electricity is used typically to be discharged using positive high voltage
Technology and negative high voltage discharge technology, when using positive high voltage discharge technology, the operating voltage of the high voltage power supply of clarifier is general not
9KV is can exceed that, the purifying property that this is resulted in for particulate matter is not ideal enough, i.e.,:Particulate matter CADR values are not high;It is meanwhile positive high
The defects of electricity also has one to become apparent is pressed to be:Caused cation can overflow with the circulation of air in positive high voltage electric discharge
Go out, and the cation overflowed has harm to the health of human body.Compared with the clarifier of positive high voltage electric discharge, negative high voltage electric discharge
During although clarifier is not in drawbacks described above, but negative high voltage discharges, its ozone output can be more smelly than what positive high voltage discharged
Oxygen yield is much higher, and ozone content is too high still to damage to the health of human body.
Mainly there are absorption type, plasma for purification formula, photocatalysis formula three for the purification style that gaseous contaminant is taken
Kind.
Wherein, the clarifier of absorption type generally requires configuration active carbon filter screen or filter core mainly using activated carbon as adsorbent,
The removal of gaseous contaminant relies primarily on charcoal absorption performance, on the one hand the adsorption effect of activated carbon depends on the absorption of itself
Ability, on the other hand can be different because of the environmental factor at activated carbon, and target affinity pollutant is in environmental system
Concentration, partial pressure can also influence adsorption equilibrium concentration of the activated carbon to the pollutant, when the adsorption equilibrium concentration of activated carbon reaches one
No longer pollutant is adsorbed when determining degree, but when environmental contaminants concentration reduces because of other influences factor, activated carbon
Target contaminant equilibrium concentration can be declined automatically, activated carbon can the spontaneous pollutant being adsorbed to Environment release.Therefore, it is living
Property charcoal is both the adsorbent of indoor air pollutants, it is also possible to as the pollution sources of clean indoor environment.Due in clarifier
The limited amount of activated carbon, it is therefore desirable to multiple filter membrane, filter screen and activated carbon are carried out in the whole life cycle of clarifier
Change, higher requirement is proposed to the structure of whole equipment, and add the risk of clarifier damage and long-term use of cost.
Plasma for purification formula clarifier can simultaneously particulate matter and gaseous contaminant, the purification to particulate matter is wide
Well known electrostatic precipitator technology, and the purification to gaseous contaminant mainly for target contaminant be VOCs, it purifies former
Reason is exactly substantially catalytic purification, is on the one hand during plasma is produced, electrion produces moment high-energy, beats
The chemical bond of some pernicious gas molecules is opened, it is resolved into harmless molecule;On the other hand it is comprising substantial amounts of in plasma
High energy electron, ion, excited state particle and the free radical isoreactivity ion with strong oxidizing property, the average energy of these active ions
Amount is above the bond energy of gas molecule, when they and pernicious gas molecule collide, can open the chemical bond of gas molecule, together
When can also produce substantial amounts of OH, HO2, the free radical such as O and the extremely strong ozone of oxidisability, these oxidizing substances with it is harmful
Chemical reaction occurs for gas molecule so as to generate harmless products.
Photocatalysis formula clarifier is then to trigger and promote photocatalysis oxidation reaction by light irradiation photochemical catalyst, is realized organic
The decomposition of thing, it mainly includes four courses of reaction:First, the generation in photoinduced electron and hole;2nd, O2、H2O and organic matter are being urged
Agent surface attachment;3rd, the generation of oxidant;4th, the catalytic decomposition of organic matter.Must be in light on general such air purifier
The leading portion configuration particulate matter of catalytic process intercepts filter screen, in case light source or photocatalyst surface by Particulate Pollution, cause light to be urged
Change failure.
Utility model content
For above-mentioned the shortcomings of the prior art, the purpose of this utility model is to provide one kind by plasma dedusting
The combined type that technology, plasma decomposing, purifying technology, photocatalysis technology and ozone decomposed technology integrate in structure
Air purifier.
To achieve these goals, the utility model adopts the following technical scheme that:
A kind of integrated combined air air purifying apparatus, it includes a bottom end opening and the air-out net cylinder of top closure, one
Sleeve in be coaxially distributed in air-out net cylinder and with air-out net cylinder ozone catalytic net cylinder, a sleeve in ozone catalytic net cylinder and with
Net cylinder that what ozone catalytic net cylinder was coaxially distributed gather dust, one are arranged in the photocatalysis electricity to gather dust in net cylinder along the axis for net cylinder of gathering dust
Pole and one be placed in and gather dust in net cylinder and emergent ray is irradiated in ultraviolet source on photochemical catalyst electrode, the air-out net cylinder with
Activated carbon granule, the net cylinder ground connection of gathering dust, the photocatalysis electricity are filled with the gap space that ozone catalytic net cylinder is formed
Negative high voltage voltage is loaded with extremely.
Wherein, preferred scheme is:The photochemical catalyst electrode includes one and is distributed and is loaded with negative along the axis for net cylinder of gathering dust
The electrode supporting bar of high tension voltage, it is placed in the top ends for net cylinder of gathering dust and is linked as the top of electrode supporting bar and net cylinder of gathering dust
The upper ventilation insulating flange of one, it is placed in the bottom for net cylinder of gathering dust and is linked as the bottom of electrode supporting bar and net cylinder of gathering dust
If lower the ventilation insulating flange and dry plate of one are equally spacedly serially connected with electrode supporting bar and electrically connected with electrode supporting bar
Photochemical catalyst electrode piece, the emergent ray of the ultraviolet source is irradiated on photochemical catalyst electrode piece.
Wherein, preferred scheme is:The electrode supporting bar includes an inner bracing piece, an equidistant sleeve, on one insulator and
Insulator once, the inner bracing piece are distributed through equidistant sleeve, and the top of the inner bracing piece is inserted by upper insulator
Be placed on ventilation insulating flange in, bottom by lower insulator sleeve in lower insulating flange;The equidistant sleeve clamping is in upper
It is pre- that one is also set between insulator and lower insulator, and on the inner bracing piece and between upper insulator and equidistant sleeve
Pressing spring, if photochemical catalyst electrode piece described in dry plate is integrated by equidistant sleeve concatenation, and the photochemical catalyst electrode piece with it is equidistant
Sleeve electrically connects.
Wherein, preferred scheme is:The photochemical catalyst electrode piece includes chip carrier and is coated on the surface of chip carrier
On layers of photo-catalytic material, the layers of photo-catalytic material is titanium dioxide or the photocatalyst mixture containing titanium dioxide.
Wherein, preferred scheme is:The photochemical catalyst electrode piece is the disc-shaped structure or edge that perisporium is smooth arc-shaped surface
Disc-shaped structure with prickle, formed between each point of discharge of the photochemical catalyst electrode piece and the inwall for net cylinder of gathering dust
Heteropole spacing it is impartial, and the heteropole spacing is 20mm-100mm.
Wherein, preferred scheme is:Several mutual circular array distributions are offered on the photochemical catalyst electrode piece
Ventilating opening, the ultraviolet source seat divulge information on flange or are installed in the bottom of electrode supporting bar located at lower insulation.
Wherein, preferred scheme is:The ozone catalytic net cylinder includes the bearing tube enclosed by carbon fiber felt and born
The ozone catalyst being loaded on bearing tube, the ozone catalyst are manganese, cobalt, copper, iron, nickel, silver, palladium, rhodium, platinum and its oxide
In one or more.
Wherein, preferred scheme is:The net cylinder of gathering dust by percent opening is 20%-50%, aperture 1mm-3mm, thickness are
0.5mm 304 stainless steel plates twist shaping.
Wherein, preferred scheme is:It also includes the air inlet mechanism of a bottom nozzle side for being installed in air-out net cylinder, the air intake
Mechanism is connected with the bottom nozzle for net cylinder of gathering dust including a top ports and the air intake barrel shell of screen pack is equiped with bottom nozzle, is placed in
The top of screen pack and be spaced apart with screen pack deflector, be arranged at deflector profile edge fresh air inlet, be placed in and lead
Pressure fan above flowing plate and it is placed in the negative high-voltage generator electrically connected in air intake barrel shell and with photochemical catalyst electrode.
As a result of such scheme, the utility model is by plasma dedusting, plasma VOCs is decomposed, photocatalysis
The purification techniques such as VOCs decomposition and ozone decomposed is integrated on process structure and discharged using negative high voltage, not only may be used
To strengthen the detergent power of whole purifier, reduce the generation of harmful substance, and greatly reduce the consumptive material for needing to change
Usage amount and long-term use of maintenance cost, be truly realized to pollutant by traditional collection transfer techniques to purification degraded
Shifts in technology.
Brief description of the drawings
Fig. 1 is the cross section structure schematic diagram of the utility model embodiment;
Fig. 2 is the Standard schematic diagram of the photochemical catalyst electrode of the utility model embodiment.
Embodiment
Embodiment of the present utility model is described in detail below in conjunction with accompanying drawing, but the utility model can be by right
It is required that the multitude of different ways for limiting and covering is implemented.
As depicted in figs. 1 and 2, a kind of integrated combined air air purifying apparatus that the present embodiment provides, it includes a bottom
The end opening and air-out net cylinder a of top closure, a sleeve are urged in air-out net cylinder a and with the air-out net cylinder a ozone being coaxially distributed
Change net cylinder b, a sleeve gathers dust in the net cylinder c that gathers dust coaxially being distributed in ozone catalytic net cylinder b and with ozone catalytic net cylinder b, an edge
Net cylinder c axis, which is arranged in the photochemical catalyst electrode d and one to gather dust in net cylinder c and is placed in, gathers dust in net cylinder c and emergent ray shines
Penetrate in the ultraviolet source e on photochemical catalyst electrode d, filled out in the gap space that air-out net cylinder a is formed with ozone catalytic net cylinder b
Filled with activated carbon granule f, and net cylinder c ground connection of gathering dust, and negative high voltage voltage is then loaded with photochemical catalyst electrode d.
Thus, by loading such as 5kv-35kv negative high voltage voltage on photochemical catalyst electrode d and the net cylinder c that will gather dust connects
Ground, unevenly corona field can be formed in the net cylinder c that gathers dust, can be in air by the cooperation between each function net cylinder
Pollutant component forms the structure mechanism of multilayer or multiple purifications, is specially:
Contaminated air will enter via the area of space close to photochemical catalyst electrode d first to gather dust in net cylinder c, in this area
Corona discharge effect in domain due to corona field can cause air to be ionized, so as to complete to include the strong oxidizing property of ozone from
By the generation of base, comprising VOCs (i.e.:Volatile organic matter) gaseous contaminant ionization and oxidative degradation, particulate matter it is charged etc.
Purification process;Particulate matter after charged can be in the presence of air-flow and corona field towards the direction motion for the net cylinder c that gathers dust, due to receiving
Dirt net cylinder c is connected with the earth, and for abundant charged particulate matter, net cylinder of gathering dust c is its positive pole, therefore electrically charged particle thing
It will in large quantities be deposited on and gather dust on net cylinder c, then discharge the negative electrical charge entrained by it, realize the major part to particulate matter herein
Collect;At the same time, the ultraviolet light that ultraviolet source e is projected passes through inwall, photochemical catalyst electrode d and the sky for the net cylinder c that gathers dust
It can be irradiated on photochemical catalyst electrode d after the multiple reflections of particulate matter in gas, to excite the photochemical catalyst on photochemical catalyst electrode d, and
Gaseous contaminant (especially VOCs gases, explaining description by taking VOCs gases as an example below) meeting in the case where not being ionized
The free movement in the space of purifier, it is decomposed (i.e. because it randomly can be collided with oxidizing species:VOCs points
Son be struck off after an electronics be in positively charged state), this part VOCs molecules can move to photochemical catalyst electrode d direction, logical
Cross after being contacted with the photochemical catalyst on photochemical catalyst electrode d surfaces and degrade, can largely ultimately generate such as titanium dioxide
The innocuous substances such as carbon, water, small part contains sulphur, the gas molecule of nitrogen then can enter activated carbon granule layer via the net cylinder c that gathers dust
In and finally adsorbed;And the ozone remained also can effectively be degraded in the presence of ozone catalytic net cylinder b.
Meanwhile utilize the activated carbon granule being filled in the gap space that air-out net cylinder a and ozone catalytic net cylinder b formed
F can form the active carbon filter core layer of an annular tubular in the periphery for the net cylinder c that gathers dust, to be functioned as follows to whole device:1、
Play a part of carrying out a certain degree of closing to the internal-response space of purifier, avoid ultraviolet light, energetic plasma
Leak, the purification process of air is completely restricted in the inside of purifier, it is not necessary to which worry impacts to external environment;2、
It can contain NOx, SO in product after part is nitrogenous, the VOCs pollutants of sulfur-bearing class decompose2Can be harmful to these Deng, activated carbon
Material is adsorbed, and reduces its harm to living environment;3rd, the caused ozone in purification process, although have passed through ozone
Net cylinder b degraded is catalyzed, but in order to which absolute guarantee's ozone influences thoroughly to be eliminated, activated carbon can adsorb the denier of residual
Ozone, adsorbed ozone will not be produced and appointed because the unstability of itself would generally be broken down into oxygen within 20-50 minutes
What secondary pollution.
The structure of device based on the present embodiment, it decomposes plasma dust separation technology, plasma VOCs net
Change technology, photocatalysis VOCs decomposing, purifyings technology and ozone decomposed purification techniques integrate on process structure, pass through
Using negative high voltage discharge technology, it not only can effectively strengthen the detergent power of whole purifier, reduce to greatest extent harmful
The generation of material, and the usage amount for the consumptive material for needing to change and long-term use of maintenance cost are greatly reduced, really realize
Transfer techniques are collected to the transformation for purifying degradation technique by traditional to pollutant.
To optimize photochemical catalyst electrode d structure, strengthen it and dismount the structural integrity after the convenience safeguarded and assembling
And stability, the photochemical catalyst electrode d of the present embodiment include one and are distributed along the axis for the net cylinder c that gathers dust and are loaded with negative high voltage voltage
Electrode supporting bar 10, be placed in the net cylinder c that gathers dust top ends and the top of electrode supporting bar 10 and the net cylinder c that gathers dust be linked as one
The upper ventilation insulating flange 20 of body, it is placed in the bottom for the net cylinder c that gathers dust and by the bottom of electrode supporting bar 10 and gathers dust net cylinder c
If lower the ventilation insulating flange 30 and dry plate that are connected as a single entity equally spacedly are serially connected with electrode supporting bar 10 and and electrode supporting
The photochemical catalyst electrode piece 40 that bar 10 electrically connects, ultraviolet source e emergent ray are irradiated on photochemical catalyst electrode piece 40.Thus,
Photochemical catalyst electrode d main body is consolidated in the case where not influenceing the air flow effect of device using ventilation insulating flange 20
Ground is assemblied in the inside of device, same come what is used as the support of photochemical catalyst electrode piece 40 and fixture by the use of electrode supporting bar 10
When, also negative high voltage voltage can be loaded by the phase photochemical catalyst electrode piece of electrode supporting bar 10.
For the structural stability for further enhancing photochemical catalyst electrode d structural compactness and being assembled in device, this reality
Apply the electrode supporting bar 10 of example include an inner bracing piece 11, an equidistant sleeve 12 and one made of such as polytetrafluoroethylene (PTFE) on
Insulator 13 and once insulator 14, inner bracing piece 11 is distributed through equidistant sleeve 12, and the top of inner bracing piece 11 passes through
The upper sleeve of insulator 13 in it is upper ventilation insulating flange 20 in, bottom by the lower sleeve of insulator 14 in lower insulating flange 30;And
Equidistant sleeve 12 is then held between insulator 13 and lower insulator 14, meanwhile, on inner bracing piece 11 and it is located at upper insulation
A pre-compressed spring 15 is also set between son 13 and equidistant sleeve 12, if dry plate photochemical catalyst electrode piece 40 is gone here and there by equidistant sleeve 12
One is connected in, and photochemical catalyst electrode piece 40 electrically connects with equidistant sleeve 12.Thus, insulator is being utilized by the two of inner bracing piece 11
End be individually fixed in corresponding to ventilation insulating flange on after, by upper insulator 13 to pre-compressed spring 15 be downwardly applied to compress
Effect, it is ensured that each building block can be fastened and is stably combined as a whole.
To ensure that photochemical catalyst electrode piece 40 will not be polluted by particulate pollutant, and ensure it to gaseous contaminant simultaneously
Effective degradation effect, the photochemical catalyst electrode piece 40 of the present embodiment include chip carrier and are coated on the surface of chip carrier
Layers of photo-catalytic material, layers of photo-catalytic material are titanium dioxide or the photocatalyst mixture containing titanium dioxide.Thus, in electrode
Surface coating layers of photo-catalytic material advantage be:Electrode surface is due to the characteristic of continuous discharge, it is ensured that it will not be by particle
Thing pollutes, and definitely clean environment is the premise of layers of photo-catalytic material continuous and effective work;Therefore, in the light of electrode surface coating
Catalyst need not individually consider that particulate matter on its issuable influence, can effectively improve whole purifier to such as completely
The clean-up effect of the gaseous contaminants such as VOCs.
To realize optimal dust removing effects and degradation effect, the photochemical catalyst electrode piece 40 of the present embodiment can be according to specific feelings
Condition uses disc-shaped structure or edge disc-shaped structure with prickle of the perisporium for smooth arc-shaped surface, meanwhile, photocatalysis electricity
The heteropole spacing formed between each point of discharge of pole piece 40 and the net cylinder c that gathers dust inwall is impartial, and heteropole spacing is preferably controlled
(edge character that certainly specific heteropole spacing can be according to photochemical catalyst electrode piece 40, electric discharge electricity are made in the range of 20mm-100mm
Pressure, purifying property, ozone control situation to determine).Thus, corona field discharge effect, particulate matter and gaseous contamination can be made
The clean-up effect of thing is more notable.
For the flow effect of air in intensifier, enable air to be sufficiently purified, opened on photochemical catalyst electrode piece 40
The ventilating opening 41 being distributed provided with several mutual circular arrays, and ultraviolet source e can then select seat as the case may be
Located at the lower mounting means to insulate on ventilation flange 30 or the mounting means being installed on the bottom of electrode supporting bar 10.Thus,
It can reduce the blocking and hinder to moving air of photochemical catalyst electrode piece 40 to greatest extent using ventilating opening 41, ensure in device
Air can be swimmingly flowed to complete corresponding clean-up effect in respective regions;Ultraviolet source e is arranged at entirely simultaneously
The lower section of device can avoid ultraviolet light light by device air inlet side leak and go out, so as to reduce ultraviolet light to device outside
The influence of environment.
Can effectively to be degraded to ozone, the secondary pollution of cancellation element to greatest extent, the present embodiment it is smelly
Oxygen catalysis net cylinder b includes the bearing tube enclosed by carbon fiber felt and the ozone catalyst being carried on bearing tube, ozone
The one or more that catalyst can be selected in manganese, cobalt, copper, iron, nickel, silver, palladium, rhodium, platinum and its oxide as the case may be.By
This, using bearing structure of the charcoal felt as ozone catalyst, plays a part of catalytic decomposition using ozone catalyst to ozone,
And the ozone for passing through ozone catalytic net cylinder b can be catalytically decomposed as oxygen, so as to effectively avoid easily going out because of leaking for ozone
The problem of existing secondary pollution.
As a preferred scheme, the net cylinder c that gathers dust of the present embodiment by percent opening is 20%-50%, aperture 1mm-
3mm, 304 stainless steel plates that thickness is 0.5mm twist shaping.Thus, the position of non-perforate can be used as gathering dust on net cylinder of gathering dust c
Face uses, and the position of perforate can then be used as ventilating surface use, so as to while the dust collection performance for the net cylinder c of ensureing to gather dust,
Also favourable condition is provided to reduce the making of whole device and maintenance cost.
To optimize the structure of whole device, the practical performance of enhancing device really, the device of the present embodiment to greatest extent
Also include the air inlet mechanism of a bottom nozzle side for being installed in air-out net cylinder c, air inlet mechanism includes a top ports and gathers dust net cylinder c's
Bottom nozzle be connected and be equiped with bottom nozzle the air intake barrel shell 60 of screen pack 50, be placed in screen pack 50 top and and screen pack
50 deflectors 70 being spaced apart, be arranged at deflector 70 profile edge fresh air inlet 80, be placed in giving for the top of deflector 70
Blower fan 90 and it is placed in the negative high-voltage generator 100 electrically connected in air intake barrel shell 60 and with photochemical catalyst electrode d.Thus, by right
Screen pack 50 and the setting of the arrangement relation of deflector 70, it may be such that contaminated air can first pass around filtering outside device
After the abundant filtering of net 50 (i.e.:After completing front end tentatively filtering) it is delivered to and is gathered dust in net cylinder c by pressure fan 90, to ensure device
To the follow-up dust separation effect of contaminated air.
Preferred embodiment of the present utility model is the foregoing is only, not thereby limits the scope of the claims of the present utility model,
Every equivalent structure made using the utility model specification and accompanying drawing content or equivalent flow conversion, or directly or indirectly fortune
Used in other related technical areas, similarly it is included in scope of patent protection of the present utility model.
Claims (9)
- A kind of 1. integrated combined air air purifying apparatus, it is characterised in that:It includes going out for a bottom end opening and top closure Wind net cylinder, a sleeve are in the ozone catalytic net cylinder being coaxially distributed in air-out net cylinder and with air-out net cylinder, a sleeve is in ozone catalytic The net cylinder of gathering dust that is distributed with ozone catalytic net cylinder in net cylinder and coaxially, one are arranged in along the axis for net cylinder of gathering dust gathers dust in net cylinder Photochemical catalyst electrode and one be placed in and gather dust in net cylinder and emergent ray is irradiated in ultraviolet source on photochemical catalyst electrode, it is described Activated carbon granule, the net cylinder ground connection of gathering dust, institute are filled with the gap space that air-out net cylinder is formed with ozone catalytic net cylinder State and negative high voltage voltage is loaded with photochemical catalyst electrode.
- A kind of 2. integrated combined air air purifying apparatus as claimed in claim 1, it is characterised in that:The photochemical catalyst electrode It is distributed including one along the axis for net cylinder of gathering dust and is loaded with the electrode supporting bar of negative high voltage voltage, is placed in the top for net cylinder of gathering dust In portion and by the top of electrode supporting bar and the upper ventilation insulating flange that net cylinder is connected as a single entity of gathering dust, the bottom for being placed in net cylinder of gathering dust If lower the ventilation insulating flange and dry plate that are connected as a single entity in portion and by the bottom of electrode supporting bar and net cylinder of gathering dust are equally spacedly The photochemical catalyst electrode piece for being serially connected with electrode supporting bar and being electrically connected with electrode supporting bar, the emergent ray of the ultraviolet source It is irradiated on photochemical catalyst electrode piece.
- A kind of 3. integrated combined air air purifying apparatus as claimed in claim 2, it is characterised in that:The electrode supporting bar Insulator including insulator on an inner bracing piece, an equidistant sleeve, one and once, the inner bracing piece is through equidistant sleeve point Cloth, and the top of the inner bracing piece by upper insulator sleeve in upper ventilation insulating flange, bottom inserted by lower insulator It is placed in lower insulating flange;The equidistant sleeve clamping between upper insulator and lower insulator, and on the inner bracing piece and A pre-compressed spring is also set between upper insulator and equidistant sleeve, if photochemical catalyst electrode piece is by equidistantly covering described in dry plate Cylinder concatenation is integrated, and the photochemical catalyst electrode piece electrically connects with equidistant sleeve.
- A kind of 4. integrated combined air air purifying apparatus as claimed in claim 2, it is characterised in that:The photochemical catalyst electrode Piece includes chip carrier and the layers of photo-catalytic material being coated on the surface of chip carrier, and the layers of photo-catalytic material is dioxy Change titanium or the photocatalyst mixture containing titanium dioxide.
- A kind of 5. integrated combined air air purifying apparatus as claimed in claim 2, it is characterised in that:The photochemical catalyst electrode Piece is the disc-shaped structure that the disc-shaped structure that perisporium is smooth arc-shaped surface or edge carry prickle, the photochemical catalyst electrode piece Each point of discharge and net cylinder of gathering dust inwall between the heteropole spacing that is formed it is impartial, and the heteropole spacing is 20mm- 100mm。
- A kind of 6. integrated combined air air purifying apparatus as claimed in claim 5, it is characterised in that:The photochemical catalyst electrode The ventilating opening of several mutual circular array distributions is offered on piece, the ultraviolet source seat is located at lower insulation ventilation method On orchid or it is installed in the bottom of electrode supporting bar.
- A kind of 7. integrated combined air air purifying apparatus as claimed in claim 1, it is characterised in that:The ozone catalytic net Cylinder includes the bearing tube enclosed by carbon fiber felt and the ozone catalyst being carried on bearing tube, the ozone catalyst For one kind in manganese, cobalt, copper, iron, nickel, silver, palladium, rhodium, platinum or its oxide.
- A kind of 8. integrated combined air air purifying apparatus as claimed in claim 1, it is characterised in that:It is described gather dust net cylinder by 304 stainless steel plates that percent opening is 20%-50%, aperture 1mm-3mm, thickness are 0.5mm twist shaping.
- A kind of 9. integrated combined air air purifying apparatus as any one of claim 1-8, it is characterised in that:It is also Include the air inlet mechanism of a bottom nozzle side for being installed in air-out net cylinder, the air inlet mechanism includes a top ports and net cylinder of gathering dust Bottom nozzle is connected and the air intake barrel shell of screen pack is equiped with bottom nozzle, is placed in the top of screen pack and is divided with screen pack interval The deflector of cloth, the fresh air inlet at profile edge for being arranged at deflector, the pressure fan that is placed in above deflector and it is placed in air intake The negative high-voltage generator electrically connected in barrel shell and with photochemical catalyst electrode.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106949561A (en) * | 2017-04-28 | 2017-07-14 | 深圳市力德诺华科技有限公司 | A kind of integrated combined air air purifying apparatus |
CN108273344A (en) * | 2018-03-13 | 2018-07-13 | 张世红 | A kind of integrated-type organic waste gas treatment device |
-
2017
- 2017-04-28 CN CN201720464317.XU patent/CN206890693U/en not_active Withdrawn - After Issue
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106949561A (en) * | 2017-04-28 | 2017-07-14 | 深圳市力德诺华科技有限公司 | A kind of integrated combined air air purifying apparatus |
CN108273344A (en) * | 2018-03-13 | 2018-07-13 | 张世红 | A kind of integrated-type organic waste gas treatment device |
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