CN103331088B - Electric light composite catalyzing gas conversion plant - Google Patents

Electric light composite catalyzing gas conversion plant Download PDF

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Publication number
CN103331088B
CN103331088B CN201310238543.2A CN201310238543A CN103331088B CN 103331088 B CN103331088 B CN 103331088B CN 201310238543 A CN201310238543 A CN 201310238543A CN 103331088 B CN103331088 B CN 103331088B
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China
Prior art keywords
vanes
electrode array
conversion plant
gas conversion
composite catalyzing
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Expired - Fee Related
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CN201310238543.2A
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Chinese (zh)
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CN103331088A (en
Inventor
夏越明
夏琦
毛茜倩
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Zhejiang Wacker Technology Co ltd
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Zhejiang Wacker Technology Co ltd
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Abstract

The present invention essentially discloses a kind of photoelectricity composite catalyzing gas conversion plant, comprise housing, in housing, be axially provided with quartz burner, ultraviolet lamp tube-surface be provided with fluorescent tube axis centered by, the catalysis electrode array of vanes of radially arranging and to electrode array of vanes.Two electrod-arrays intert together with one heart.Catalysis electrode array of vanes is connected independently electrode respectively with to electrode array of vanes.At housing two ends, air inlet and air outlet are set respectively.Catalyst coat is had at catalysis electrode blade surface.The present invention can be oxidized efficiently and remove the VOC in surrounding air, and it is finally converted into harmless carbon dioxide and water.

Description

Electric light composite catalyzing gas conversion plant
Technical field
The present invention relates to the gas catalysis oxidation technology under normal temperature, particularly relate to the conversion to poison, useless, harmful and imflammable gas and treatment technology, particularly about a kind of photoelectricity composite catalyzing gas conversion plant.
Background technology
Along with a large amount of exploitation and people's improving constantly housing need of real estate, increasing artificial material enters in daily life and working environment, as coating, the furniture that composite is made and ornament materials, all kinds of electric appliance casings that plastics are made etc.These artificial materials overwhelming majority have passed through chemical treatment, or in preparation process, have employed some chemicals, as solvent etc.These chemicals more or less have damaging effect to the health of human body.Although producer usually can on sale before carry out certain process, from product, get rid of the time that these chemicals often need extremely to grow completely.Even if nose can not be heard out completely, people are among the encirclement being still in number of chemical gas/vapor unconsciously.
Existing air clearing product, often based on filtering solid dust, does not possess the disposal ability to chemical gas.Some other is as charcoal absorption type clarifier, due to absorption selective and limit by capacity, often lack the detergent power of wide spectrum, and use cost is higher.In recent years, along with plasma oxidation, the development of the technology such as photochemical catalytic oxidation, some emerging air cleaning facilities start the ability possessing process pernicious gas.These technology have broad spectrum activity gas processing capability.But due to oxidated technology, the restriction of the conditions such as unit power consumption and volume, the gas transformation efficiency of these products is often lower.The present inventor is for this present situation, and design a kind of photoelectricity composite catalyzing gas conversion plant, this case produces thus.
Summary of the invention
The object of this invention is to provide a kind of photoelectricity composite catalyzing gas conversion plant, can be oxidized efficiently and remove the VOC in surrounding air, it is finally converted into harmless carbon dioxide and water.
To achieve these goals, the technical solution used in the present invention is as follows:
Photoelectricity composite catalyzing gas conversion plant, comprise housing, axially quartz burner is provided with in housing, ultraviolet lamp tube-surface be provided with fluorescent tube axis centered by, the catalysis electrode array of vanes of radially arranging and to electrode array of vanes, two electrod-arrays intert together with one heart, and catalysis electrode array of vanes is connected independently electrode respectively with to electrode array of vanes; At housing two ends, air inlet and air outlet are set respectively; Catalyst coat is had at catalysis electrode blade surface.
Described housing comprises the column of hollow, and covers air distribution cavity lid and the air collecting chamber lid at column two ends, arranges seal cover respectively in the outside of air distribution cavity lid and air collecting chamber lid; The inner surface of housing is provided with some with axis being parallel for fixed catalytic electrode array of vanes or the cutting to electrode blade.
The seal cover of described air distribution cavity lid and its side offers the circular hole inserted for quartz burner, there is the groove bottom for fixing quartz burner inside air collecting chamber lid.
Described is made up of independent metal sheet electrode array of vanes, and all there is ledge at its two ends, is socketed on the retainer ring of insulation respectively.
Described catalysis electrode array of vanes is made up of independent metal sheet, and all there is ledge at its two ends, connects on the locating ring of insulation respectively.
Described locating ring inner ring is enclosed within quartz burner, and outer ring is inserted solid for the jut of catalysis electrode blade; Described retainer ring inner ring is enclosed within the jut of catalysis electrode blade, and outer ring is for inserting solid to the jut of electrode blade.
The blade that described catalysis electrode blade is made up of metallic aluminium, zinc, vanadium, titanium, copper or other metal or alloy, the catalyst coat on its surface is semiconductor or ceramic coating; Coating composition can comprise oxide, metal particle, or both mixtures.
Described oxide comprises titanium dioxide, zinc oxide, tri-iron tetroxide, aluminium oxide etc.; Described metal comprises platinum, gold, copper, cobalt, nickel etc.Coating can be sintered by powder coated, or sol-gal process sintering.
Described is made up of aluminium or stainless steel electrode blade, surface application reflector layer.
There is a circle gas dispersion hole described air distribution cavity lid inside, the seal cover of air distribution cavity lid side has the air admission hole for connecting outside gas circuit.
There is a circle gas collection hole described air collecting chamber lid inside, the seal cover of air collecting chamber lid side has the venthole for connecting outside gas circuit.
After adopting technique scheme, while ultraviolet illumination, apply auxiliary electric field, generation free electron and hole are respectively to electric field two end motion, and therefore the probability of its compound can reduce, and ARL increases.Effective charge can move and be gathered in catalyst surface, and increase the contact probability with fluid media (medium), therefore catalytic conversion efficiency can significantly improve.
The present invention not only may be used for IAQ and controls, also can be used for commercial building and industrial premises air quality control, some civilian or industrial exhaust-gas treatment, and the technological processing for explosion protection feature of the imflammable gas of some particular surroundings, as gases such as ethene in the device in Gas in colliery and petrochemical industry.
Accompanying drawing explanation
Fig. 1 is present pre-ferred embodiments external structure schematic diagram one;
Fig. 2 is present pre-ferred embodiments external structure schematic diagram two;
Fig. 3 is present pre-ferred embodiments internal breakup schematic diagram;
Fig. 4 is present pre-ferred embodiments catalysis electrode array of vanes and the arrangement schematic cross-section to electrode array of vanes;
Fig. 5 is present pre-ferred embodiments catalysis electrode array of vanes and the mutual disengaging arrangement schematic diagram to electrode array of vanes;
Fig. 6 is the whole system schematic of present pre-ferred embodiments application.
Detailed description of the invention
By reference to the accompanying drawings, present pre-ferred embodiments is described in further details.
As depicted in figs. 1 and 2, first present pre-ferred embodiments is combined into the column of hollow by two panels arc-like sheet 20,21, be provided with air distribution cavity lid 31 and air collecting chamber lid 11 at the two ends of this column, loads onto seal cover 30,10 respectively in both outsides simultaneously.Gas flows into from air distribution cavity lid 31 one end, flows out from air collecting chamber lid 11 one end.
Column in the present invention can adopt single cylindrical structure also can adopt multiple combined-type, is similar in the present embodiment and lifts.Housing can by plastics, and pottery or other synthetic insulating material are made, and shell inner surface have cutting 211, for fixed catalytic electrode array of vanes 23 with to electrode array of vanes 24.
See Fig. 3, inner at hollow column, be coaxially arranged with quartz burner 25.The power connection part of ultraviolet lamp tube is in outside housing.There are two the radial electrode array of vanes that overlap centered by axis of a cylinder in column inside, composition graphs 4 simultaneously.First catalysis electrode array of vanes 23.Another is to electrode array of vanes 24.Two electrod-arrays intert together with one heart, and that is adjacent two panels blade is the blade of different motor.
Composition graphs 5, catalysis electrode array of vanes 23 is made up of independent metal sheet, all has ledge at its two ends, connects locating ring 15 and 33 respectively.Locating ring 15 and 33 is made up of insulating materials such as plastics or potteries, and its inner ring is enclosed within quartz burner 25, and also there is corresponding cutting its outer ring, for the jut at fixed catalytic electrode array of vanes 23 Leaf two ends.Catalysis electrode array of vanes 23 is also connected with the catalysis electrode 32 of ring-type near the ledge of air distribution cavity lid 31 simultaneously.
The blade of catalysis electrode array of vanes 23 can be made up of metallic aluminium, zinc, vanadium, titanium, copper or other metal or alloy.Layer of semiconductor or ceramic catalyst coating 233 is provided with at blade surface.Coating composition can comprise oxide, as titanium dioxide, zinc oxide, tri-iron tetroxide, aluminium oxide etc., or metal, as platinum, gold, copper etc., and above-mentioned several mixture.Coating can by powder coated and sinter, sol-gal process sintering or the method such as autoxidation sintering make.
Electrode array of vanes 24 is made up of independent metal sheet.Also there is ledge at its two ends, are connected and fixed ring 14,34 respectively.Retainer ring 14,34 is made up of the insulating materials such as plastics or pottery, and its inner ring is enclosed within outside the ledge of catalysis electrode array of vanes 23, and its outer ring has corresponding cutting equally, for the fixing jut to electrode array of vanes 24 Leaf two ends.
To electrode array of vanes 24 near air collecting chamber lid 11 ledge also with ring-type electrode 13 is connected.Can be made up of the material such as aluminium or stainless steel electrode array of vanes 24.Surface can apply reflector layer, also can not be coated with and only do any surface finish process, strengthens reflecting power.
As shown in Figure 4, Figure 5, catalysis electrode array of vanes 23 and to contactless between all blades of electrode array of vanes 24, can independently separate.
The air distribution cavity lid 31 of inlet end side in the present embodiment, there is the gas dispersion hole 311 of a circle circumferential arrangement its inside.There is a circular hole 302 at seal cover 30 center outside air distribution cavity lid 31.When changing quartz burner 25, quartz burner 25 can insert by circular hole 302 thus, and power connection part stays the surface of seal cover 30.Seal cover 30 separately there is an air admission hole 301, can be used for connecting outside gas circuit.
The air collecting chamber lid 11 of side, outlet side in the present embodiment, there is a circle gas collection hole 111 its inside.There is the groove 112 of a circle at air collecting chamber lid 11 center, can be used to the bottom of fixing quartz burner 25.Seal cover 10 outside air collecting chamber lid 11 there is a venthole 101, can be used for connecting outside gas circuit.
During real work of the present invention, comprise filter element 1, fan/air pump unit 2, photoelectricity composite catalyzing gas conversion unit/group 3(in whole filtration system and can comprise one or more combination of photoelectricity composite catalyzing gas conversion plant of the present invention in it), and center control/display unit 4, as shown in Figure 6.
Operation principle following (for purification of air), whole system starts, and fan/air pump unit 2 starts, and system sucks air from surrounding environment.Solid dust particle in air, first through filter element 1, is removed by air.Air after purification, is delivered to photoelectricity composite catalyzing gas conversion unit/group 3 through air pump, returns in surrounding environment after purification from photoelectricity composite catalyzing gas conversion unit/group 3.
After system starts, in photoelectricity composite catalyzing gas conversion plant, quartz burner 25 lights startup, simultaneously catalysis electrode 32 and to electrode 13 between apply a quiescent direct current voltage.The magnitude of voltage applied can change according to the different size of the model of specific product.But should be in and not produce within the scope of the safety value of electric discharge.
Because ultraviolet source is enclosed in column cavity, the utilization ratio of luminous energy is higher.Ultraviolet light is through to the multiple reflections on electrode 13 and catalysis electrode 32 surface and scattering, and finally the semiconductor catalyst (as titanium dioxide) of catalyzed dose of coating 233 absorbs.The ultraviolet photon absorbed produces free charge, i.e. electronics and hole in catalyst.
The electronics produced and hole are moved towards each self-corresponding electrode under the effect of electrostatic field.Partial charge with the metallic member arriving catalysis electrode before corresponding charge recombination.Remaining corresponding electric charge, under the effect of electric field, arrives and is gathered in catalyst surface, with the gas molecule generation redox reaction of process.
The voltage direction of conversion electrostatic field can obtain hole (to be oxidized to object) or the electronics (to be reduced to object) of high concentration selectively at catalyst surface.
In general use procedure, gas enters from air admission hole 301, and the dispersion hole 311 in air distribution cavity lid 31 enters catalysis electrode array 23 and to the space between electrod-array 24.And move towards outlet side in this space.In moving process, because suction-operated or direct collision are at catalyst surface., as water vapour, chemical reaction can be there is with the hole of catalyst surface, produce the hydroxyl free radical having oxidability in the material in partial air.Hydroxyl free radical and then react with the organic molecule in contiguous gas, resolves into harmless tasteless carbon dioxide and water the most at last.Air is finally assembled from gas collection hole 111, finally discharges from venthole 101.In use, semiconductor catalyst is lossless.In theory, can unlimitedly use.
Above-described embodiment only illustrates inventive concept of the present invention for explaining, but not the restriction to rights protection of the present invention, all changes utilizing this design the present invention to be carried out to unsubstantiality, all should fall into protection scope of the present invention.

Claims (10)

1. photoelectricity composite catalyzing gas conversion plant, it is characterized in that: comprise housing, axially quartz burner is provided with in housing, the catalysis electrode array of vanes of be provided with centered by fluorescent tube axis at ultraviolet lamp tube-surface, radially arranging and to electrode array of vanes, two electrod-arrays intert together with one heart, and catalysis electrode array of vanes is connected independently electrode respectively with to electrode array of vanes; At housing two ends, air inlet and air outlet are set respectively; Catalyst coat is had at catalysis electrode blade surface.
2. photoelectricity composite catalyzing gas conversion plant as claimed in claim 1, it is characterized in that: described housing comprises the column of hollow, and cover air distribution cavity lid and the air collecting chamber lid at column two ends, in the outside of air distribution cavity lid and air collecting chamber lid, seal cover is set respectively; The inner surface of housing is provided with some with axis being parallel for fixed catalytic electrode array of vanes or the cutting to electrode blade.
3. photoelectricity composite catalyzing gas conversion plant as claimed in claim 2, it is characterized in that: the seal cover of described air distribution cavity lid and its side offers the circular hole inserted for quartz burner, there is the groove bottom for fixing quartz burner inside air collecting chamber lid.
4. photoelectricity composite catalyzing gas conversion plant as claimed in claim 1, is characterized in that: described is made up of independent metal sheet electrode array of vanes, and all there is ledge at its two ends, is socketed on the retainer ring of insulation respectively.
5. photoelectricity composite catalyzing gas conversion plant as claimed in claim 4, is characterized in that: described catalysis electrode array of vanes is made up of independent metal sheet, and all there is ledge at its two ends, connects on the locating ring of insulation respectively.
6. photoelectricity composite catalyzing gas conversion plant as claimed in claim 5, is characterized in that: described locating ring inner ring is enclosed within quartz burner, and outer ring is inserted solid for the jut of catalysis electrode blade; Described retainer ring inner ring is enclosed within the jut of catalysis electrode blade, and outer ring is for inserting solid to the jut of electrode blade.
7. photoelectricity composite catalyzing gas conversion plant as claimed in claim 4, it is characterized in that: the blade that described catalysis electrode blade is made up of metallic aluminium, zinc, vanadium, titanium, copper or other metal or alloy, the catalyst coat on its surface is semiconductor or ceramic coating; Coating composition can comprise oxide, metal particle, or both mixtures.
8. photoelectricity composite catalyzing gas conversion plant as claimed in claim 1, is characterized in that: described is made up of aluminium or stainless steel electrode blade, surface application reflector layer.
9. photoelectricity composite catalyzing gas conversion plant as claimed in claim 2, is characterized in that: there is a circle gas dispersion hole described air distribution cavity lid inside, the seal cover of air distribution cavity lid side has the air admission hole for connecting outside gas circuit.
10. photoelectricity composite catalyzing gas conversion plant as claimed in claim 2, is characterized in that: there is a circle gas collection hole described air collecting chamber lid inside, the seal cover of air collecting chamber lid side has the venthole for connecting outside gas circuit.
CN201310238543.2A 2013-06-17 2013-06-17 Electric light composite catalyzing gas conversion plant Expired - Fee Related CN103331088B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106512601B (en) * 2016-11-29 2018-10-02 东南大学 A kind of duct type oil smoke catalyzing, oxidizing and purifying device and method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10323527A (en) * 1997-05-23 1998-12-08 Nippon Sanso Kk Gas purity device and method
CN2732344Y (en) * 2004-09-30 2005-10-12 广东工业大学 Photoelectric catalyzing reactor for degrading organic pollutants
CN201033280Y (en) * 2006-06-22 2008-03-12 复旦大学 Device using double plasma to process industrial waste gas
CN203507800U (en) * 2013-06-17 2014-04-02 浙江瓦克科技有限公司 Electro-optic combined catalytic gas conversion device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10323527A (en) * 1997-05-23 1998-12-08 Nippon Sanso Kk Gas purity device and method
CN2732344Y (en) * 2004-09-30 2005-10-12 广东工业大学 Photoelectric catalyzing reactor for degrading organic pollutants
CN201033280Y (en) * 2006-06-22 2008-03-12 复旦大学 Device using double plasma to process industrial waste gas
CN203507800U (en) * 2013-06-17 2014-04-02 浙江瓦克科技有限公司 Electro-optic combined catalytic gas conversion device

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