CN112957889A - VOCs purifier - Google Patents
VOCs purifier Download PDFInfo
- Publication number
- CN112957889A CN112957889A CN202110149307.8A CN202110149307A CN112957889A CN 112957889 A CN112957889 A CN 112957889A CN 202110149307 A CN202110149307 A CN 202110149307A CN 112957889 A CN112957889 A CN 112957889A
- Authority
- CN
- China
- Prior art keywords
- tower body
- vocs
- bioreactor
- tower
- liquid
- 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.)
- Pending
Links
- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 40
- 238000010521 absorption reaction Methods 0.000 claims abstract description 25
- 238000000746 purification Methods 0.000 claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000005507 spraying Methods 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims description 38
- 239000007921 spray Substances 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 28
- 238000000889 atomisation Methods 0.000 description 10
- 239000004094 surface-active agent Substances 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 8
- 239000002912 waste gas Substances 0.000 description 7
- 230000015556 catabolic process Effects 0.000 description 6
- 238000006731 degradation reaction Methods 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 239000003344 environmental pollutant Substances 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- 230000002209 hydrophobic effect Effects 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 238000005842 biochemical reaction Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 208000005623 Carcinogenesis Diseases 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000036952 cancer formation Effects 0.000 description 1
- 231100000504 carcinogenesis Toxicity 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 210000002216 heart Anatomy 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002703 mutagenesis Methods 0.000 description 1
- 231100000350 mutagenesis Toxicity 0.000 description 1
- 210000000653 nervous system Anatomy 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- GPRLSGONYQIRFK-MNYXATJNSA-N triton Chemical compound [3H+] GPRLSGONYQIRFK-MNYXATJNSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/38—Removing components of undefined structure
- B01D53/44—Organic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1487—Removing organic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
- B01D53/185—Liquid distributors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/95—Specific microorganisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
- B01D2252/20—Organic absorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a VOCs purification device, which comprises a bioreactor, an absorption tower, an ultrasonic atomizer and a spraying device, wherein the bioreactor is arranged on the top of the absorption tower; the absorption tower comprises a tower body, an exhaust pipe arranged at the upper part of the tower body and an air inlet pipe arranged at the lower part of the tower body, wherein the bottom of the tower body is communicated with the bioreactor; the spraying device comprises a water pump arranged in the bioreactor and a spraying head arranged at the top of the tower body and communicated with the water pump; the ultrasonic atomizer is connected with the lower part of the tower body. The device has the advantages of good treatment effect, high purification efficiency, safety and low energy consumption.
Description
Technical Field
The invention belongs to the technical field of purification equipment, and particularly relates to a VOCs purification device.
Background
In recent years, the amount of industrial exhaust gas emissions has increased due to the economic development and the accelerated progress of industrialization, in which VOCs are produced into O3And PM2.5The precursor is easy to cause harm to human organs such as heart, lung, liver and nervous system of human body, even cause adverse effects such as carcinogenesis and mutagenesis, and is concerned about due to great harm to human health and environment. The conventional VOCs waste gas treatment technology comprises the traditional physical, chemical and biological technologies, which are mature in research, and part of the technology is verified by engineering and enters marketized operation, so that the technology can be basically applied to purification of industrial production waste gas. However, as our country pay more and more attention to environmental protection, a single biological treatment technology cannot meet the environmental protection requirement, and most of the treated objects are low-concentration substances and easily biodegradable VOCs, and the problem to be solved in the practical engineering is still urgent for the treatment of high-concentration and difficultly degradable VOCs. Meanwhile, the mass transfer of gas and liquid, working conditions and environment, biochemical degradation and other influencing factors are involved, the practical application is not deep enough, and a plurality of aspects still need deep research.
Under the current serious atmospheric pollution condition, a more efficient treatment way for VOCs needs to be explored.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention provides the VOCs purification device which has the advantages of good treatment effect, high purification efficiency, safety and low energy consumption.
The technical scheme adopted by the invention is as follows: it comprises a bioreactor, an absorption tower, an ultrasonic atomizer and a spraying device;
the absorption tower comprises a tower body, an exhaust pipe arranged at the upper part of the tower body and an air inlet pipe arranged at the lower part of the tower body, wherein the bottom of the tower body is communicated with the bioreactor;
the spraying device comprises a water pump arranged in the bioreactor and a spraying head arranged at the top of the tower body and communicated with the water pump;
the ultrasonic atomizer is connected with the lower part of the tower body.
Furthermore, a grid net and a plurality of packing layers are arranged in the tower body of the absorption tower, and the packing layers are positioned below the grid net.
Further, the lower part of the tower body is connected with an ultrasonic atomizer through a spraying pipeline.
Further, the bottom of the tower body is connected with the bioreactor through a liquid discharge pipe.
Further, a valve is arranged on the liquid discharge pipe.
Further, a gas flowmeter is arranged on the gas inlet pipe.
Further, the water pump is connected with the spray header through a liquid pipeline.
Further, a liquid flowmeter is arranged on the liquid pipeline.
The invention has the beneficial effects that:
the waste gas to be treated is introduced from the air inlet pipe of the tower body, VOCs gas is collected by fog drops generated by the ultrasonic atomizer, and then flows from bottom to top in the tower body. And then a water pump is started, the washing liquid is sprayed from top to bottom in the tower body, the gas at the bottom ascends, the liquid at the top descends, and the gas and the liquid are in countercurrent contact to carry out secondary absorption on the VOCs. And discharging the treated VOCs waste gas through an exhaust pipe.
The invention sets ultrasonic atomization surfactant for strengthening absorption, and gas-liquid contact is formed by gaseous pollutants and fog drops generated by ultrasonic waves, so that the absorption of VOCs gas is further strengthened. The invention combines the bioreactor, the ultrasonic atomizer 3 and the tower body 2, when in use, the biochemical reaction is carried out in the absorption tower in advance, which greatly strengthens the absorption and degradation effect and improves the treatment capacity of the device.
The invention integrates the ultrasonic atomization surfactant and the biological washing multi-stage purification principle to purify pollutants in a synergistic manner, not only can overcome the problems of high treatment difficulty and unstable operation of high-concentration VOCs (particularly hydrophobic VOCs), but also can reduce mass transfer resistance, increase the contact area between gas and liquid, reduce degradation time, avoid secondary pollution, enhance treatment effect and improve purification efficiency.
The invention combines the bioreactor, the ultrasonic atomizer and the tower body, greatly enhances the absorption and degradation effect and improves the processing capacity of the device.
Drawings
FIG. 1 is a schematic front view of the present invention;
FIG. 2 is a schematic side view of the present invention;
FIG. 3 is an isometric view of the present invention.
In the figure: 1. the system comprises a bioreactor, 2. a tower body, 3. an ultrasonic atomizer, 4. a grid net, 5. an exhaust pipe, 6. an air inlet pipe, 7. a water pump, 8. a spray header, 9. a valve, 10. a liquid pipeline, 11. a liquid flowmeter, 12. a gas flowmeter, 13. a spray pipeline, 14. a packing layer and 15. a liquid discharge pipe.
Detailed Description
In order to clearly understand the technical scheme of the invention, the invention is further explained with reference to the attached drawings.
As shown in figure 1, the invention provides a VOCs purification device, in particular to a device for biologically purifying VOCs by using ultrasonic atomization surfactant in cooperation, which comprises a bioreactor 1, an absorption tower, an ultrasonic atomizer 3 and a spraying device.
The absorption tower includes tower body 2, sets up the blast pipe 5 on 2 upper portions of tower body sets up at the intake pipe 6 of 2 lower parts of tower body, the bottom and the bioreactor 1 intercommunication of tower body 2, liquid discharge pipe 15 is passed through to the bottom of tower body 2 and bioreactor 1 is connected.
Spray set is including setting up water pump 7 in bioreactor 1 with set up at 2 tops of tower body and with the shower head 8 of water pump 7 intercommunication, shower head 8 is used for spraying washing liquid to 2 inside from the top down of tower body, the washing liquid is the liquid of pump 7 extraction from bioreactor 1.
The ultrasonic atomizer 3 is connected with the lower part of the tower body 2. The lower part of the tower body 2 is connected with an ultrasonic atomizer 3 through a spraying pipeline 13. The particle size of the fog drops generated by the ultrasonic atomization of the ultrasonic atomizer 3 is below 10um, the fog drops are small and uniform, so that the specific surface area between gas and liquid is increased, the gas can rapidly react with the fog drops, and meanwhile, the atomized fog drops generated by the ultrasonic atomization have fine particle size and higher quality, and the removal rate of the gas is improved.
A grid net 4 and a plurality of packing layers 14 are arranged in the tower body 2 of the absorption tower, and the packing layers 14 are located below the grid net 4.
In this embodiment, the number of the filler layers 14 is three, the filler is polypropylene, and the filler has a polyhedral hollow sphere structure with a diameter of 25 mm.
The liquid discharge pipe 15 is provided with a valve 9.
The gas inlet pipe 6 is provided with a gas flowmeter 12.
The water pump 7 is connected with the spray header 8 through a liquid pipeline 10.
The liquid pipeline 10 is provided with a liquid flow meter 11.
In the embodiment, the internal structure of the ultrasonic atomizer 3 comprises a humidifying tank and an ultrasonic humidifying high-frequency oscillator, wherein the inner diameter of the humidifying tank is 270 mm, the height of the humidifying tank is 280 mm, the height of the ultrasonic humidifying high-frequency oscillator is 50 mm, the height of the liquid level in the humidifying tank is 35 mm, the inlet gas temperature is 289.6K, the inlet relative humidity is 43%, the flow rate is 15.71L/min, the pressure of the humidifying tank is 196 kPa, 251 transducers are provided, and the power is 35W; the transducer was tested to humidify 450 mL/h at standard atmospheric pressure at 293K and 50% relative humidity.
Before the invention is used, the bioreactor 1 is filled with cultured and domesticated activated sludge, the washing liquid extracted from the bioreactor 1 and used for spraying is the activated sludge and the supernatant liquid thereof, the ultrasonic atomizer 3 is added with a surfactant, the surfactant in the embodiment is one of tween, triton and saponin, and the concentration of the surfactant is controlled to be 1-2 CMC. When the device is used, firstly, the prepared surfactant solution is added into the ultrasonic atomizer 3, the ultrasonic atomizer 3 is opened, fog drops generated by the ultrasonic atomizer 3 flow into the tower body 2 through the spray pipeline 13, then VOCs waste gas to be treated is introduced from the air inlet pipe 6 of the tower body 2, the fog drops generated by the ultrasonic atomizer 3 capture the VOCs gas, and the VOCs gas flows from bottom to top in the tower body 2. Then the water pump 7 is opened, the cleaning solution in the bioreactor 1 is sprayed out from the spray header 8 under the pumping action of the water pump 7, and the cleaning solution is sprayed from top to bottom in the tower body 2 because the spray header 8 is arranged at the top of the tower body 2, the gas at the bottom goes upwards, the liquid at the top goes downwards, and the gas and the liquid are in countercurrent contact to carry out secondary absorption on the VOCs. The process of the air flow from bottom to top passes through the three-layer packing layer, and the biological cleaning solution and the atomized liquid drops flow into the bioreactor 1 through the liquid discharge pipe 15. And the treated VOCs waste gas is discharged from an exhaust pipe 5. In this embodiment, the exhaust gas of the exhaust pipe 5 is detected, and the detection result shows that the removal rate of the VOCs exhaust gas (taking toluene as an example) reaches 99% or more.
The ultrasonic atomization device, namely the ultrasonic atomizer 3, performs enhanced absorption, and gas-liquid contact is formed by gaseous pollutants and fog drops generated by ultrasonic waves, so that VOCs gas absorption is further enhanced. The particle size of the fog drops generated by ultrasonic atomization is below 10um, and the fog drops are small and uniform, so that the specific surface area between gas and liquid is increased, the gas can quickly react with the fog drops, and meanwhile, the atomized fog drops generated by the ultrasonic atomization have fine particle size and higher quality, and the removal rate of the gas is improved. And by adding the surfactant in the ultrasonic device, the dissolution of hydrophobic substances in VOCs is promoted, the gas retention time and the contact area are increased, and the biochemical reaction is carried out in the absorption tower in advance. This greatly enhances the absorption and degradation effect and improves the processing capacity of the device.
The invention integrates the ultrasonic atomization surfactant and the biological washing multi-stage purification principle to purify pollutants in a synergistic manner, can overcome the problems of high treatment difficulty, unstable operation and the like of high-concentration VOCs (particularly hydrophobic VOCs) on the basis of continuing the advantages of the traditional biological treatment technology, can reduce mass transfer resistance, increase the contact area between gas and liquid, reduce degradation time, has no secondary pollution, enhances the treatment effect, improves the purification efficiency and the like, and provides the device for purifying the biological purification waste gas of the high-concentration hydrophobic VOCs on the basis of high efficiency, safety and low energy consumption.
The invention improves the absorption and purification efficiency and the actual application range, adds the ultrasonic atomization technology on the basis of the bioreactor, and utilizes ultrasonic waves to atomize the surfactant into liquid drops to form cold mist, thereby realizing more effective reinforced absorption of gaseous pollutants and further improving the purification efficiency. Under the condition of serious atmospheric pollution at present, the device provides a new treatment way in the aspect of treating VOCs.
The method can meet the experimental requirements of biological purification of the VOCs developed by scientific research institutions, is used for researching the treatment potential and mechanism of the biological purification VOCs technology, and can provide a method for atmospheric pollution treatment for environmental protection departments.
The above description is only a preferred embodiment of the present invention, and all equivalent changes or modifications of the structure, characteristics and principles described in the present invention are included in the scope of the present invention.
Claims (8)
1. A VOCs purification device is characterized by comprising a bioreactor (1), an absorption tower, an ultrasonic atomizer (3) and a spraying device;
the absorption tower comprises a tower body (2), an exhaust pipe (5) arranged at the upper part of the tower body (2), and an air inlet pipe (6) arranged at the lower part of the tower body (2), wherein the bottom of the tower body (2) is communicated with the bioreactor (1);
the spraying device comprises a water pump (7) arranged in the bioreactor (1) and a spraying head (8) arranged at the top of the tower body (2) and communicated with the water pump (7);
the ultrasonic atomizer (3) is connected with the lower part of the tower body (2).
2. A VOCs purification apparatus as claimed in claim 1, wherein a grid mesh (4) and a plurality of packing layers (14) are disposed in the tower body (2) of the absorption tower, and the packing layers (14) are disposed below the grid mesh (4).
3. A purification apparatus for VOCs as claimed in claim 1, wherein the lower part of the tower (2) is connected to the ultrasonic atomizer (3) via a spray pipe (13).
4. A purification apparatus for VOCs as claimed in claim 1, wherein the bottom of said tower (2) is connected to the bioreactor (1) via a liquid discharge pipe (15).
5. A purification apparatus for VOCs according to claim 4, wherein the liquid discharge pipe (15) is provided with a valve (9).
6. A purification apparatus for VOCs as claimed in claim 1, wherein said inlet pipe (6) is provided with a gas flow meter (12).
7. A purification apparatus for VOCs as claimed in claim 1, wherein said water pump (7) and said shower head (8) are connected by a fluid line (10).
8. A purification apparatus for VOCs according to claim 7, wherein a liquid flow meter (11) is arranged in the liquid conduit (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110149307.8A CN112957889A (en) | 2021-02-03 | 2021-02-03 | VOCs purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110149307.8A CN112957889A (en) | 2021-02-03 | 2021-02-03 | VOCs purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112957889A true CN112957889A (en) | 2021-06-15 |
Family
ID=76274254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110149307.8A Pending CN112957889A (en) | 2021-02-03 | 2021-02-03 | VOCs purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112957889A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857198A (en) * | 1988-07-29 | 1989-08-15 | Zimpro/Passavant Inc. | Process for treatment of water containing volatile and toxic compounds |
| CN101708426A (en) * | 2009-12-04 | 2010-05-19 | 广东省微生物研究所 | Biologic filtration method and device for purifying industrial organic waste gas |
| CN206138979U (en) * | 2016-09-18 | 2017-05-03 | 广东智环创新环境科技有限公司 | Big amount of wind low concentration organic waste gas processing apparatus |
| CN110201504A (en) * | 2019-07-12 | 2019-09-06 | 厚德九天（湖北）环保科技集团有限公司 | Supersonic atomizer, desulfurizing tower and atomization sulfur removal technology |
| CN110237683A (en) * | 2019-05-27 | 2019-09-17 | 河北科技大学 | The novel reinforced absorption VOCs processing unit of one kind and its method |
| CN210814702U (en) * | 2019-07-25 | 2020-06-23 | 上海碧州环保能源科技有限公司 | Biological washing exhaust treatment device |
-
2021
- 2021-02-03 CN CN202110149307.8A patent/CN112957889A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4857198A (en) * | 1988-07-29 | 1989-08-15 | Zimpro/Passavant Inc. | Process for treatment of water containing volatile and toxic compounds |
| CN101708426A (en) * | 2009-12-04 | 2010-05-19 | 广东省微生物研究所 | Biologic filtration method and device for purifying industrial organic waste gas |
| CN206138979U (en) * | 2016-09-18 | 2017-05-03 | 广东智环创新环境科技有限公司 | Big amount of wind low concentration organic waste gas processing apparatus |
| CN110237683A (en) * | 2019-05-27 | 2019-09-17 | 河北科技大学 | The novel reinforced absorption VOCs processing unit of one kind and its method |
| CN110201504A (en) * | 2019-07-12 | 2019-09-06 | 厚德九天（湖北）环保科技集团有限公司 | Supersonic atomizer, desulfurizing tower and atomization sulfur removal technology |
| CN210814702U (en) * | 2019-07-25 | 2020-06-23 | 上海碧州环保能源科技有限公司 | Biological washing exhaust treatment device |
Non-Patent Citations (1)
| Title |
|---|
| 纪红兵编著: "《蓝天白云不是梦》", 中山大学出版社 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102241422B (en) | Circulating closed ammonia nitrogen stripping system | |
| CN202080917U (en) | Circulating closed-loop type ammonia nitrogen stripping system | |
| CN104338436B (en) | A kind of efficient processing high concentration is mixed the deodoration system of foul smell | |
| CN107261811B (en) | A filtration separator for handling contain mercury industrial waste gas | |
| CN210613307U (en) | Flue gas absorption system based on spiral sprays | |
| CN104606996B (en) | Adsorption filtration and atomizing purification device suitable for industrial exhaust gas treatment | |
| CN102161534A (en) | Device for processing dimethylamine exhaust gas and wastewater | |
| CN209791267U (en) | High-efficient bio-trickling-filtering deodorizing purifier | |
| CN110898620A (en) | Fountain exhaust gas purification device | |
| CN206950959U (en) | Odor gas purification system | |
| CN112957889A (en) | VOCs purifier | |
| CN201704096U (en) | Ultrasonic ammonia nitrogen blowing device | |
| CN106964246A (en) | A kind of flue gas processing device | |
| CN110606624A (en) | All-dimensional deodorization process and device for microorganism enhanced proliferation reactor | |
| CN202725010U (en) | Device for removing trace acidic gas in indoor air | |
| CN214051162U (en) | High-efficient processing apparatus of VOC exhaust-gas treatment | |
| CN112957888A (en) | VOCs purification method | |
| CN207708821U (en) | A kind of VOC gas processing unit | |
| CN201124074Y (en) | Industrial waste gas purifier | |
| CN205308115U (en) | Vertical scrubbing tower industrial waste gas administers purifier | |
| CN212549010U (en) | Low concentration organic waste gas treatment device | |
| CN205913986U (en) | Sewage treatment pond that contains waste gas treatment system | |
| CN2860596Y (en) | Dust purifier | |
| CN219964492U (en) | Polyurethane silicone oil production exhaust treatment device | |
| CN110465174A (en) | A kind of deodorizing device and deodorization process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210615 |
|
| RJ01 | Rejection of invention patent application after publication |