CN203678240U - Catalytic plasma and tunnel plasma including same - Google Patents
Catalytic plasma and tunnel plasma including same Download PDFInfo
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- CN203678240U CN203678240U CN201320128882.0U CN201320128882U CN203678240U CN 203678240 U CN203678240 U CN 203678240U CN 201320128882 U CN201320128882 U CN 201320128882U CN 203678240 U CN203678240 U CN 203678240U
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Abstract
The utility model provides catalytic plasma and tunnel plasma including the same. The catalytic plasma comprises an insulated housing with an air inlet and an exhaust hole, two electrode plates and a catalytic core, wherein the electrode plates are parallel to each other and arranged inside the insulated housing; the catalytic core is clamped between the electrode plates; a plurality of cells are arranged on the catalytic core; the cells are hollow pipelines and consistent in arrangement directions; the air inlet, the cells and the exhaust hole are sequentially communicated; the electrode plates can ionize molecules in a cooking fume waste gas into free ions; the catalytic core can guide the free ions to react, so as to generate a harmless gas. Furthermore, the catalytic core adopts a cell array structure, so that the action area and the action time between the catalytic core and the ions can be increased, and thus the catalytic efficiency is high. Therefore, the cooking fume waste gas can be efficiently electrolyzed and guided to be transformed into the harmless gas by the catalytic plasma disclosed by the utility model.
Description
Technical field
The utility model relates to air purification field, the tunnel electricity slurry that particularly a kind of catalyst electricity is starched and comprised it.
Background technology
In the time of high-temperature cooking, edible oil can produce a large amount of " thermal oxide catabolites ", and those catabolites are diffused in air with the form of smog, forms oil flue waste gas.The composition of oil flue waste gas is very complicated, mainly contains aldehyde, ketone, hydrocarbon, aliphatic acid, alcohol, aromatic compound, ester, lactone, heterocyclic compound etc.In addition, in oil flue waste gas, also comprise BaP, volatile nitrosamine, the contour carcinogenic substance of heterocyclic amine compound.
Similarly, the vehicles such as automobile, jet airplane and steamer are using fossil fuel as the energy, and give off the oil flue waste gas of harmful substances such as comprising solid suspended particle, carbon monoxide, hydrocarbons and nitrogen oxide.
The oil flue waste gas producing in order to remove above-mentioned various situation, adopts the modes such as active carbon adsorption, zeolite adsorption, high temperature incineration oxidation, cryogenic condensation recovery conventionally in prior art.But active carbon adsorption and zeolite adsorption exist regeneration, high energy consumption and the secondary pollution problem of repeating, high temperature incineration oxidation and cryogenic condensation reclaim and can bring again that superelevation consumes energy, cost of equipment is high and the problem of high maintenance costs.In addition, above-mentioned four kinds of processing modes all can not change into innocuous gas by oil flue waste gas, exist secondary pollution.
Therefore, how oil flue waste gas is changed into innocuous gas efficiently, perplexing the research staff of this area always.
Utility model content
The technical problems to be solved in the utility model is the defect that oil flue waste gas cannot be changed into innocuous gas in prior art in order to overcome, the tunnel electricity slurry that provides a kind of catalyst electricity slurry and comprise it, this catalyst electricity slurry can change into innocuous gas efficiently by oil flue waste gas.
The utility model is to solve above-mentioned technical problem by following technical proposals:
A kind of catalyst electricity slurry, its feature is, this catalyst electricity slurry comprises that one has the insulation crust of air inlet and exhaust outlet, two battery lead plates and a catalyst fuse, those battery lead plates are parallel to each other, and be arranged in this insulation crust, this catalyst fuse is located between those battery lead plates, this catalyst fuse is gone into battle and is shown multiple cells, those cells are hollow pipeline and orientation is consistent, and this air inlet, those cells and this exhaust outlet are communicated with successively.
Preferably, on two surfaces that are oppositely arranged of those battery lead plates, be distributed with many spray points.
Preferably, the body of this catalyst fuse is insulating substrate, between each battery lead plate and this catalyst fuse, is also provided with a dielectric plate.According to the kind of oil flue waste gas, at the surface attachment last layer catalyst of the body of catalyst fuse, the kind of catalyst can be chosen as metal solvent, metal oxide catalyst or nonmetal catalyst.For example, the in the situation that of being mainly nitre and nitrogen oxide in oil flue waste gas, generally need to use platinum, Ba Huolaodeng three races precious metal element; The in the situation that of being mainly oxysulfide or sulfohydrate in oil flue waste gas, need to use metal oxide catalyst, for example, chromium oxide, molybdenum oxide, iron oxide, manganese oxide, zinc oxide, nickel oxide, cupric oxide and tungsten oxide.
A kind of tunnel electricity slurry, for decomposing oil smoke waste gas, its feature is, and this tunnel electricity slurry comprises at least two son electricity slurry modules of series connection successively, and this little electricity slurry module comprises catalyst electricity slurry as above.
Preferably, this little electricity slurry module also comprises at least one nanometer electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those catalyst electricity slurries, those nanometer electricity slurries.
Preferably, this little electricity slurry module also comprises at least one medium electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those medium electricity slurries, those catalyst electricity slurries, those nanometer electricity slurries.
Preferably, this little electricity slurry module also comprises at least one smoke removing electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those smoke removing electricity slurries, those medium electricity slurries, those catalyst electricity slurries, those nanometer electricity slurries.
Preferably, this a little electricity slurry module comprises multiple smoke removing electricity slurries, multiple medium electricity slurry, multiple catalyst electricity slurry and multiple nanometer electricity slurry, at least two smoke removing electricity slurries in those smoke removing electricity slurries are in parallel, at least two medium electricity slurries in those medium electricity slurries are in parallel, at least two catalyst electricity slurries in those catalyst electricity slurries are in parallel, and at least two nanometer electricity slurries in those nanometer electricity slurries are in parallel.
Preferably, each smoke removing electricity slurry comprises an electrion reactor, this tunnel electricity slurry also comprises an automatically controlled disconnecting link, those electrion reactors are all electrically connected with this automatically controlled disconnecting link, those electrion reactors are at this automatically controlled disconnecting link this oil flue waste gas of electrolysis during in the first gear, and those electrion reactors are at this automatically controlled disconnecting link this oil flue waste gas of thermal evaporation during in the second gear.By using this automatically controlled disconnecting link, this oil smoke decomposition device can manufacture and have the dual-use function that oil smoke decomposes and oil smoke evaporates concurrently, can effectively remove difficult decomposed substance, has improved operating efficiency and life-span.
Preferably, this automatically controlled disconnecting link comprises a disconnecting link housing, an actuator and one and the swing arm that is articulated of this actuator, and this actuator is used for driving this swing arm to be rocked to this first gear or this second gear.
Preferably, each smoke removing electricity slurry also comprises an air inlet pipe, a processing unit and an escape pipe, this processing unit comprises this electrion reactor, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this electrion reactor and this escape pipe.
Preferably, this processing unit also comprises a pretreatment module, this pretreatment module comprises a centrifugal blower, waste material interception groove and a waste material outlet, this waste material interception groove is used for stopping and reclaiming the solid or the liquid debris that are thrown away by this centrifugal blower, this waste material outlet is for those solids or liquid debris are discharged, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this pretreatment module, this electrion reactor and this escape pipe.
Preferably, this processing unit also comprises waste material recycling module again, this waste material again recycling module comprises a waste material guide channel and waste material outlet again, this waste material guide channel is for solid or liquid debris are directed to this waste material outlet again, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this pretreatment module, this electrion reactor, this waste material recycling module and this escape pipe again.
Positive progressive effect of the present utility model is: those battery lead plates can become the molecular ionization in oil flue waste gas the ion of free state, and this catalyst fuse can guide the ionic reaction of those free states to generate innocuous gas.Moreover this catalyst fuse adopts array of cells structure, can increase and active area and the action time of those ions, thereby catalytic efficiency is higher.Hence one can see that, and catalyst electricity slurry electrolysis efficiently of the present utility model also guides oil flue waste gas to be converted into innocuous gas.
Accompanying drawing explanation
Fig. 1 is the structural representation of the tunnel electricity slurry of the utility model preferred embodiment.
Fig. 2 is the structural representation of the smoke removing electricity slurry array during the tunnel electricity of Fig. 1 is starched.
Fig. 3 is the structural representation that in Fig. 2, smoke removing electricity is starched a smoke removing electricity slurry in array.
Fig. 4 is the structural representation of smoke removing electricity slurry after removal disconnecting link in Fig. 3.
Fig. 5 is the partial structurtes schematic diagram of smoke removing electricity slurry in Fig. 4.
Fig. 6 is the structural representation of the disconnecting link of smoke removing electricity slurry in Fig. 3.
Fig. 7 is the structural representation of the medium electricity slurry array during the tunnel electricity of Fig. 1 is starched.
Fig. 8 is the structural representation of the catalyst electricity slurry array during the tunnel electricity of Fig. 1 is starched.
Fig. 9 is the structural representation that the catalyst electricity of Fig. 8 is starched a catalyst electricity slurry in array.
Figure 10 is the internal structure schematic diagram of the catalyst electricity slurry of Fig. 9.
Figure 11 is the structural representation of the nanometer electricity slurry array during the tunnel electricity of Fig. 1 is starched.
Description of reference numerals:
Smoke removing electricity slurry array: 1 medium electricity slurry array: 2
Catalyst electricity slurry array: 3 nanometer electricity slurry arrays: 4
Smoke removing electricity slurry: 10 medium electricity slurries: 20
Catalyst electricity slurry: 30 nanometer electricity slurries: 40
Air inlet pipe: 11 attaching parts: 12
Pretreatment module: 13 processing units: 14
Escape pipe: 15 electrion reactors: 16
Waste material is recycling module again: 17 automatically controlled disconnecting links: 18
Centrifugal blower: 131 waste material interception grooves: 132
Waste material outlet: 133 waste material guide channels: 171
Waste material is outlet again: 172 disconnecting link housings: 181
Actuator: 182 swing arms: 183
The second gear: 184 springs: 185
Inlet wire cable: 186 evaporation cables: 187
Decompose cable: 188 casing covers: 31
Electric pole plate: dielectric plate on 32: 33
Catalyst fuse: 34 times dielectric plates: 35
Lower electrode plate: 36 insulation crusts: 37
Air inlet: 371 exhaust outlets: 372
The specific embodiment
Lift a preferred embodiment below, and carry out by reference to the accompanying drawings the clearer the utility model that intactly illustrates.
As shown in Figure 1, the present embodiment provides a kind of tunnel electricity slurry, for decomposing oil smoke waste gas, this tunnel electricity slurry comprises seven son electricity slurry modules of series connection successively, this a little electricity slurry module comprises that a smoke removing electricity slurry array 1(specifically please refer to Fig. 2), three medium electricity slurry array 2(specifically please refer to Fig. 7), a catalyst electricity slurry array 3(specifically please refer to Fig. 8) and two nanometer electricity starch array 4(and specifically please refer to Figure 11).
This smoke removing electricity slurry array 1 is for decomposing and remove dust granules and the liquid greasy dirt of oil flue waste gas, thereby suitable this tunnel electricity that is arranged at is starched foremost.Those medium electricity slurry arrays 2 are mainly used in gaseous molecular to be converted into the ion of a large amount of free states, this catalyst electricity slurry array 3 can catalysis and is guided the ionic reaction of those free states to generate innocuous gas, thereby suitable those media electricity slurry arrays 2 and this catalyst electricity slurry array 3 connects successively, and be arranged at the mid portion that this tunnel electricity is starched.Those nanometer electricity slurry arrays 4 are mainly used in deodorization and sterilization, and by anion in innocuous gas Molecular Adsorption after treatment, and then give off salubrious pleasant air.
Thereby the tunnel of the present embodiment electricity slurry is according to the feature of oil flue waste gas, decomposing oil smoke waste gas layer by layer categorizedly, and give off the air of salubrious pleasant high-negative ion concentration, decomposes and to remove the efficiency of oil flue waste gas higher.
As shown in Figure 2, this smoke removing electricity slurry array 1 comprises 12 smoke removing electricity slurries 10, and those smoke removing electricity slurries 10 are arranged in parallel.As shown in Figure 7, each medium electricity slurry array 2 comprises eight medium electricity slurries 20, and those medium electricity slurries 20 are arranged in parallel.As shown in Figure 8, this catalyst electricity slurry array 3 comprises six catalyst electricity slurries 30, and those catalyst electricity slurries 30 are arranged in parallel.As shown in figure 11, each nanometer electricity slurry array 4 comprises that eight nanometer electricity slurry 40(Figure 11 have only demonstrated four nanometer electricity slurries, and another four nanometers electricity slurry is blocked), those nanometer electricity slurries 40 are arranged in parallel.
By " being arranged in parallel " mode, can increase the area of son electricity slurry module, so that the oil flue waste gas being applicable under different flow operating mode decomposes.
Fig. 2 has only schematically drawn smoke removing electricity slurry 10, when actual production, smoke removing electricity slurry 10 can be produced and is become the form shown in Fig. 3.
As shown in Fig. 3-6, the smoke removing electricity slurry 10 in the tunnel electricity slurry of the present embodiment, for decomposing oil smoke waste gas, it comprises an air inlet pipe 11, a processing unit 14 and an escape pipe 15.This processing unit 14 comprises an electrion reactor 16, a pretreatment module 13 and waste material recycling module 17 again.The front-end and back-end of this processing unit 14 are connected with this escape pipe 15 with air inlet pipe 11 by attaching parts 12 respectively.
This tunnel electricity slurry also comprises an automatically controlled disconnecting link 18, and as shown in Figure 3, this automatically controlled disconnecting link 18 is electrically connected with this electrion reactor 16.
As shown in Figure 4, this waste material again recycling module 17 comprises a waste material guide channel 171 and waste material outlet 172 again, and this waste material guide channel 171 is for being directed to this waste material outlet 172 again by solid or liquid debris.
As shown in Figure 5, this pretreatment module 13 comprises a centrifugal blower 131, waste material interception groove 132 and a waste material outlet 133, this waste material interception groove 132 is for stopping and reclaiming the solid or the liquid debris that are thrown away by this centrifugal blower 131, and this waste material outlet 133 is for discharging those solids or liquid debris.
As shown in Figure 6, this automatically controlled disconnecting link 18 comprises a disconnecting link housing 181, an actuator 182 and one and the swing arm 183 that is articulated of this actuator 182, and this actuator 182 is for driving this swing arm 183 to be rocked to this first gear (decomposing cable 188 places) or this second gear 184.This second gear 184 comprises a spring 185, thereby forms elastic connecting contravention.Two inlet wire cables 186 and two evaporation cable 187(are also set on this disconnecting link housing 181 and please also refer to Fig. 3 and Fig. 6, to understand the line construction that this automatically controlled disconnecting link 18 is electrically connected with this electrion reactor 16).
When decomposing oil smoke waste gas, this automatically controlled disconnecting link 18 is placed in the first gear (decomposing cable 188 places), please understand in conjunction with Fig. 3-5 simultaneously, opens this electrion reactor 16 and this centrifugal blower 131.This centrifugal blower 131 extracts oil flue waste gas by this air inlet pipe 11, and the solid in oil flue waste gas or liquid debris are carried out to pretreatment by this waste material interception groove 132 and this waste material outlet 133.After pretreatment remaining solid or liquid debris through centrifugal drying to this waste material again recycling module 17 again process.Pretreated gas carries out electrolysis through this electrion reactor 16.Because the surface of electrion reactor 16 hollow core electrodes is applied with the high-tension electricity of tens kilovolts, therefore can interrupt thoroughly molecular link, carbon monoxide is changed into carbon and oxygen, hydrocarbon is finally changed into carbon, oxygen G&W, conversion of nitrogen oxides is become to nitrogen and oxygen etc.
Evaporation when oil flue waste gas, is placed in the second gear 184 by this automatically controlled disconnecting link 8, and this electrion reactor 16(please refer to Fig. 3-4) in coreless armature in electrical heating to higher than 1000 ℃.The material of coreless armature can be according to heating wire in commercially available " immersion heater ", for example, ferrum-chromium-aluminum heating wire, NI-G heating wire, standard choose.By those difficult decomposed substances of heating evaporation (distillation), spot can not gathered in the surface of the fuse of this oil smoke decomposition device, comparatively bright and clean, thereby has improved operating efficiency and life-span.
In a word, can be by controlling the mode of the first power supply and second source, realize to reciprocation cycle decomposing oil smoke waste gas and evaporation oil flue waste gas.
Smoke removing electricity slurry in the tunnel electricity slurry of the present embodiment has following technique effect:
The first, by using this automatically controlled disconnecting link, this oil smoke decomposition device can manufacture and have the dual-use function that oil smoke decomposes and oil smoke evaporates concurrently, can effectively remove difficult decomposed substance, has improved operating efficiency and life-span.
The second, by this first gear and this second gear being designed to the form of elastic connecting contravention, in the time closing a floodgate, the end of this swing arm can form firmly soft contact with this first gear or this second gear, is not only electrically connected fastness higher, and is not easy to produce electric spark.
Three, when centrifugal blower High Rotation Speed, can be in smoke removing electricity slurry formation negative pressure, the receive flow of accelerating charge pipe to oil flue waste gas.
Four, pretreatment module can be effectively solid-state or liquid parts in the centrifugal and oil flue waste gas that throws away, electrion reactor is the gaseous state composition in decomposing oil smoke waste gas effectively, and waste material again recycling module carries out secondary recovery to the solid-state or liquid parts in oil flue waste gas.Smoke removing electricity slurry in the application's tunnel electricity slurry can be distinguished the gentle three kinds of state compositions of solid, liquid in oil flue waste gas, and processes targetedly, and treatment effect is greatly improved.
As shown in Fig. 8-10, this catalyst electricity slurry 30 comprises an insulation crust 37 with air inlet 371 and exhaust outlet 372, a casing cover 31, two battery lead plates (comprising electric pole plate 32 and lower electrode plate 36) and catalyst fuses 34.Those battery lead plates (comprising electric pole plate 32 and lower electrode plate 36) are parallel to each other, and are arranged in this insulation crust 37, and this catalyst fuse 34 is located between those battery lead plates, on two surfaces that are oppositely arranged of those battery lead plates, are distributed with many spray points.
The body of this catalyst fuse 34 is that insulating substrate and array have multiple cells, and those cells are hollow pipeline and orientation is consistent, and this air inlet 371, those cells (being positioned on catalyst fuse 34) and this exhaust outlet 372 are communicated with successively.Between each battery lead plate (electric pole plate 32 or lower electrode plate 36) and this catalyst fuse, be also provided with a dielectric plate (upper dielectric plate 33 or lower dielectric plate 35).
The catalyst electricity slurry of the present embodiment has following technique effect:
The first, those battery lead plates can become the molecular ionization in oil flue waste gas the ion of free state, and this catalyst fuse can guide the ionic reaction of those free states to generate innocuous gas.Moreover this catalyst fuse adopts array of cells structure, can increase and active area and the action time of those ions, thereby catalytic efficiency is higher.Hence one can see that, and the catalyst electricity slurry electrolysis efficiently of the present embodiment also guides oil flue waste gas to be converted into innocuous gas.
The second, on two surfaces that are oppositely arranged, be distributed with many spray points, " spray point structure " utilized the principle of point discharge preferably.
Three, dielectric plate can make electric discharge or electrolysis homogenising, has avoided the effectively electrolysis of region between adjacent spray point, realizes the effect of homogenising electrolysis.
When actual production, the tunnel electricity slurry of the present embodiment is not limited to the version that four seed electricity slurry modules are connected successively, and the structure that two seed electricity slurry modules or three seeds electricity slurry module are connected successively also can adopt.In addition, the present embodiment has only schematically been drawn medium electricity slurry (as shown in Figure 7) and nanometer electricity slurry (as shown in Figure 9), in the time of actual production tunnel electricity slurry, can buy commercially available medium electricity slurry and nanometer electricity slurry.
In addition, the in the situation that of containing high concentration mist of oil and toxic gas (sulfur-bearing, chlorine, nitrogen or fluorine element) in oil flue waste gas, can also a kitchen sink be set at the front end of the tunnel of the present embodiment electricity slurry, to carry out pretreatment such as dissolving and filtering.
Although more than described the specific embodiment of the present utility model, it will be understood by those of skill in the art that these only illustrate, protection domain of the present utility model is limited by appended claims.Those skilled in the art is not deviating under the prerequisite of principle of the present utility model and essence, can make various changes or modifications to these embodiments, but these changes and modification all fall into protection domain of the present utility model.
Claims (13)
1. a catalyst electricity slurry, it is characterized in that, this catalyst electricity slurry comprises that one has the insulation crust of air inlet and exhaust outlet, two battery lead plates and a catalyst fuse, those battery lead plates are parallel to each other, and be arranged in this insulation crust, this catalyst fuse is located between those battery lead plates, this catalyst fuse is gone into battle and is shown multiple cells, those cells are hollow pipeline and orientation is consistent, and this air inlet, those cells and this exhaust outlet are communicated with successively.
2. catalyst electricity slurry as claimed in claim 1, is characterized in that, on two surfaces that are oppositely arranged of those battery lead plates, is distributed with many spray points.
3. the electricity of the catalyst as described in any one in claim 1-2 slurry, is characterized in that, the body of this catalyst fuse is insulating substrate, between each battery lead plate and this catalyst fuse, is also provided with a dielectric plate.
4. a tunnel electricity slurry, for decomposing oil smoke waste gas, is characterized in that, this tunnel electricity slurry comprises at least two son electricity slurry modules of series connection successively, and this little electricity slurry module comprises the electricity of the catalyst described in any one slurry in claim 1-3.
5. tunnel as claimed in claim 4 electricity slurry, is characterized in that, this little electricity slurry module also comprises at least one nanometer electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those catalyst electricity slurries, those nanometer electricity slurries.
6. tunnel as claimed in claim 5 electricity slurry, is characterized in that, this little electricity slurry module also comprises at least one medium electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those medium electricity slurries, those catalyst electricity slurries, those nanometer electricity slurries.
7. tunnel as claimed in claim 6 electricity slurry, it is characterized in that, this a little electricity slurry module also comprises at least one smoke removing electricity slurry, and this tunnel electricity slurry in use, makes this oil flue waste gas successively by those smoke removing electricity slurries, those medium electricity slurries, those catalyst electricity slurries, those nanometer electricity slurries.
8. tunnel as claimed in claim 7 electricity slurry, it is characterized in that, this a little electricity slurry module comprises multiple smoke removing electricity slurries, multiple medium electricity slurry, multiple catalyst electricity slurry and multiple nanometer electricity slurry, at least two smoke removing electricity slurries in those smoke removing electricity slurries are in parallel, at least two medium electricity slurries in those medium electricity slurries are in parallel, at least two catalyst electricity slurries in those catalyst electricity slurries are in parallel, and at least two nanometer electricity slurries in those nanometer electricity slurries are in parallel.
9. tunnel as claimed in claim 7 electricity slurry, it is characterized in that, each smoke removing electricity slurry comprises an electrion reactor, this tunnel electricity slurry also comprises an automatically controlled disconnecting link, those electrion reactors are all electrically connected with this automatically controlled disconnecting link, those electrion reactors are at this automatically controlled disconnecting link this oil flue waste gas of electrolysis during in the first gear, and those electrion reactors are at this automatically controlled disconnecting link this oil flue waste gas of thermal evaporation during in the second gear.
10. tunnel as claimed in claim 9 electricity slurry, is characterized in that, this automatically controlled disconnecting link comprises a disconnecting link housing, an actuator and one and the swing arm that is articulated of this actuator, and this actuator is used for driving this swing arm to be rocked to this first gear or this second gear.
11. tunnel as claimed in claim 9 electricity slurries, it is characterized in that, each smoke removing electricity slurry also comprises an air inlet pipe, a processing unit and an escape pipe, this processing unit comprises this electrion reactor, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this electrion reactor and this escape pipe.
12. tunnel as claimed in claim 11 electricity slurries, it is characterized in that, this processing unit also comprises a pretreatment module, this pretreatment module comprises a centrifugal blower, waste material interception groove and a waste material outlet, this waste material interception groove is used for stopping and reclaiming the solid or the liquid debris that are thrown away by this centrifugal blower, this waste material outlet is for those solids or liquid debris are discharged, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this pretreatment module, this electrion reactor and this escape pipe.
13. tunnel as claimed in claim 12 electricity slurries, it is characterized in that, this processing unit also comprises waste material recycling module again, this waste material again recycling module comprises a waste material guide channel and waste material outlet again, this waste material guide channel is for solid or liquid debris are directed to this waste material outlet again, and this oil smoke decomposition device is used for making this oil flue waste gas successively by this air inlet pipe, this pretreatment module, this electrion reactor, this waste material recycling module and this escape pipe again.
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| CN201320128882.0U CN203678240U (en) | 2013-03-20 | 2013-03-20 | Catalytic plasma and tunnel plasma including same |
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| CN201320128882.0U CN203678240U (en) | 2013-03-20 | 2013-03-20 | Catalytic plasma and tunnel plasma including same |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104056532A (en) * | 2013-03-20 | 2014-09-24 | 刘颖姝 | Catalyst plasma and tunnel plasma comprising catalyst plasma |
| CN105381692A (en) * | 2014-09-04 | 2016-03-09 | 苏州鼎德电环保科技有限公司 | Kitchen purifier having capsicum annuum odor removing function |
-
2013
- 2013-03-20 CN CN201320128882.0U patent/CN203678240U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104056532A (en) * | 2013-03-20 | 2014-09-24 | 刘颖姝 | Catalyst plasma and tunnel plasma comprising catalyst plasma |
| CN105381692A (en) * | 2014-09-04 | 2016-03-09 | 苏州鼎德电环保科技有限公司 | Kitchen purifier having capsicum annuum odor removing function |
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Owner name: SUZHOU WONDERFUL TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: LIU YINGSHU Effective date: 20150611 |
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Effective date of registration: 20150611 Address after: 215021 Suzhou Industrial Park, Jiangsu, China Road, No. 10 Patentee after: Suzhou Wangde Technology Co.,Ltd. Address before: 215021 Suzhou Industrial Park, Jiangsu, China Road, No. 10 Patentee before: Liu Yingshu |
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Effective date of registration: 20190722 Address after: 215000 International Science and Technology Park, Suzhou Industrial Park, Suzhou City, Jiangsu Province, Phase 4 1705 Patentee after: SUZHOU DINGDEDIAN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 215021 Suzhou Industrial Park, Jiangsu, China Road, No. 10 Patentee before: Suzhou Wangde Technology Co.,Ltd. |
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