CN210171179U - Cloud and mist supergravity VOC processing system with high-energy UV sterilization function - Google Patents
Cloud and mist supergravity VOC processing system with high-energy UV sterilization function Download PDFInfo
- Publication number
- CN210171179U CN210171179U CN201920112731.3U CN201920112731U CN210171179U CN 210171179 U CN210171179 U CN 210171179U CN 201920112731 U CN201920112731 U CN 201920112731U CN 210171179 U CN210171179 U CN 210171179U
- Authority
- CN
- China
- Prior art keywords
- water
- cloud
- mist
- centrifugal
- filter
- 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
- 239000003595 mist Substances 0.000 title claims abstract description 52
- 230000001954 sterilising effect Effects 0.000 title description 4
- 238000004659 sterilization and disinfection Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 120
- 238000001914 filtration Methods 0.000 claims abstract description 57
- 239000002912 waste gas Substances 0.000 claims abstract description 33
- 239000002351 wastewater Substances 0.000 claims abstract description 33
- 239000007921 spray Substances 0.000 claims abstract description 22
- 238000005507 spraying Methods 0.000 claims abstract description 15
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 14
- 231100000719 pollutant Toxicity 0.000 claims abstract description 14
- 238000006303 photolysis reaction Methods 0.000 claims abstract description 11
- 230000015843 photosynthesis, light reaction Effects 0.000 claims abstract description 9
- 238000011084 recovery Methods 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 29
- 239000004744 fabric Substances 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 8
- 230000002070 germicidal effect Effects 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 2
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 230000000249 desinfective effect Effects 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 4
- 239000008399 tap water Substances 0.000 abstract description 3
- 235000020679 tap water Nutrition 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 2
- 239000008213 purified water Substances 0.000 abstract description 2
- 239000008223 sterile water Substances 0.000 abstract description 2
- 239000012855 volatile organic compound Substances 0.000 description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 238000000746 purification Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000008187 granular material Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000010815 organic waste Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 150000007523 nucleic acids Chemical class 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000007084 catalytic combustion reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 102000039446 nucleic acids Human genes 0.000 description 2
- 108020004707 nucleic acids Proteins 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000002085 irritant Substances 0.000 description 1
- 231100000021 irritant Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Physical Water Treatments (AREA)
Abstract
The utility model provides a cloud and mist hypergravity VOC processing system that high energy UV disinfected, include: the device comprises a box body 1, a spraying and filtering device 2, a primary water filtering plate 3, a cloud and mist filtering device 4, a secondary water filtering plate 5, a super-gravity centrifugal device 6, an exhaust fan 7, a wastewater recovery device 8 and a photolysis device 9. The spray filter 2 and the cloud filter 4 preferably use water as a treatment medium, including tap water, purified water, sterile water, and other liquids having water as a primary carrier. The utility model provides a be difficult to among the prior art fully adsorb the technical problem of particulate pollutant and VOC in the waste gas, can reach the degree of pure air after handling, and adopt water as purifying material, have that use cost is low, adsorb advantages such as purify fully.
Description
Technical Field
The utility model belongs to the technical field of exhaust purification, a cloud and mist hypergravity VOC processing system that high energy UV disinfected is related to.
Background
Exhaust gas is gas discharged during industrial production, combustion of fossil fuels, combustion of garbage and industrial wastes, and driving of automobiles. According to the generation process, the method can be divided into: industrial organic waste gas, boiler smoke waste gas, industrial acid and alkali waste gas, industrial production peculiar smell, industrial harmful fine particles, automobile tail gas and the like. VOC is an acronym for volatile organic compounds (volatile organic compounds), and VOC exhaust gas generated in industrial production processes is more and more complex, and the direct emission of the exhaust gas has a great influence on the surrounding environment. The waste gas is discharged after being subjected to the standard through waste gas purification equipment.
In order to cooperate with environmental protection work, the existing enterprises improve the working environment of workers, reduce pollutant emission, reduce the influence of pollutants on the surrounding environment, collect and treat waste gas, and make the waste gas meet the standard and then be discharged. The main technologies for treating the volatile organic compound waste gas pollution at present are as follows: catalytic combustion, activated carbon adsorption, low temperature plasma, ultraviolet irradiation, and the like. The catalytic combustion technology has a thorough treatment effect, but needs higher concentration of organic waste gas, the concentration of the organic waste gas can not meet the combustion requirement, natural gas and the like are needed for auxiliary combustion, and the construction and operation costs of the method are higher. The adsorption effect of the activated carbon is ideal, but the activated carbon needs to be replaced regularly, and the replaced activated carbon becomes dangerous waste and needs to be recycled or regenerated, so that the cost is high and the maintenance is inconvenient. The removal rate of organic waste gas by low-temperature plasma and ultraviolet irradiation is not ideal.
The utility model aims at not only enabling the waste gas to reach the safety standard, but also enabling the waste gas to reach the degree of pure air after being processed. The utility model discloses a water is as purifying material, has characteristics such as use cost is low, absorption purification is abundant.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a cloud and mist hypergravity VOC processing system that high energy UV disinfected, this cloud and mist hypergravity VOC processing system that high energy UV disinfected can not only adsorb the solid pollutant particle in the waste gas, also can adsorb peculiar smell gas molecule and volatile organic compound gas molecule in the waste gas, and the most common has benzene, toluene, xylol, styrene etc. in the VOC waste gas.
The utility model provides a cloud and mist hypergravity VOC processing system that high energy UV disinfected, include: the box body is provided with an air inlet for sucking waste gas to be purified and an air outlet for discharging purified pure gas; the spraying and filtering device is positioned behind the air inlet, and a cavity inside the spraying and filtering device is communicated with the air inlet through a pipeline; a nozzle arranged in the spray filtering device forms water-like water drops through water pressure and is used for preliminarily mixing particle pollutants in the waste gas; the primary water filtering plate is positioned behind the spraying and filtering device and consists of a plurality of obliquely arranged water retaining sheets; the cloud and mist filtering device is positioned behind the primary filter plate, and a cavity inside the cloud and mist filtering device generates fine cloud and mist through an ultrasonic cloud and mist generator and is used for adsorbing peculiar smell and volatile gas molecules in the waste gas; the secondary water filtering plate is positioned behind the cloud and mist filtering device, and mesh water filtering holes are distributed on the secondary water filtering plate; the hypergravity centrifugal device is positioned behind the secondary water filtering plate, at least one centrifugal filter is arranged in the hypergravity centrifugal device, and filter cloth is arranged on the periphery of the centrifugal filter; the wastewater penetrating through the secondary water filtering plate flows into the centrifugal filter by virtue of wind power, and the wastewater is thrown into the filter cloth and collected by virtue of a supergravity centrifugal force generated by high-speed rotation of the centrifugal filter; the air exhaust fan is positioned behind the super-gravity centrifugal device and used for forming one-way airflow between the air inlet and the air outlet; and the photolysis device is positioned between the exhaust fan and the air outlet, an ultraviolet lamp is arranged in a cavity of the photolysis device and used for irradiating the pure gas after the cloud and mist are collected to kill bacteria, and the sterilized pure air is discharged from the air outlet.
In the cloud and hypergravity VOC treatment system with high-energy UV sterilization provided by the utility model, the spraying and filtering device comprises at least one water tank module, at least one water pump and at least one nozzle; the spray nozzles are distributed above the inner cavity of the spray filtering device and are sequentially connected with the water pump and the water tank module through pipelines; the water pump pumps water for spraying from the water tank module and generates high-strength water pressure to form water mist-shaped water drops through the nozzle.
The utility model provides in the cloud and mist hypergravity VOC processing system that high energy UV disinfected, set up the acid-base concentration monitor in the water tank module.
The utility model provides in the cloud hypergravity VOC processing system that high energy UV disinfected, still set up the separate shelf in cloud filter equipment's the inner chamber, separate the shelf and mark off a plurality of independent spaces in the inner chamber, set up in every independent space ultrasonic wave cloud fog generator for generate even meticulous cloud in every independent space.
The utility model provides in the cloud and mist hypergravity VOC processing system that high energy UV disinfected, the fan of airing exhaust with centrifugal filter's quantity is the same, the fan of airing exhaust is installed one-to-one centrifugal filter's rear for the equilibrium passes through hypergravity centrifugal device's wind-force.
The utility model provides in the cloud and mist hypergravity VOC processing system that high energy UV disinfected, the linear velocity when centrifugal filter's meticulous filter core runner rotated is 1 kilometer/second-1.2 kilometers/second.
The utility model provides in the cloud and mist hypergravity VOC processing system that high energy UV disinfected, the cloud and mist hypergravity VOC processing system that high energy UV disinfected still includes: a wastewater reclamation apparatus for reclaiming wastewater located below the primary and secondary strainer plates.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model discloses an adopt and spray filter equipment and spray the water droplet at its inner chamber and form the vaporific water droplet of water, make solid pollution granule, chemical molecule etc. in water mist form water droplet and the waste gas preliminary mix and adsorb, the rethread uses elementary water filtering plate to make waste water condense and instil into the below on it, forms preliminary purification through collecting waste water.
The utility model discloses an adopt cloud and mist filter equipment to form meticulous cloud and mist in the inner chamber, when the linear velocity of its meticulous filter core runner can reach 1 kilometer/second-1.2 kilometers/second, when waste gas passes meticulous filter core runner, the small particle pollutant in the waste gas and volatile organic compound gas molecule are adsorbed and are mixed by meticulous cloud and mist, and the size range of the particulate matter of being collected begins from 0.01 grade of granule. The primary purification is formed by collecting the waste water while making the cloud water drop condense thereon and drop below by using a fine filter core runner.
The utility model discloses an adopt hypergravity centrifugal device to produce the centrifugal force that surpasss more than 2G, the cloud and mist water droplet that will see through secondary water strainer plate gets rid of to the filter cloth around, and the filter cloth adsorbs adopts cloud and mist water droplet, discharges from the air outlet through the absorptive pure air of filter cloth.
The above technical means are adopted in the utility model, solved the technical problem that is difficult to fully adsorb particulate pollutant and VOC in the waste gas among the prior art, can reach the degree of pure air after handling, and adopt water as purifying material, have that use cost is low, adsorb advantages such as purify fully.
Drawings
Fig. 1 is a schematic structural diagram of the high-energy UV sterilizing cloud-mist supergravity VOC treatment system of the present invention.
FIG. 2 is a schematic view showing the connection between the shower filtration apparatus and the waste water recovering apparatus in the embodiment.
FIG. 3 is a schematic diagram of a super-gravity centrifuge.
Fig. 4 is a sectional view showing the structure of the centrifugal device and the exhaust fan according to the present embodiment.
In the drawings 1-4, 1-box, 11-air inlet, 12-air outlet, 2-spray filter device, 21-water tank module, 22-water pump, 23-nozzle, 3-primary water filter plate, 4-cloud filter device, 41-separation frame, 5-secondary water filter plate, 6-super gravity centrifugal device, 61-centrifugal filter, 62-filter cloth, 7-exhaust fan, 8-waste water recovery device, and 9-photolysis device.
Detailed Description
The high energy UV germicidal cloud hypergravity VOC treatment system as proposed by the present invention will now be described in more detail with reference to the schematic drawings, in which preferred embodiments of the invention are shown, it being understood that one skilled in the art could modify the invention described herein while still achieving the beneficial effects of the invention. Accordingly, the following description should be construed as broadly as possible to those skilled in the art and not as limiting the invention.
Fig. 1 shows a schematic diagram of a high energy UV germicidal cloud hypergravity VOC treatment system. The utility model discloses cloud hypergravity VOC processing system that high energy UV disinfected includes: the device comprises a box body 1, a spraying and filtering device 2, a primary water filtering plate 3, a cloud and mist filtering device 4, a secondary water filtering plate 5, a super-gravity centrifugal device 6, an exhaust fan 7, a wastewater recovery device 8 and a photolysis device 9. In the embodiment of the present invention, the spray filter 2 and the mist filter 4 preferably use water as a treatment medium, including tap water, purified water, sterile water, and other liquids using water as a main carrier. The adsorption mixture in the following examples of the present invention is commonly used tap water.
The box body 1 is provided with an air inlet 11 for sucking waste gas to be purified and an air outlet 12 for discharging purified gas. The exhaust fan 7 is located behind the supergravity centrifugal device 6, and is used for forming a unidirectional air flow between the air inlet 11 and the air outlet 12.
The spraying filter device 2 is positioned behind the air inlet 11, and a cavity inside the spraying filter device 2 is communicated with the air inlet 11 through a pipeline. The spray nozzles 23 provided in the shower filter device 2 form water mist-like water droplets by water pressure for preliminary mixing of particulate pollutants in the exhaust gas. More specifically, the spray filter assembly 2 includes at least one tank module 21, at least one water pump 22, and at least one spray nozzle 23. The spray nozzles 23 are distributed above the inner cavity of the spray filter device 2, and the spray nozzles 23 are sequentially connected with the water pump 22 and the water tank module 21 through pipelines. The water pump 22 pumps water for spraying from the inside of the water tank module 21 and generates high-intensity water pressure to form water mist-like water droplets through the nozzles 23 to adsorb pollutants in the exhaust gas. The pollutants include not only solid pollution particles, but also odor gas molecules and volatile organic compound gas molecules in the adsorbed exhaust gas.
The primary water filter plate 3 is positioned behind the spraying and filtering device 2, and the primary water filter plate 3 consists of a plurality of obliquely arranged water retaining sheets. The water retaining sheet condenses the water mist water drops, can collect most large granule waste water in the waste gas, and the one-way air current of tiny particle waste water and waste gas year in the water mist gets into cloud filter equipment 4 and works as well.
The cloud and mist filtering device 4 is positioned behind the primary filtering plate, and a cavity inside the cloud and mist filtering device 4 generates fine cloud and mist through an ultrasonic cloud and mist generator and is used for adsorbing peculiar smell and volatile gas molecules in the waste gas. More specifically, a partition frame 41 is further arranged in an inner cavity of the cloud and mist filtering device 4, the partition frame 41 partitions a plurality of independent spaces in the inner cavity, and an ultrasonic cloud and mist generator is arranged in each independent space and used for generating uniform fine cloud and mist in each independent space.
The secondary water filtering plate 5 is positioned behind the cloud and mist filtering device 4, and reticular water filtering holes are distributed on the secondary water filtering plate 5. The secondary water filtering plate 5 is a filter device with filtering holes distributed on the surface, such as a filter screen, an aluminum plate or a filter element. The aperture and the number of the filter holes of the filter element can influence the wind resistance and the filtering efficiency inside the air purifier, so that the aperture and the number of the filter holes of the filter element can be adjusted according to the actual use requirement.
The hypergravity centrifugal device 6 is positioned behind the secondary water filtering plate 5, at least one centrifugal filter 61 is arranged in the hypergravity centrifugal device 6, and filter cloth 62 is arranged on the periphery of the centrifugal filter 61. The wastewater passing through the secondary water filter 5 flows into the centrifugal filter 61 by wind power, and the wastewater is thrown into the filter cloth 62 by the supergravity centrifugal force generated by the high-speed rotation of the centrifugal filter 61 and collected. The linear speed of the fine filter element rotating wheel of the centrifugal filter 61 is 1-1.2 km/s when rotating, and the rotating speed is 1000-3000 r/min, so that the centrifugal force of more than 2G is generated, and most of wastewater is thrown to the surrounding filter cloth 62 by the centrifugal force. Wherein, the filter cloth 62 can be dismantled and replaced, can open the case and replace after having adsorbed the abundant waste water.
The exhaust fan 7 is located behind the supergravity centrifugal device 6, and is used for forming a unidirectional airflow between the air inlet 11 and the air outlet 12, and the pure air after the waste water is collected by the filter cloth 62 is discharged from the air outlet 12. More preferably, the number of the exhaust fans 7 is the same as that of the centrifugal filters 61, and the exhaust fans 7 are installed in one-to-one correspondence to the rear of the centrifugal filters 61 for equalizing the wind force passing through the supergravity centrifugal device 6.
The wastewater recovery device 8 for recovering wastewater is located below the primary water filter plate 3 and the secondary water filter plate 5, and the wastewater recovery device 8 is used for recovering wastewater dripped from the primary water filter plate 3 and the secondary water filter plate 5 from a bottom mobile phone. More preferably, the wastewater recovery device 8 is connected to the water tank module 21 through a pipeline, and the wastewater in the wastewater recovery device 8 can be sent to the water tank module 21 for recycling. More preferably, an acid-base concentration monitor is arranged in the water tank module 21, and the water tank module 21 can be integrally taken out and replaced until the concentration of pollutants adsorbed by the wastewater collected in the water tank module 21 reaches the preset value.
By carrying out the above examples, it was experimentally demonstrated that:
the utility model discloses an adopt and spray filter equipment and spray the water droplet at its inner chamber and form the vaporific water droplet of water, make solid pollution granule, chemical molecule etc. in water mist form water droplet and the waste gas preliminary mix and adsorb, the rethread uses elementary water filtering plate to make waste water condense and instil into the below on it, forms preliminary purification through collecting waste water.
The utility model discloses an adopt cloud and mist filter equipment to form meticulous cloud and mist in the inner chamber, when the linear velocity of its meticulous filter core runner can reach 1 kilometer/second-1.2 kilometers/second, when waste gas passes meticulous filter core runner, the small particle pollutant in the waste gas and volatile organic compound gas molecule are adsorbed and are mixed by meticulous cloud and mist, and the size range of the particulate matter of being collected begins from 0.01 grade of granule. The primary purification is formed by collecting the waste water while making the cloud water drop condense thereon and drop below by using a fine filter core runner.
The utility model discloses an adopt hypergravity centrifugal device to produce the centrifugal force that surpasss more than 2G, the cloud and mist water droplet that will see through secondary water strainer plate gets rid of to the filter cloth around, and the filter cloth adsorbs adopts cloud and mist water droplet, discharges from the air outlet through the absorptive pure air of filter cloth.
The utility model adopts the above technical means, solved the technical problem that is difficult to fully adsorb particle pollutant and VOC in the waste gas among the prior art, can reach the degree of pure air after handling, the utility model discloses the adsorption mixture who adopts mainly with materials such as running water, distilled water, compare in current high density filter core, its use cost is extremely low has use cost low, adsorbs and purifies advantage such as abundant.
The above description is only for the preferred embodiment of the present invention, and does not limit the present invention. Any technical personnel who belongs to the technical field, in the scope that does not deviate from the technical scheme of the utility model, to the technical scheme and the technical content that the utility model discloses expose do the change such as the equivalent replacement of any form or modification, all belong to the content that does not break away from the technical scheme of the utility model, still belong to within the scope of protection of the utility model.
Claims (7)
1. A high energy UV germicidal cloud hypergravity VOC processing system, comprising:
the device comprises a box body (1), wherein the box body (1) is provided with an air inlet (11) for sucking waste gas to be purified and an air outlet (12) for discharging purified pure gas;
the spraying and filtering device (2) is positioned behind the air inlet (11), and a cavity inside the spraying and filtering device (2) is communicated with the air inlet (11) through a pipeline; a nozzle (23) arranged in the spray filtering device (2) forms water mist-shaped water drops through water pressure, and the water mist-shaped water drops are used for preliminarily mixing particle pollutants in the waste gas;
the primary water filtering plate (3) is positioned behind the spraying and filtering device (2), and the primary water filtering plate (3) consists of a plurality of obliquely arranged water retaining sheets;
the cloud and mist filtering device (4) is positioned behind the primary water filtering plate, and fine cloud and mist is generated in a cavity inside the cloud and mist filtering device (4) through an ultrasonic cloud and mist generator and is used for adsorbing peculiar smell and volatile gas molecules in the waste gas;
the secondary water filtering plate (5) is positioned behind the cloud and mist filtering device (4), and mesh water filtering holes are distributed on the secondary water filtering plate (5);
the super-gravity centrifugal device (6) is positioned behind the secondary water filtering plate (5), at least one centrifugal filter (61) is arranged in the super-gravity centrifugal device (6), and filter cloth (62) is arranged on the periphery of the centrifugal filter (61); the wastewater penetrating through the secondary water filtering plate (5) flows into the centrifugal filter (61) by virtue of wind power, and the wastewater is thrown into the filter cloth (62) by virtue of the supergravity centrifugal force generated by the high-speed rotation of the centrifugal filter (61) for collection;
the exhaust fan (7) is positioned behind the hypergravity centrifugal device (6) and is used for forming unidirectional air flow between the air inlet (11) and the air outlet (12); and
photolysis device (9), it is located exhaust fan (7) with between air outlet (12), be equipped with ultraviolet lamp in photolysis device's the cavity and shine and kill the bacterium to the pure gas after the cloud and mist is collected, and the pure air after disinfecting is discharged from air outlet (12).
2. A high energy UV germicidal cloud hypergravity VOC treatment system as claimed in claim 1 wherein the spray filtration device (2) comprises at least one water tank module (21), at least one water pump (22) and at least one spray nozzle (23); the spray nozzles (23) are distributed above the inner cavity of the spray filtering device (2), and the spray nozzles (23) are sequentially connected with a water pump (22) and a water tank module (21) through pipelines; the water pump (22) pumps water for spraying from the water tank module (21) and generates high-intensity water pressure to form water mist-shaped water drops through the nozzle (23).
3. The high energy UV germicidal cloud hypergravity VOC treatment system as claimed in claim 2, characterized in that an acid-base concentration monitor is provided inside said water tank module (21).
4. A high-energy UV-germicidal cloud hypergravity VOC treatment system according to claim 1 characterized in that a separation frame (41) is further arranged in the inner cavity of the cloud filtering device (4), the separation frame (41) divides a plurality of independent spaces in the inner cavity, the ultrasonic cloud generator is arranged in each independent space for generating uniform fine cloud in each independent space.
5. The high-energy UV-sterilized cloud-mist hypergravity VOC processing system according to claim 1, characterized in that the number of said exhaust fans (7) is the same as the number of said centrifugal filters (61), said exhaust fans (7) being installed one-to-one behind said centrifugal filters (61) for equalizing the wind force passing through said hypergravity centrifugal device (6).
6. The high energy UV germicidal cloud high gravity VOC processing system as claimed in claim 1 wherein the fine filter element wheel of said centrifugal filter (61) rotates at a linear velocity of 1-1.2 km/s.
7. The high energy UV germicidal cloud hypergravity VOC treatment system as claimed in any of claims 1-6 further comprising: a waste water recovery device (8) for recovering waste water located below the primary and secondary strainer plates (3, 5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920112731.3U CN210171179U (en) | 2019-01-23 | 2019-01-23 | Cloud and mist supergravity VOC processing system with high-energy UV sterilization function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920112731.3U CN210171179U (en) | 2019-01-23 | 2019-01-23 | Cloud and mist supergravity VOC processing system with high-energy UV sterilization function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210171179U true CN210171179U (en) | 2020-03-24 |
Family
ID=69828869
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920112731.3U Expired - Fee Related CN210171179U (en) | 2019-01-23 | 2019-01-23 | Cloud and mist supergravity VOC processing system with high-energy UV sterilization function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210171179U (en) |
-
2019
- 2019-01-23 CN CN201920112731.3U patent/CN210171179U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208436600U (en) | A kind of bituminous mixing plant exhaust treatment system | |
| CN105311931B (en) | Industrial VOCs exhaust gas decomposing, purifying processing method and equipment | |
| CN110508113B (en) | System and process for treating organic waste gas by micro-nano oxygen bubbles in cooperation with iron ions | |
| CN207413050U (en) | A kind of paint exhaust treatment device | |
| CN109876585B (en) | Traditional chinese medicine plaster production exhaust gas treatment system | |
| CN107362647A (en) | A kind of paint exhaust treatment device and method | |
| CN104128059B (en) | Percussion flow gas purge system | |
| CN104998511B (en) | Cremator tail gas clean-up environment-friendly disposal system | |
| CN110207286B (en) | Novel haze air integrated purification system | |
| CN207641271U (en) | Vertical exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
| CN110280117B (en) | Centrifugal oxidation method and micro-nano bubble VOCs (volatile organic chemicals) processing system | |
| CN202122901U (en) | Tableware-kitchen oil mist and oily fume purifier | |
| CN205164386U (en) | Cremator tail -gas clean -up environmental protection processing system | |
| CN205965456U (en) | Organic waste gas integrated treating equipment | |
| CN213050101U (en) | Waste gas treatment system suitable for coal chemical industry | |
| CN203954985U (en) | Percussion flow gas purge system | |
| CN210171179U (en) | Cloud and mist supergravity VOC processing system with high-energy UV sterilization function | |
| CN210171180U (en) | Cloud and mist supergravity VOC treatment system with high-energy high-temperature UV sterilization function | |
| CN216825629U (en) | VOC exhaust treatment device | |
| CN109529577A (en) | A kind of hypergravity cloud and mist anion VOC processing system of high temperature sterilization | |
| CN108043216A (en) | A kind of paint exhaust treatment device and method | |
| CN210171210U (en) | Photocatalyst cloud and mist hypergravity VOC processing system | |
| CN215539485U (en) | Injection molding waste gas treatment device | |
| CN210171154U (en) | Cloud and mist supergravity VOC treatment system | |
| CN109529557A (en) | A kind of cloud and mist hypergravity VOC processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| 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: 20200324 |