CN203724958U - System for processing volatile gas at periphery of toll station - Google Patents
System for processing volatile gas at periphery of toll station Download PDFInfo
- Publication number
- CN203724958U CN203724958U CN201320876512.5U CN201320876512U CN203724958U CN 203724958 U CN203724958 U CN 203724958U CN 201320876512 U CN201320876512 U CN 201320876512U CN 203724958 U CN203724958 U CN 203724958U
- Authority
- CN
- China
- Prior art keywords
- gas
- treating apparatus
- charge station
- escaping gas
- air inlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000012545 processing Methods 0.000 title abstract description 11
- 238000001035 drying Methods 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims description 48
- 239000011941 photocatalyst Substances 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 32
- 239000003610 charcoal Substances 0.000 claims description 29
- 229910052799 carbon Inorganic materials 0.000 claims description 28
- 238000000746 purification Methods 0.000 claims description 28
- 239000002250 absorbent Substances 0.000 claims description 17
- 230000002745 absorbent Effects 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 15
- 230000003647 oxidation Effects 0.000 claims description 14
- 238000007254 oxidation reaction Methods 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 14
- 239000007921 spray Substances 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 8
- 239000003814 drug Substances 0.000 claims description 7
- 238000003860 storage Methods 0.000 claims description 7
- 238000004378 air conditioning Methods 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 238000013461 design Methods 0.000 abstract description 3
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 123
- 239000012530 fluid Substances 0.000 description 20
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 238000010586 diagram Methods 0.000 description 7
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 6
- OUUQCZGPVNCOIJ-UHFFFAOYSA-M Superoxide Chemical compound [O-][O] OUUQCZGPVNCOIJ-UHFFFAOYSA-M 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 5
- 239000000945 filler Substances 0.000 description 4
- 229960002163 hydrogen peroxide Drugs 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000006253 efflorescence Methods 0.000 description 1
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 1
- -1 hydroxyl free radical Chemical class 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 206010037844 rash Diseases 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000012224 working solution Substances 0.000 description 1
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a system for processing volatile gas at periphery of a toll station, which comprises a volatile gas processing device, a blower, a volatile gas region at the periphery of the toll station and the closed toll station, wherein the volatile gas processing device is provided with a gas inlet and a gas outlet; the blower is provided with a gas inlet and a gas outlet; the toll station is provided with a gas inlet and a gas outlet; and the volatile gas region at the periphery of the toll station is connected with the gas inlet of the volatile gas processing device through a pipeline, the gas outlet of the volatile gas processing device is connected with the gas inlet of the toll station through a pipeline, the gas outlet of the toll station is connected with the gas inlet of the blower, and the gas outlet of the blower is connected with the gas inlet of the volatile gas processing device. According to the utility model, the system is simple in structure, convenient to use, reasonable in design, energy-saving and environment-friendly. The processed gas is communicated with the gas inlet of the toll station through a gas outlet of a drying tower, thereby realizing true cyclic utilization.
Description
Technical field
The utility model relates to escaping gas process field, is specifically related to a kind of charge station system that escaping gas is processed around.
Background technology
The escaping gas that industrial activity produces is one of source of contaminated environment.Charge station on highway is very common, and is relatively airtight space, and the personnel that work in charge station are in the environment of vehicle exhaust for a long time.These volatile gases, sticky particle thing cannot efflorescence, and treatment cost is high, there is no effective improvement method, administer supervision easily in uncontrolled state, escaping gas is often not treated just directly enters atmosphere, becomes one of reason forming haze.
At present, in country's escaping gas governance standard, containing PM2.5, do not administer, escaping gas and PM2.5 production source are administered and need to be leaned on technology and equipment running to realize, how to solve the working environment of personnel in charge station, the toxic and harmful that automobile in its working environment is produced is processed, and is the difficult problem that people face.For these reasons, be badly in need of at present a kind of charge station system that escaping gas is processed around.
Utility model content
The purpose of this utility model is to provide a kind of working environment that can improve personnel in charge station, makes the quality of the escaping gas after processing reach charge station's escaping gas of discharging standards and the treatment system of PM2.5.
In order to overcome the deficiencies in the prior art, the technical scheme that the utility model provides is: a kind of charge station system that around escaping gas is processed, and the described charge station system that around escaping gas is processed comprises escaping gas region around of escaping gas treating apparatus, blower fan, charge station and the charge station of sealing; On described escaping gas treating apparatus, be provided with air inlet and gas outlet, on described blower fan, be provided with air inlet and gas outlet; In described charge station, be provided with air inlet and gas outlet;
Described charge station escaping gas region is around connected with the air inlet of escaping gas treating apparatus by pipeline, the gas outlet of described escaping gas treating apparatus is connected with the air inlet of charge station by pipeline, the gas outlet of described charge station is connected with the air inlet of blower fan, and the gas outlet of described blower fan is connected with the air inlet of escaping gas treating apparatus.
Further, the described charge station system that around escaping gas is processed also comprises and is provided with central air-conditioning; Described central air-conditioning is arranged between escaping gas treating apparatus and charge station.
Further, described blower fan is one or more; Described blower fan be arranged in escaping gas treating apparatus or be arranged at escaping gas and charge station escaping gas region around between or be arranged between escaping gas treating apparatus and charge station.
Further, gas double purification device and drying tower between described escaping gas treating apparatus and charge station, be provided with air inlet and gas outlet on described drying tower; On described gas double purification device, be provided with air inlet and gas outlet;
The gas outlet of described charge station is connected with the air inlet of escaping gas treating apparatus by pipeline, and the gas outlet of described escaping gas treating apparatus is connected with the air inlet of gas double purification device; The gas outlet of described gas double purification device is connected with the air inlet of drying tower by pipeline; The gas outlet of described drying tower is connected with the air inlet of blower fan.
Further, the air inlet place of described escaping gas treating apparatus is provided with particle filtering net; The air inlet place of described drying tower is provided with particle filtering net; Described double purification device is water curtain tower.
Further, described escaping gas treating apparatus comprise in filter, low-temperature plasma treating apparatus, photocatalyst treating apparatus, absorbent charcoal adsorber or vapour phase oxidation process treating apparatus any one or several arbitrarily.
Further, described filter, low-temperature plasma treating apparatus, photocatalyst treating apparatus, absorbent charcoal adsorber, vapour phase oxidation process treating apparatus are connected successively by pipeline; Described vapour phase oxidation process treating apparatus comprises spray column, liquid medicine water storage box and water pump; Described low-temperature plasma treating apparatus comprises low-temperature plasma generator and low-temperature plasma generator guide rail, by being provided with low-temperature plasma generator on low-temperature plasma generator guide rail;
Described photocatalyst treating apparatus comprises ultraviolet ray photocatalyst generator and ultraviolet ray photocatalyst generator guide rail, on described ultraviolet ray photocatalyst generator guide rail, is provided with ultraviolet ray photocatalyst generator.
Further, described low-temperature plasma generator power supply is connected with low-temperature plasma generator by electric connection line, to low-temperature plasma generator, provides power supply; Ultraviolet ray photocatalyst generator power is connected with ultraviolet ray photocatalyst generator by electric connection line, to ultraviolet ray photocatalyst generator, provides power supply.
Further, described absorbent charcoal adsorber comprises charcoal treatment casing; In described absorbent charcoal adsorber, be provided with active carbon.
Further, described active carbon is cylindrical particle active carbon.
Beneficial effect: the charge station of the present utility model system that around escaping gas is processed, simple in structure, easy to use, reasonable in design, energy-conserving and environment-protective.
(1) escaping gas molecule obtains nontoxic gas after treatment, and native system has been guaranteed escaping gas purification up to standard, has surpassed national relevant emission standards;
(2) if the gas after processing is connected with the gas outlet of drying tower and the air inlet of charge station, can realize recycling of gas.PM2.5 in gas is also processed, effectively avoided the generation of haze.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model;
Fig. 2 is the schematic diagram of embodiment mono-of the present utility model;
Fig. 3 is the internal structure plane of low-temperature plasma treating apparatus of the present utility model;
Fig. 4 is the internal structure plane of photocatalyst treating apparatus of the present utility model;
Fig. 5 is the internal structure front elevation of low-temperature plasma treating apparatus of the present utility model;
Fig. 6 is the internal structure front elevation of photocatalyst treating apparatus of the present utility model;
Fig. 7 is the structural plan figure of photocatalyst generator of the present utility model;
Fig. 8 is the double-dielectric barrier discharge structural representation in low-temperature plasma generator of the present utility model;
The schematic diagram of Fig. 9 absorbent charcoal adsorber of the present utility model;
The internal framework schematic diagram of Figure 10 absorbent charcoal adsorber of the present utility model;
Figure 11 is the drawer structure schematic diagram of absorbent charcoal adsorber of the present utility model;
Figure 12 is the charcoal absorption schematic diagram of absorbent charcoal adsorber of the present utility model;
Figure 13 is the schematic diagram of vapour phase oxidation process treating apparatus of the present utility model;
Wherein: 1 escaping gas treating apparatus; 2 blower fans; 3 charge stations; The gas outlet of 301 charge stations; The air inlet of 302 charge stations; 4 charge stations escaping gas region around; 5 gas double purification devices; 6 particle filtering nets; 7 activated carbon; 8 honeycomb active carbon filter nets; 9 water curtain towers; 10 drying towers; 11 filters; 12 low-temperature plasma treating apparatus; 1201 low-temperature plasma generators; 1202 plasma pulse power supplys; 1203 low-temperature plasma generator power supplys; 1204 low-temperature plasma generator guide rails; 1205 earth electrodes; 1206 block medias; 1207 high-field electrodes; 1208 discharging gaps; 13 photocatalyst treating apparatus; 1301 ultraviolet ray photocatalyst generators; 1302 quartz burners; 1303 ultraviolet ray photocatalyst generator powers; 1304 photocatalyst net power supplys; 1305 ultraviolet ray photocatalyst generator guide rails; 14 absorbent charcoal adsorbers; 1401 air inlets; 1402 gas outlets; 1403 active carbon drawers; 1404 quick clips; 1405 charcoal treatment casings; 1406 intercept net; 1407 labyrinth, gas outlet baffle plates; 1408 drawer handles; 1409 lower margins; 1410 access doors; 1411 active carbons; 1412 air inlet labyrinth baffle plates; 1413 cross flow proof dividing plates; 1414 support keels; 1415 drawer rails; 15 vapour phase oxidation process treating apparatus; 1501 spray columns; 1502 liquid medicine water storage boxes; 1505 water pumps; 1506 air inlets; 1507 circulation fluid pipelines; 1508 water inlet valves; 1509 mouth sprays; 1510 filler rooms; 1511 gas outlets.
The specific embodiment
Below in conjunction with Figure of description, the utility model is described further.
Embodiment 1
As shown in figure 1 to figure 13, the utility model provides a kind of charge station system that escaping gas is processed around, and the described charge station system that around escaping gas is processed comprises escaping gas treating apparatus 1, charge station escaping gas region 4 around and the charge station 3 of sealing; On described escaping gas treating apparatus 1, be provided with air inlet and gas outlet, in described charge station 3, be provided with air inlet and gas outlet;
Described charge station escaping gas region 4 is around connected with the air inlet of escaping gas treating apparatus 1 by pipeline, the gas outlet of described escaping gas treating apparatus 1 is connected with the air inlet 302 of charge station 3 by pipeline, the gas outlet 301 of described charge station 3 is connected with the air inlet of blower fan 2, and the gas outlet of described blower fan 2 is connected with the air inlet of escaping gas treating apparatus 1.
The described charge station system that around escaping gas is processed also comprises and is arranged at drying tower 10 and the gas double purification device 5 of escaping gas treating apparatus 1 between charge station, on described drying tower 10, is provided with air inlet and gas outlet; On described gas double purification device 5, be provided with air inlet and gas outlet;
The gas outlet of described charge station 3 is connected with the air inlet of escaping gas treating apparatus 1 by pipeline, and the gas outlet of described escaping gas treating apparatus 1 is connected with the air inlet of gas double purification device 5; The gas outlet of described gas double purification device 5 is connected with the air inlet of drying tower 10 by pipeline; The gas outlet of described drying tower 10 is connected with the air inlet of blower fan 2.
The air inlet place of described escaping gas treating apparatus 1 is provided with particle filtering net 6; The air inlet place of described drying tower 10 is provided with particle filtering net 6.
The gas outlet of described drying tower 10 is connected with the air inlet of blower fan 2.
The air inlet place of described drying tower 10 is provided with particle filtering net 6.In described gas double purification device 5, be provided with activated carbon 7, in described gas double purification device 5, be provided with honeycomb active carbon filter net 8.
Described gas double purification device 5 is water curtain tower 9.
Described water curtain tower 9 comprises casing, recycle liquid pump, holds liquid case, recycle liquid pump, distribution box, liquid barrier, clean-up port, blowoff valve and fluid infusion mouth.Described box inside rear portion is provided with liquid curtain plate a, liquid curtain plate b;
Described liquid curtain plate a comprises that circulation fluid case a and dentation curtain are along a; Described liquid curtain plate a top is provided with circulation fluid case a, and circulation fluid case a is provided with overfall a, and the circulation fluid Direct Uniform trickling of overfall a overflow is on liquid curtain plate a, and liquid curtain plate a bottom is provided with dentation curtain along a, and deflector a is housed;
Described liquid curtain plate b comprises that circulation fluid case b and dentation curtain are along b; Described liquid curtain plate b top is provided with circulation fluid case b, and circulation fluid case b is provided with overfall b, and the circulation fluid Direct Uniform trickling of overfall b overflow is on liquid curtain plate b; Liquid curtain plate b bottom is provided with dentation curtain along b, and deflector b is housed.
Described lower box is provided with liquid bath, in liquid bath one side, is provided with liquid bath overfall; Described casing arranged outside has the liquid of holding case, described liquid bath overfall with hold liquid case and be connected; The described liquid case that holds is provided with inlet and liquid outlet;
Described inlet is used for supplying and holds liquid case liquid, keeps liquid level; Blowoff valve is equipped with in the described liquid case bottom of holding, for holding the blowdown of liquid case; The described liquid holding in liquid case is water or oil or anti-icing fluid; Described liquid case one side of holding is provided with recycle liquid pump, the inlet of recycle liquid pump by pipeline with hold liquid case and be connected; Liquid-controlling valve a, liquid-controlling valve b are housed respectively, for controlled circulation liquid case a and circulation fluid case b feed liquor amount, to keep certain liquid level on described recycle liquid pump;
The liquid outlet of recycle liquid pump is connected with circulation fluid case a and circulation fluid case b respectively by circulation fluid pipe; Liquid-controlling valve c is housed in the input duct of described recycle liquid pump.
Described carbon dioxide, water and unnecessary superoxide anion enter water curtain tower 6, and superoxide anion is decomposed into rapidly oxygen by the recirculated water in gas double purification device 4; Moisture escaping gas enters gas double purification device 5.In gas double purification device 5, be provided with active carbon and honeycomb active carbon filter net, described gas double purification device 5 absorbs steam.
Described escaping gas treating apparatus 1 comprises filter 11, low-temperature plasma treating apparatus 12, photocatalyst treating apparatus 13, absorbent charcoal adsorber 14, vapour phase oxidation process treating apparatus 15;
Described filter 11, low-temperature plasma treating apparatus 12, photocatalyst treating apparatus 13, absorbent charcoal adsorber 14, vapour phase oxidation process treating apparatus 15 are connected successively by pipeline;
Described low-temperature plasma treating apparatus 12 comprises low-temperature plasma generator 1201 and low-temperature plasma generator guide rail 1204, and described low-temperature plasma generator 1201 is arranged on low-temperature plasma generator guide rail 1204;
Described photocatalyst treating apparatus 13 comprises ultraviolet ray photocatalyst generator 1301 and ultraviolet ray photocatalyst generator guide rail 1305, and described ultraviolet ray photocatalyst generator 1301 is arranged on ultraviolet ray photocatalyst generator guide rail 1305;
Described low-temperature plasma generator power supply 1203 is connected with low-temperature plasma generator 1201 by electric connection line, to low-temperature plasma generator 1201, provides electric energy; Described ultraviolet ray photocatalyst generator power 1303 is connected with ultraviolet ray photocatalyst generator 1301 by electric connection line, to ultraviolet ray photocatalyst generator 1301, provides electric energy.
In described low-temperature plasma generator 1201, be provided with high-field electrode 1207, earth electrode 1205, and block media 1206 is housed, between high-field electrode 1207 and earth electrode 1205, be provided with discharging gap 1208, high-field electrode 1207 is connected with plasma pulse power supply 1202 respectively by wire with earth electrode 1205;
Described ultraviolet ray photocatalyst generator 1301 is provided with quartz burner 1302, in quartz burner 1302 peripheries, is provided with photocatalyst net, and described photocatalyst net is connected with photocatalyst net power supply 1304 by electric connection line.
Escaping gas, under the splitting action of low-temperature plasma treating apparatus 12, is decomposed into subset by macromolecular mass, by ozone oxidation carbon dioxide and water;
The small-sized organic molecule group not decomposed completely, enters photocatalyst treating apparatus 13 and carries out photodissociation cleansing phase, and superoxide anion and hydroxyl free radical that escaping gas is produced by photocatalyst treating apparatus 13 are oxidizing to end product carbon dioxide and water;
Described absorbent charcoal adsorber 14 comprises charcoal treatment casing 1405.Described absorbent charcoal adsorber 14 comprises charcoal treatment casing 1405.Described charcoal treatment casing 1405 comprises active carbon drawer 1403, drawer rail 1415, quick clip 1404, drawer handle 1408, active carbon 1411, intercepts net 1406, air inlet labyrinth baffle plate 1412, labyrinth, gas outlet baffle plate 1407, cross flow proof dividing plate 1413, support keel 1414 and netted collet.Active carbon 1411 is a kind of porous carbon containing matters, it has highly developed hole structure, the loose structure of active carbon 1411 provides a large amount of surface areas for it, can fully contact with gaseous impurity, thereby given active carbon 1411 peculiar absorption property, made it be very easy to reach the object that absorbs collection impurity.As magnetic force, between all molecules, all there is attractive interaction.Just because of this, a large amount of molecule on active carbon 1411 hole walls can produce powerful gravitation, thereby reach, harmful impurity is attracted to the object in aperture.
On described drawer rail 1415, be provided with active carbon drawer 1403, active carbon drawer 1403 is fixedly connected by quick clip 1404 and charcoal treatment casing 1405.Described active carbon drawer 1403 bottoms are provided with netted collet, and active carbon drawer 1403 front portions are provided with drawer handle 1408.Described active carbon drawer 1408 is more than 2 or 2.One side of the air inlet 1401 of described charcoal treatment casing 1405 is provided with and intercepts net 1406 and air inlet labyrinth baffle plate 1412, in the gas outlet 1402 of charcoal treatment casing 1405, is provided with labyrinth, gas outlet baffle plate 1407.Lower margin 1409 is equipped with in described charcoal treatment casing 1405 bottoms; One side of described charcoal treatment casing 1405 is provided with access door 1410.
In described active carbon drawer 1408, be provided with active carbon 1411.Described active carbon 1411 is cylindrical particle active carbon 1416, and the interior absorption of described cylindrical particle active carbon 1416 has impurity molecule 1417.
Described vapour phase oxidation process treating apparatus 15 comprises spray column 1501, liquid medicine water storage box 1502 and water pump 1505, on described water pump 1505, is provided with water inlet and water out.
One side of described spray column 1501 is provided with water pump 1505, and described liquid medicine water storage box 1502 is connected with water pump 1505 water inlets by pipeline; Described water pump 1505 delivery ports are connected with spray column 1501 by circulation fluid pipeline 1507, and described spray column 1501 is connected with the liquid medicine water storage box 1502 of its underpart by pipeline.
Described spray column 1501 bottoms are provided with air inlet 1506, and spray column 1501 tops are provided with gas outlet 15011.
On circulation fluid pipeline 1507 in described spray column 1501, be provided with mouth spray 1509, on the circulation fluid pipeline 1507 of water pump 1505 delivery ports, be provided with water inlet valve 1508.Described spray column 1501 bottoms are provided with circulation fluid outlet 1503, and described circulation fluid outlet 1503 is connected with the pipeline that is provided with water outlet valve 1504; Described water outlet valve 1504 is connected with liquid medicine water storage box 1502.
In described spray column 1501, be provided with filler room 1510, filler is equipped with filler in room.
In described vapour phase oxidation process treating apparatus 15, be provided with solvent and solution, the described solvent of processing for escaping gas is water, and solution is oxydol H
2o
2composite absorption liquid with DORC formation.
The solvent that in described vapour phase oxidation process treating apparatus 15, escaping gas is processed is water, is equipped with a certain amount of oxydol H
2o
2form composite absorption liquid with DORC; There is the hydrogen peroxide of strong oxidability under the synergy of DORC, to produce the reaction of chain biography, hydrogen peroxide is all cleaved into two with not matching only electronics gene along weak bond, in working solution high speed, produce a large amount of strong oxidizing property hydroxyl radical free radicals, make the organic molecule in escaping gas be oxidized to carbon dioxide and water;
Described carbon dioxide, water and unnecessary superoxide anion enter water curtain tower 9, superoxide anion is decomposed into rapidly the moisture escaping gas of oxygen by the recirculated water in gas double purification device 5 and enters gas double purification device 5, in gas double purification device 5, be provided with activated alumina and activated alumina screen pack, described gas double purification device 5 absorbs steam.
The charge station of the present utility model system that around escaping gas is processed, simple in structure, easy to use, reasonable in design, energy-conserving and environment-protective.
(1) escaping gas molecule obtains nontoxic gas after treatment, and native system has been guaranteed escaping gas purification up to standard, has surpassed national relevant emission standards;
(2) if the gas after processing is connected with the air inlet of charge station 3 with the gas outlet of drying tower, can realize recycling of gas.PM2.5 in gas is also processed, effectively avoided the generation of haze.
The above is only preferred embodiment of the present utility model; be noted that for those skilled in the art; do not departing under the prerequisite of the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (10)
- The 1.Yi Zhong charge station system that around escaping gas is processed, is characterized in that: the described charge station system that around escaping gas is processed comprises escaping gas region around of escaping gas treating apparatus, blower fan, charge station and the charge station of sealing; On described escaping gas treating apparatus, be provided with air inlet and gas outlet, on described blower fan, be provided with air inlet and gas outlet; In described charge station, be provided with air inlet and gas outlet;Described charge station escaping gas region is around connected with the air inlet of escaping gas treating apparatus by pipeline, the gas outlet of described escaping gas treating apparatus is connected with the air inlet of charge station by pipeline, the gas outlet of described charge station is connected with the air inlet of blower fan, and the gas outlet of described blower fan is connected with the air inlet of escaping gas treating apparatus.
- 2. the charge station according to claim 1 system that around escaping gas is processed, is characterized in that: the described charge station system that around escaping gas is processed also comprises central air-conditioning; Described central air-conditioning is arranged between escaping gas treating apparatus and charge station.
- 3. the charge station according to claim 2 system that around escaping gas is processed, is characterized in that: described blower fan is one or more; Described blower fan be arranged in escaping gas treating apparatus or be arranged at escaping gas and charge station escaping gas region around between or be arranged between escaping gas treating apparatus and charge station.
- 4. the charge station according to claim 3 system that around escaping gas is processed, is characterized in that: gas double purification device and drying tower between described escaping gas treating apparatus and charge station, be provided with air inlet and gas outlet on described drying tower; On described gas double purification device, be provided with air inlet and gas outlet;The gas outlet of described charge station is connected with the air inlet of escaping gas treating apparatus by pipeline, and the gas outlet of described escaping gas treating apparatus is connected with the air inlet of gas double purification device; The gas outlet of described gas double purification device is connected with the air inlet of drying tower by pipeline; The gas outlet of described drying tower is connected with the air inlet of blower fan.
- 5. the charge station according to claim 4 system that around escaping gas is processed, is characterized in that: the air inlet place of described escaping gas treating apparatus is provided with particle filtering net; The air inlet place of described drying tower is provided with particle filtering net; Described double purification device is water curtain tower.
- 6. the charge station according to claim 5 system that around escaping gas is processed, is characterized in that: described escaping gas treating apparatus comprise in filter, low-temperature plasma treating apparatus, photocatalyst treating apparatus, absorbent charcoal adsorber or vapour phase oxidation process treating apparatus any one or several arbitrarily.
- 7. the charge station according to claim 6 system that around escaping gas is processed, is characterized in that: described filter, low-temperature plasma treating apparatus, photocatalyst treating apparatus, absorbent charcoal adsorber, vapour phase oxidation process treating apparatus are connected successively by pipeline; Described vapour phase oxidation process treating apparatus comprises spray column, liquid medicine water storage box and water pump; Described low-temperature plasma treating apparatus comprises low-temperature plasma generator and low-temperature plasma generator guide rail, by being provided with low-temperature plasma generator on low-temperature plasma generator guide rail;Described photocatalyst treating apparatus comprises ultraviolet ray photocatalyst generator and ultraviolet ray photocatalyst generator guide rail, on described ultraviolet ray photocatalyst generator guide rail, is provided with ultraviolet ray photocatalyst generator.
- 8. the charge station according to claim 7 system that around escaping gas is processed, is characterized in that: described low-temperature plasma generator power supply is connected with low-temperature plasma generator by electric connection line, to low-temperature plasma generator, provides power supply; Ultraviolet ray photocatalyst generator power is connected with ultraviolet ray photocatalyst generator by electric connection line, to ultraviolet ray photocatalyst generator, provides power supply.
- 9. the charge station according to claim 6 system that around escaping gas is processed, is characterized in that: described absorbent charcoal adsorber comprises charcoal treatment casing; In described absorbent charcoal adsorber, be provided with active carbon.
- 10. the charge station according to claim 9 system that around escaping gas is processed, is characterized in that: described active carbon is cylindrical particle active carbon.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320876512.5U CN203724958U (en) | 2013-12-29 | 2013-12-29 | System for processing volatile gas at periphery of toll station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320876512.5U CN203724958U (en) | 2013-12-29 | 2013-12-29 | System for processing volatile gas at periphery of toll station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203724958U true CN203724958U (en) | 2014-07-23 |
Family
ID=51195059
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320876512.5U Expired - Fee Related CN203724958U (en) | 2013-12-29 | 2013-12-29 | System for processing volatile gas at periphery of toll station |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203724958U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307321A (en) * | 2014-09-22 | 2015-01-28 | 北京华创朗润环境科技有限公司 | Non-contact type synergistic-oxidation method waste gas purification machine |
| CN111167535A (en) * | 2018-11-13 | 2020-05-19 | 上海重智科技发展有限公司 | Volatile gas automatic purification experiment table |
-
2013
- 2013-12-29 CN CN201320876512.5U patent/CN203724958U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104307321A (en) * | 2014-09-22 | 2015-01-28 | 北京华创朗润环境科技有限公司 | Non-contact type synergistic-oxidation method waste gas purification machine |
| CN111167535A (en) * | 2018-11-13 | 2020-05-19 | 上海重智科技发展有限公司 | Volatile gas automatic purification experiment table |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102784550B (en) | System for treatment of spraying organic waste gas by circulating liquid curtain | |
| CN203017966U (en) | Circulating liquid curtain spray coating organic waste gas treatment system | |
| CN201454339U (en) | Composite harmful waste gas purification device | |
| CN205760609U (en) | A kind of device for low-temperature plasma synergistic catalysis treatment organic exhaust gas | |
| CN204293566U (en) | A kind of waste gas treatment equipment adopting ultraviolet catalytic technology | |
| CN106178945A (en) | A kind of plasma light catalytic control equipment | |
| CN203724958U (en) | System for processing volatile gas at periphery of toll station | |
| CN203724959U (en) | Volatile gas processing and recycling system | |
| CN103706216A (en) | System and method for treating volatile gas and PM2.5 (particulate matter2.5) produced by cooking process | |
| CN103706610A (en) | Volatile gas and PM2.5 treatment system and method in metal plastic molding production process | |
| CN107029533A (en) | A kind of multifunctional purifying removes the method and device of oil flue waste gas | |
| CN206535372U (en) | New waste gas filtration and adsorption treatment device | |
| CN103721513A (en) | Volatile gas processing system and method | |
| CN103691246A (en) | Volatile gas treatment recycling system and method thereof | |
| CN206285631U (en) | A kind of low-temperature plasma purifying device of additional adsorption unit | |
| CN203724960U (en) | Volatile gas processing system | |
| CN203797809U (en) | Industrial air purifier | |
| CN203725470U (en) | Processing system of volatile gas generated in metal plastic molding production process | |
| CN201906560U (en) | Treatment device capable of discharging dirt from gas | |
| CN103721512A (en) | System and method for treating volatile gases and PM2.5 (Particulate Matter 2.5) around toll station | |
| CN206215039U (en) | A kind of plasma light catalytic control equipment | |
| CN203725026U (en) | System for treating volatile gas and PM2.5 (Particulate Matter 2.5) in cooking process | |
| CN203724979U (en) | Activated carbon volatile gas and PM2.5 treatment system | |
| CN203724993U (en) | Low-temperature plasma volatile gas and PM2.5 treatment system | |
| CN211514047U (en) | Low-temperature plasma synergistic adsorption industrial waste gas treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: NANJING SHENLIU MACHINERY EQUIPMENT MANUFACTURING Free format text: FORMER OWNER: SUN JINKUI Effective date: 20150213 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 210003 NANJING, JIANGSU PROVINCE TO: 211806 NANJING, JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150213 Address after: 211806 Nanjing Ning industrial concentration area, Pukou District, Jiangsu, 19-8, Nanjing Patentee after: Nanjing Shenliu Mechanical Equipment Manufacturing Co.,Ltd. Address before: 801, room 02, building 41, pizza garden, 210003 East Bay, Gulou District, Jiangsu, Nanjing Patentee before: Sun Jinkui |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140723 |