CN206701008U

CN206701008U - The clarifier of low-altitude discharged waste gas purification processing

Info

Publication number: CN206701008U
Application number: CN201720368710.9U
Authority: CN
Inventors: 黄嘉铭
Original assignee: Individual
Current assignee: Individual
Priority date: 2017-04-10
Filing date: 2017-04-10
Publication date: 2017-12-05
Anticipated expiration: 2027-04-10

Abstract

It the utility model is related to air purification field, more particularly to a kind of clarifier of low-altitude discharged waste gas purification processing, the clarifier includes sealing shell body, exhaust gas entrance, takes off liquid dedirt collection system, refilters system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer and clean air outlet；Exhaust gas entrance and clean air outlet are arranged on sealing shell body, de- liquid dedirt collection system, refilter system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer and be arranged in housing, waste gas is entered in housing by exhaust gas entrance, and successively by taking off liquid dedirt collection system, refiltering and discharged after system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer are purified from clean air outlet.De- liquid dedirt collection system of the present utility model can isolate profit compound and solid granulates in air, so as to solve the problems, such as that plasma purifier can not the big gas of purifying aqueous oil content.

Description

The clarifier of low-altitude discharged waste gas purification processing

Technical field

It the utility model is related to air purification field, and in particular to a kind of clarifier of low-altitude discharged waste gas purification processing.

Background technology

In recent years, as the continuous development of countries in the world economy, China's industry, food and drink, tourism are also developed rapidly, thus produced Waste gas that life can not be exempted from, flue gas.As waste gas contains substantial amounts of H₂S、NH₃, VOC toxic and harmful gas, flue gas, the oil smoke such as HCL remove Burning is formed outside solid suspension, and also containing substantial amounts of liquid, liquid is mainly into being profit compound.

The filler major part that the filtering link of existing market clarifier uses is metal screen, web etc., and resistance is big.And Filter net jam is easily caused for the waste gas for having being stained with property oil-containing hydrate.Because the maintenance to filter net jam, replacing are too late When, clarifier tends not to effectively filter waste gas, has many sticking oily matters through being commonly in smoke discharging pipe, even along flue tube Wall, ground are flowed out to, causes second of pollution, or even causes the direct hidden danger of fire.

Utility model content

The purpose of this utility model is to provide a kind of low-altitude discharged waste gas purification treatment and purification device, and it is provided with de- liquid and taken off Dirt collection system, to overcome existing air purifier can not efficiently separate lacking for the profit compound in air and solid granulates Fall into.

In order to solve the above problems, the utility model provides a kind of clarifier of low-altitude discharged waste gas purification processing, should Clarifier includes sealing shell body, exhaust gas entrance, takes off liquid dedirt collection system, refilters system, energetic ion pipe group, low temperature etc. Ionic decontamination devices, activated carbon filter plate layer and clean air outlet；The exhaust gas entrance and clean air outlet are arranged at institute State on sealing shell body, the de- liquid dedirt collection system, refilter system, energetic ion pipe group, low-temperature plasma purification dress Put, activated carbon filter plate layer is arranged in housing, waste gas is entered in housing by the exhaust gas entrance, and successively by described de- Liquid dedirt collection system, refilter system, energetic ion pipe group, low-temperature plasma purifying device, the progress of activated carbon filter plate layer only Discharged after change from the clean air outlet.

As preferable, the de- liquid dedirt collection system includes the first de- liquid dedirt passage and the second de- liquid dedirt is led to Road, the described first de- liquid dedirt feeder connection end connects with the exhaust gas entrance, described first take off liquid dedirt channel outlet and The arrival end connection of second de- liquid dedirt passage, the described first de- interior first coacervation staggered provided with polylith of liquid dedirt passage Plate, is provided with multiple second coacervation plates and the 3rd coacervation plate in the described second de- liquid dedirt passage, the second coacervation plate with it is described 3rd coacervation plate is staggered.

As preferable, the described first de- liquid dedirt passage is vertically arranged, and the described second de- liquid dedirt passage is horizontally disposed with, It is described to refilter system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer to be arranged at described second de- The top of liquid dedirt passage.

As preferable, the second coacervation plate is located on the roof of the described second de- liquid dedirt passage, the trimerization Solidifying plate is arranged on the bottom wall of the described second de- liquid dedirt passage, and the length of the second coacervation plate is less than the 3rd coacervation plate Length.

As preferable, the bottom of the 3rd coacervation plate is provided with leakage fluid dram, the row on adjacent two blocks of the 3rd coacervation plates The position of liquid mouth is different.

As preferable, the port of export of the described second de- liquid dedirt passage is provided with liquid collection trough.

As preferable, the system that refilters includes cushion chamber, air filtering core group and flows filter plate, the cushion chamber The port of export that entrance point takes off liquid collection system with the dedirt is connected, and the air filtering core group is arranged in the cushion chamber, institute Stream filter plate is stated to be located at outside the cushion chamber, and at the port of export of the cushion chamber.

As preferable, the energetic ion pipe group is detachably arranged in the sealing shell body, the ionic tube group Including body, multiple ion pipe units and photocatalysis net, the photocatalysis net is set on the body, multiple ionic tubes Unit is arranged to two rows, and parallel with the photocatalysis net, wherein row's ionic tube is located at photocatalysis net side, it is another to be discharged to son Pipe is located at photocatalysis net opposite side.

As preferable, the low-temperature plasma purifying device includes power supply module and plasma cleaning module, described close To seal shell body and be provided with electric field inspection window, the plasma cleaning module is located in the sealing shell body, and positioned at described Electric field checks at window that the power supply module lid is located at the electric field and checked on window, and one end checks window with the electric field Side wall rotation connection, the power supply module is provided with safety switch.

As preferable, the plasma cleaning module includes support body, minus plate, multiple anode tubes and multiple negative electrodes electricity Pole, multiple anode tubes are arranged on support body, and the minus plate is arranged on the side of the support body, multiple cathode electrodes One end be connected on minus plate, and be inserted into correspondingly in the anode tube.

Low-altitude discharged waste gas purification treatment and purification device of the present utility model, takes off liquid collection system using dedirt, can isolate Profit compound in waste gas；This low-altitude discharged waste gas purification treatment and purification device also includes de- liquid dedirt collection system, refiltered The multistage composite filtering of system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer；It is of particular importance that This low-altitude discharged waste gas purification treatment and purification device solve plasma purifier can not the big gas of purifying aqueous oil content ask Topic.

Brief description of the drawings

Fig. 1 is the structural profile signal of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Figure；

Fig. 2 is the outer surface signal of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Figure；

Fig. 3 is the second de- liquid dedirt of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Coacervation plate arrangement schematic diagram in passage；

Fig. 4 is the plasma cleaning dress of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Put structural representation；

Fig. 5 is the ionic tube group structure of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Schematic diagram；

Fig. 6 is the safety switch construction of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment Schematic diagram；

Fig. 7 is that the power supply module of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment is opened View；

Fig. 8 is that the power supply module of the clarifier of the low-altitude discharged waste gas purification processing of the utility model preferred embodiment is closed View.

Wherein, 1, sealing shell body；11st, exhaust gas entrance；12nd, liquid dedirt collection system is taken off；121st, the first de- liquid dedirt is led to Road；1211st, the first coalescence dividing plate；1212nd, the first coacervation plate；1213rd, the second coalescence dividing plate；122nd, the second de- liquid dedirt passage； 1221st, the 3rd coacervation plate；1222nd, the second coacervation plate；1223rd, liquid collection trough；1224th, oil-water discharge valve；1225th, liquid level gauge； 1226th, leakage fluid dram；123rd, the first inspection socket；13rd, system is refiltered；131st, cushion chamber；132nd, air filtering core group；133rd, stream filter Onboard body；134th, filter plate is flowed；135th, the second inspection socket；14th, energetic ion pipe group；141st, energetic ion pipe group carrier；142、 Photocatalysis net；143rd, ion pipe unit；15th, low-temperature plasma purifying device；151st, anode canister；152nd, cathode electrode；153rd, it is cloudy Pole plate；154th, the first insulator；155th, power supply module；1551st, power supply indicator；1552nd, ammeter；1553rd, open and close type electronic box Door；1554th, electric field checks window；1555th, radiator fan；1556th, power supply；1557th, insulate fixing lock；156th, safety switch； 1561st, power cable；1562nd, felt pad；1563rd, porcelain vase pot cover；1564th, the second insulator；1565th, stainless steel spring；1566、 Porcelain vase thimble；157th, anode module；158th, support body；16th, activated carbon filter plate layer；161st, activated carbon filter plate layer carrier；17th, it is clean empty Gas exports；18th, first pressure table；19th, second pressure gauge.

Embodiment

With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below Embodiment is used to illustrate the utility model, but is not limited to the scope of the utility model.

Embodiment 1

With reference to shown in Fig. 1 and Fig. 2, the low-altitude discharged waste gas purification processing of the utility model embodiment is schematically showed Clarifier, the clarifier includes sealing shell body 1 and the exhaust gas entrance 11 and pure air that are arranged on sealing shell body 1 go out Mouth 17, de- liquid dedirt collection system 12, refilter system 13, energetic ion pipe group 14, low-temperature plasma purifying device 15, activity Carbon filtration flaggy 16 is arranged in sealing shell body 1, and air is entered in sealing shell body 1 by exhaust gas entrance 11, and is passed through successively Cross de- liquid dedirt collection system 12, refilter system 13, energetic ion pipe group 14, low-temperature plasma purifying device 15, activated carbon Filter plate layer 16 is discharged after being purified from clean air outlet 17；Through take off liquid dedirt collection system 12 remove water oil removing air again by Subsequent purification link is purified, so as to realize that plasma purifier can the big gas of purifying aqueous oil content.

De- liquid dedirt collection system 12 includes the first de- de- liquid dedirt passage 122 of liquid dedirt passage 121, second, and first is de- The arrival end of liquid dedirt passage 121 connects with exhaust gas entrance 11, and the port of export and the second de- liquid of the first de- liquid dedirt passage 121 take off The arrival end connection of dirt passage 122, the interior first coalescence dividing plate 1211 and second that is provided with of sealing shell body 1 coalesce dividing plate 1213, the The side wall of one coalescence dividing plate 1211 and sealing shell body 1 forms the first de- liquid dedirt passage 121, the second coalescence dividing plate 1213 with it is close The lower wall for sealing shell body 1 forms the second de- liquid dedirt passage 122；Polylith staggered row is provided with first de- liquid dedirt passage 121 First coacervation plate 1212 of cloth, in multiple the first staggered coacervation plates 1212, wherein a row is arranged in sealing shell body 1 On wall, another row is arranged on the second coalescence dividing plate 1213；Second coacervation plate 1222 is located at the top of the second de- liquid dedirt passage 122 On wall (the i.e. second coalescence dividing plate 1213), the bottom wall that the 3rd coacervation plate 1221 is arranged on the second de- liquid dedirt passage 122 (seals Shell body 1) on, because the second de- bottom of liquid dedirt passage 122 need to deposit profit compound and solid granulates, so the second coacervation The length of plate 1222 is less than the length of the 3rd coacervation plate 1221；The length of second coacervation plate 1222 and the length of the 3rd coacervation plate 1221 Degree sum should be greater than the height of the second de- liquid dedirt passage 122, to ensure that air can flow through each piece of He of the second coacervation plate 1222 3rd coacervation plate 1221.

The length of first coacervation plate 1212 is more than the half of the first de- width of liquid dedirt passage 121；Second de- liquid dedirt is led to Multiple second coacervation plates 1222 and the 3rd coacervation plate 1221, the second coacervation plate 1222 and the 3rd coacervation plate 1221 are provided with road 122 It is staggered, the staggered buffering condensation for being advantageous to air of multiple coacervation plates, even if greasy dirt is accumulated on coacervation plate, also not The blocking of air duct can be caused；Air is by multiple in the first de- 121 and second de- liquid dedirt passage 122 of liquid dedirt passage Coacervation plate and the condensation for coalescing dividing plate 1211, the profit compound in air and solid granulates are separated；

Preferably, the first inspection socket 123 is arranged on sealing shell body 1, and positioned at the first de- He of liquid dedirt passage 121 At second de- liquid dedirt passage 122, for the situation in observation passage and the first de- 121 and second de- liquid of liquid dedirt passage is safeguarded Dedirt passage 122；First coacervation plate 1212, the second coacervation plate 1222 and the 3rd coacervation plate 1221 use aluminum material.

First de- liquid dedirt passage 121 is vertically arranged, and the second de- liquid dedirt passage 122 is horizontally disposed, the oil being separated Hydrate and solid granulates prevent because the effect of gravity flows to its port of export from the arrival end of the first de- liquid dedirt passage 121 Dirt is accumulated in passage；Refilter system 13, energetic ion pipe group 14, low-temperature plasma purifying device 15, activated carbon filter plate Layer 16 is arranged at the top of the second de- liquid dedirt passage 122.

Preferably, the first de- middle part of liquid dedirt passage 121 is provided with first pressure table 18.

With reference to shown in Fig. 1 and Fig. 3, the bottom of the 3rd coacervation plate 1221 is provided with leakage fluid dram 1226, adjacent two pieces of trimerizations The position of leakage fluid dram 1226 on solidifying plate 1221 is different, so that each 3rd coacervation plate in the second de- liquid dedirt passage 122 Profit compound and solid granulates between 1221 can be shunted averagely；The port of export of second de- liquid dedirt passage 122 is provided with liquid Body collecting tank 1223, to store the profit compound of deposition and solid granulates；Oil-water discharge is provided with sealing shell body 1 Valve 1224, and oil-water discharge valve 1224 is located at liquid collection trough 1223, can periodically discharge the profit compound and solid-state of deposition Particle；Liquid level gauge 1225 is provided with sealing shell body 1, and liquid level gauge 1225 is located at liquid collection trough 1223, for observation The capacity of liquid is stored up in case groove.

Refiltering system 13 includes cushion chamber 131, air filtering core group 132 and flows filter plate assembly, the entrance of cushion chamber 131 The port of export for taking off liquid passage 122 with the second dedirt is held to connect, air filtering core group 132 is arranged in cushion chamber 131, flows filter plates Part is located at outside cushion chamber 131, and at the port of export of cushion chamber 131.

Stream filter plate assembly is removably disposed in sealing shell body 1, is easy to current check to flow filter plates with changing Part also includes flowing filter plate carrier 133 and flows filter plate 134, flows filter plate 134 and is arranged on and flows on filter plate carrier 133.

Preferably, the inspection socket 135 of second pressure gauge 19 and second is provided with sealing shell body 1, and second pressure gauge 19 and second inspection socket 135 be located at the port of export of cushion chamber 131, second pressure gauge 19 can compare with first pressure table 18, With judge air in passage it is whether smooth；Second inspection socket 135 is observing and safeguard air filtering core group 132.

With reference to shown in Fig. 2 and Fig. 5, energetic ion pipe group 14 is removably disposed in sealing shell body 1, energetic ion pipe Group 14 includes carrier 141, multiple ion pipe units 143 and photocatalysis net 142, and photocatalysis net 142 is arranged on carrier 141, more The individual ion pipe unit 143 is arranged to two rows, and parallel with photocatalysis net 142, wherein row's ionic tube is located at photocatalysis net 142 sides, another row's ionic tube are located at the opposite side of photocatalysis net 142；The two neighboring ion pipe unit 143 of each row's ionic tube Spacing is H, and wherein H is 120~160mm；The width of energetic ion pipe group 14 is L, and wherein L is 300mm；Energetic ion pipe group 14 Substantial amounts of positive and negative particle can be produced after energization, positive and negative particle collides to form positive and negative ion with the oxygen molecule in air, positive oxonium ion With very strong oxidisability, can in very short time internal oxidition, decompose the pollution factors such as methyl mercaptan, ammonia, hydrogen sulfide, and with VOC Molecule opens the chemical bond of volatile organic gas after being in contact, ultimately generate carbon dioxide and water etc. and stablize harmless molecule.

It is preferably, pre- on sealing shell body 1, and between the system that refilters 13 and low-temperature plasma purifying device 15 The redundancy groove position of multiple high energy plasma pipe groups 14 is left, for increasing and decreasing high energy plasma pipe group 14 during use according to demand.

With reference to shown in Fig. 4 and Fig. 6 to Fig. 8, low-temperature plasma purifying device 15 includes power supply module 155 and plasma cleaning Module, sealing shell body 1 are provided with electric field and check window 1554, and plasma cleaning module is located in sealing shell body 1, and is located at Electric field is checked at window 1554；The lid of power supply module 155 is located at electric field and checked on window 1554, and one end checks window with the electric field The side wall rotation connection of mouth 1554, the power supply module 155 are provided with safety switch 156.

Plasma cleaning module includes support body 158, minus plate 153, anode module 157 and multiple cathode electrodes 152, anode Module 157 is arranged on support body 158, and anode module 157 includes multiple anode canisters 151, and minus plate 153 is arranged on support body 158 Side, minus plate 153 are connected with anode module 157 by the first insulator 154, one end connection of multiple cathode electrodes 152 On minus plate 153, and it is inserted into correspondingly in anode canister 151；Because anode produces corona discharge, air is by rapid electricity From positively charged contaminant particles, having poison gas particle in the presence of powerful electric field force, hit cathode electrode and adsorption precipitation in the moon On pole electrode 152.

Power supply module 155 includes power supply 1556, radiator fan 1555, power supply indicator 1551, ammeter 1552 and safety Switch 156；Safety switch 156 includes power cable 1561, felt pad 1562, porcelain vase pot cover 1563, the second insulator 1564, no Become rusty steel spring 1565 and porcelain vase thimble 1566；Porcelain vase thimble 1566 is connected progress conduction with stainless steel spring 1565, then by second Insulator 1564 is used as insulation protection, is connected to power cable 1561 by the power supply line bar in the second insulator 1564, finally Insulation protection is used as by porcelain vase pot cover 1563 and felt pad 1562.

With reference to shown in Fig. 7, when power supply module 155 is opened, insulation fixing lock 1557 unlocks with power supply module 155, Porcelain vase thimble 1566 departs from and powered off with anode module 157.

With reference to shown in Fig. 8, when power supply module 155 is closed, porcelain vase thimble 1566 is made by the elasticity of stainless steel spring 1565 Contacted and be powered with anode module 157 is pressed into, now power supply module 155 is locked by insulation fixing lock 1557, to ensure electricity consumption Safety.

Preferably, the shape of cathode electrode 152 includes needle-like, wire, zigzag, star, prickle shape, fishbone knot Structure；Multiple power supplys 1556 correspond with multiple anode modules 157, the power supply of an electric field one are realized to control, to strengthen power supply Stability；And it is standard that the power of power supply 1556, which is selected with loaded more than anode module 157 1/3,.

With reference to shown in Fig. 1, activated carbon filter plate layer assembly is removably disposed in sealing shell body 1, is easy to current check With replacing, activated carbon filter plate layer assembly also includes activated carbon filter plate layer carrier 161 and activated carbon filter plate layer 16, activated carbon filter plate layer 16 are arranged on activated carbon filter plate layer carrier 161；Air is after the filtering of activated carbon filter plate layer 16, from the row of clean air outlet 17 Go out.

In summary, purification of the air by the de- liquid dedirt collection system 12 of this clarifier containing profit compound Afterwards, profit compound and solid granulates in air can be effectively separated, so as to realize that plasma purifier can be purifying aqueous The big gas of oil content；In this clarifier multiple components include flowing filter plate 134 and its carrier 133, energetic ion pipe group 14 and Its carrier 141, activated carbon filter plate layer 16 and its carrier 161 employ drawer type design for disassembly, rational in infrastructure with more Change.

Embodiment 2

The present embodiment is substantially the same manner as Example 1, and difference is, the second de- liquid dedirt passage 122 is changed by horizontally disposed To be obliquely installed, incline direction is that the second de- arrival end of liquid dedirt passage 122 takes off the port of export of liquid dedirt passage 122 higher than second, It is easy to the profit compound that deposits and solid particle voluntarily to flow to liquid collection trough 1223 under gravity, and just In the solidliquid mixture in liquid collection trough 1223 is discharged by oil-water discharge valve 1224.

Above-described embodiment is only used for further illustrating a kind of purification of low-altitude discharged waste gas purification processing of the present utility model Device, but the utility model is not limited to embodiment, it is every that above example is made according to the technical essence of the utility model Any simple modification, equivalent change and modification, each fall within the protection domain of technical solutions of the utility model.

Claims

1. a kind of clarifier of low-altitude discharged waste gas purification processing, it is characterised in that the clarifier includes sealing shell body, waste gas Entrance, de- liquid dedirt collection system, refilter system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer And clean air outlet；The exhaust gas entrance and clean air outlet are arranged on the sealing shell body, and the de- liquid takes off Dirt collection system, refilter system, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer and be arranged at shell In vivo, waste gas is entered in housing by the exhaust gas entrance, and is passed through the de- liquid dedirt collection system successively, refiltered and be System, energetic ion pipe group, low-temperature plasma purifying device, activated carbon filter plate layer are arranged after being purified from the clean air outlet Go out.

2. the clarifier of low-altitude discharged waste gas purification processing according to claim 1, it is characterised in that the de- liquid dedirt is received Collecting system includes the first de- liquid dedirt passage and the second de- liquid dedirt passage, the described first de- liquid dedirt feeder connection end with it is described Exhaust gas entrance connects, and the arrival end that the described first de- liquid dedirt channel outlet takes off liquid dedirt passage with second connects, and described the Provided with the first staggered coacervation plate of polylith in one de- liquid dedirt passage, multiple the are provided with the described second de- liquid dedirt passage Two coacervation plates and the 3rd coacervation plate, the second coacervation plate and the 3rd coacervation plate are staggered.

3. the clarifier of low-altitude discharged waste gas purification processing according to claim 2, it is characterised in that the described first de- liquid takes off Dirt passage is vertically arranged, and the described second de- liquid dedirt passage is horizontally disposed with, described to refilter system, energetic ion pipe group, low temperature Plasma purifier, activated carbon filter plate layer are arranged at the top of the described second de- liquid dedirt passage.

4. the clarifier that the low-altitude discharged waste gas purification according to Claims 2 or 3 is handled, it is characterised in that described second is poly- Solidifying plate is located on the roof of the described second de- liquid dedirt passage, and the 3rd coacervation plate is arranged on the described second de- liquid dedirt passage Bottom wall on, the length of the second coacervation plate is less than the length of the 3rd coacervation plate.

5. the clarifier of low-altitude discharged waste gas purification processing according to claim 4, it is characterised in that the 3rd coacervation plate Bottom be provided with leakage fluid dram, the position of the leakage fluid dram on adjacent two blocks of the 3rd coacervation plates is different.

6. the clarifier of low-altitude discharged waste gas purification processing according to claim 5, it is characterised in that the described second de- liquid takes off The port of export of dirt passage is provided with liquid collection trough.

7. the clarifier of low-altitude discharged waste gas purification processing according to claim 1, it is characterised in that described to refilter system Filter plate assembly is flowed including cushion chamber, air filtering core group and, the filter plate assembly that flows also includes flowing filter plate carrier and flowed Filter plate, flow filter plate and be arranged on stream filter plate carrier, the entrance point of the cushion chamber takes off going out for liquid collection system with the dedirt The connection of mouth end, the air filtering core group are arranged in the cushion chamber, and the stream filter plate is located at outside the cushion chamber, and is located at At the port of export of the cushion chamber.

8. the clarifier of low-altitude discharged waste gas purification processing according to claim 1, it is characterised in that the energetic ion pipe Group is detachably arranged in the sealing shell body, and the ionic tube group includes body, multiple ion pipe units and photocatalysis net, The photocatalysis net is set on the body, and multiple ion pipe units are arranged to two rows, and are put down with the photocatalysis net OK, wherein row's ionic tube is located at photocatalysis net side, another row's ionic tube is located at photocatalysis net opposite side.

9. the clarifier of low-altitude discharged waste gas purification processing according to claim 1, it is characterised in that the low-temperature plasma Purifier includes power supply module and plasma cleaning module, and the sealing shell body is provided with electric field and checks window, described etc. Ion cleaning module is located in the sealing shell body, and checks at window that the power supply module lid is located at positioned at the electric field The electric field is checked on window, and one end checks that the side wall of window is rotatablely connected with the electric field, and the power supply module is provided with Safety switch.

10. the clarifier of low-altitude discharged waste gas purification processing according to claim 9, it is characterised in that the plasma is net Changing module includes support body, minus plate, multiple anode tubes and multiple cathode electrodes, and multiple anode tubes are arranged on support body, institute The side that minus plate is arranged on the support body is stated, one end of multiple cathode electrodes is connected on minus plate, and is corresponded Ground is inserted into the anode tube.