CN108014595A - A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology - Google Patents
A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology Download PDFInfo
- Publication number
- CN108014595A CN108014595A CN201711266285.3A CN201711266285A CN108014595A CN 108014595 A CN108014595 A CN 108014595A CN 201711266285 A CN201711266285 A CN 201711266285A CN 108014595 A CN108014595 A CN 108014595A
- Authority
- CN
- China
- Prior art keywords
- exhaust gas
- photooxidation
- module
- lamp group
- high energy
- 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
- 238000007539 photo-oxidation reaction Methods 0.000 title claims abstract description 66
- 239000007788 liquid Substances 0.000 title claims abstract description 46
- 238000005516 engineering process Methods 0.000 title claims abstract description 26
- 239000007789 gas Substances 0.000 claims abstract description 170
- 238000005336 cracking Methods 0.000 claims abstract description 39
- 238000000034 method Methods 0.000 claims abstract description 34
- 238000001514 detection method Methods 0.000 claims abstract description 21
- 230000005684 electric field Effects 0.000 claims abstract description 16
- 238000000746 purification Methods 0.000 claims abstract description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000003546 flue gas Substances 0.000 claims abstract description 13
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 59
- 238000012545 processing Methods 0.000 claims description 18
- 238000006555 catalytic reaction Methods 0.000 claims description 14
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 11
- 230000008569 process Effects 0.000 claims description 10
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 5
- 239000004615 ingredient Substances 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 10
- 239000012855 volatile organic compound Substances 0.000 abstract description 6
- 230000003647 oxidation Effects 0.000 description 13
- 238000007254 oxidation reaction Methods 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 229910001868 water Inorganic materials 0.000 description 9
- 238000013461 design Methods 0.000 description 8
- 230000004992 fission Effects 0.000 description 8
- 239000002912 waste gas Substances 0.000 description 8
- 239000003344 environmental pollutant Substances 0.000 description 7
- 230000006872 improvement Effects 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 238000006303 photolysis reaction Methods 0.000 description 6
- 239000007921 spray Substances 0.000 description 6
- 239000000356 contaminant Substances 0.000 description 5
- 230000001699 photocatalysis Effects 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- 150000003384 small molecules Chemical class 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- 238000005457 optimization Methods 0.000 description 3
- 238000007146 photocatalysis Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 244000286663 Ficus elastica Species 0.000 description 2
- 206010020843 Hyperthermia Diseases 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000012668 chain scission Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000036031 hyperthermia Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000005201 scrubbing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- -1 oxonium ion Chemical class 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000010057 rubber processing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 238000006557 surface reaction Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000010148 water-pollination Effects 0.000 description 1
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
- B01D53/007—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 irradiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
-
- 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
-
- 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
- B01D53/75—Multi-step processes
-
- 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
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Toxicology (AREA)
- Dispersion Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology, cavitation liquid exhaust gas scrubber is connected with oil gas purification electric field equipment by air hose, oil gas purifies electric field equipment and is connected with photooxidation cracking cabinet by air hose, exhaust gas concentration detection sensor is installed on photooxidation cracking cabinet inlet, high energy ultraviolet lamp group module is installed in photooxidation cracking cabinet by certain amount and spacing, single-chip computer control system is installed in Intelligent control cabinet, air-introduced machine is installed at photooxidation cracking cabinet air outlet and the air outlet of the suction type air-introduced machine accesses the dry method flue gas integrated treatment tank;Single-chip computer control system can control the combination open and close of lamp group module according to exhaust gas concentration detection sensor feedack.The energy-efficient operation of the achievable whole system of the present invention, extends the service life of lamp group module, improves VOCs treatment effect, secondary pollution problem caused by avoiding conventional wet technique, realizes ultra-clean discharge.
Description
Technical field
This patent is related to technical field of waste gas treatment, specifically a kind of intelligent tail gas photooxidation using cavitation liquid technology
Cracker.
Background technology
Atmosphere pollution is one of China's environmental problem most prominent at present.Wherein industrial waste gas is the important of atmosphere pollution
Source.Most intractable in industrial waste gas is exactly organic exhaust gas, mainly including various hydro carbons, alcohols, aldehydes, acids, ketone and
Amine etc..They are mainly derived from the exhaust gas discharged in oil and chemical industry production process, and feature is that quantity is larger, organic matter
Content fluctuation is big, it is flammable, have certain toxicity, some goes back foul smelling.The rubber relevant industries such as domestic rubber plant, reclaimed rubber factory exist
Also substantial amounts of organic exhaust gas can be produced in production process.These organic exhaust gas, can also be in addition to causing direct atmosphere pollution
The reaction generation secondary pollution of complexity is participated in air, becomes one of main source of PM2.5.So processing of organic exhaust gas
It is urgently to be resolved hurrily with purifying problem.
Mainly include for organic waste-gas purification processing means at present:Direct high-temperature combustion method, catalytic oxidation, ozone remove
Smelly method, active carbon adsorption, soda acid liquid spray process, biological odor removal method etc..There are equipment throwing to varying degrees for these methods
Money is high, operating cost is high, it is big to handle narrow-minded, job insecurity, occupied space, deodorization purification efficiency is not high, there are secondary dirt
The problems such as dye.Ultraviolet exhaust treatment system new at present has obtained more and more applications, after UV treatment
The strand of macromolecular organic exhaust gas, which is interrupted, becomes small molecule contaminants, then can be by exhaust gas by the processing of follow-up equipment
Discharge is reduced to a very low level.But these ultraviolet equipments also one problem of generally existing is exactly intelligentized control method water
It is flat very low, it is impossible to control the processing power of ultraviolet equipment in real time according to pollutant concentration so that cause the energy waste or
The problem of pollutant process is not up to standard.In addition locate after the exhaust gas after ultraviolet equipment is handled is in discharge because of conventional wet
The limitation of reason equipment (generally using scrubbing tower) can also pollute thing with secondary dirt caused by water mist of gas flowing discharge
Dye problem, the especially formation with PM2.5 have much relations.
In Chinese patent literature, CN103505990A is related to a kind of UV-VOC emission-control equipments, including babinet, described
Photodissociation oxidation fission chamber is equipped with babinet, the photodissociation oxidation fission chamber is connected by pipeline with waste gas inlet;Described
Excitation high-pressure installation is equipped with photodissociation oxidation fission chamber, organic exhaust gas is decomposed to fission;Control is additionally provided with the babinet
System, the control system include master controller, B/P EGR Back Pressure Transducer EGR, photoelectric sensor, realize the overall operation to the equipment
And security control.The present invention aoxidizes fission chamber by photodissociation effectively realizes the purified treatment of exhaust gas, and organic exhaust gas is abundant
Oxidation fission discharge, it is pollution-free;The filtering and separation of exhaust gas are realized by pretreatment section, for follow-up photodissociation oxidation fission processing system
The processing to exhaust gas of uniting creates conditions;The application of water circulation system doubles to extend the use of photodissociation oxidation fission device handling system
Service life.CN104667674B is related to technical field of air purification processing, more particularly, to coating waste gas treatment process and its device,
Including paint mist treatment, the dust particles in exhaust gas are handled by water spray;Photocatalysis treatment, makes organic or inorganic high score in exhaust gas
Sub- malodorous compound molecular chain degradation is transformed into low molecular compound, is thus modified as hydrophily gas;And at gas-liquid mixed
Reason, removes the peculiar smell in removing exhaust gas, exhaust-gas treatment is more thorough.Its device has a paint mist treatment tower, a photocatalysis treatment device and one
Gas-liquid mixed processor, the coaxial word of three are connected successively, form sealing passage, according to above-mentioned process coating waste gas, knot
Structure is simple, easily makes, and clean-up effect is good, is applicable in industrial waste gas processing.CN105964120A discloses a kind of exhaust-gas treatment system
System, including alkali spray column, plant liquid spraying tower, photocatalytic oxidation device, wind turbine and chimney, the alkali spray column, vegetation water spray
Leaching tower, photocatalytic oxidation device, wind turbine and chimney are sequentially connected.The present invention is compared with conventional art, design science, handles exhaust gas
Effect is obvious, soda acid is handled, biochemical treatment and Treatment by Photocatalysis Oxidation combine in a system, can fully handle mixed
Mould assembly exhaust gas, discharge after being allowed to up to standard.Entitled " combined plastic granulation waste gas cleaning system ", Publication No.
The utility model patent of CN205550040U discloses a kind of technical solution, including spray scrubber and whirlwind aqueous vapor separation dress
Put, waste gas treatment equipment, waste gas treatment equipment includes activated carbon adsorption storehouse, UV photooxidations catalysis storehouse and low-temperature plasma equipment.On
The technology of stating can effectively remove smog and debirs in removing exhaust gas.But above-mentioned technical proposal intelligentized control method level is very low, no
The processing power of ultraviolet equipment can be controlled in real time according to pollutant concentration, the waste or pollutant process for causing the energy do not reach
Target problem.In addition the exhaust gas after ultraviolet equipment is handled (is generally adopted in discharge because of conventional wet equipment for after-treatment
With scrubbing tower) limitation can also pollute thing with water mist of gas flowing discharge caused by secondary pollution problem.
The content of the invention
The present invention provides a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology.In order to overcome the prior art
In deficiency, the object of the present invention is to provide a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology, can be used for
The cracking such as waste rubber and waste plastic exhaust gas, rubber processing and the tail gas in reclaimed rubber process and food and drink in chemical plant
The vent gas treatment of industry.
The technical solution adopted in the present invention is as follows:
A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology, its major part include cavitation liquid exhaust gas
Wash mill, oil gas purification electric field equipment, exhaust gas concentration detection sensor, photooxidation cracking cabinet, dust-proof filter wet web, high energy ultraviolet
Lamp group module, ozone supply module, TiO2Catalysis net, single-chip computer control system, suction type air-introduced machine, dry method flue gas integrated treatment
Tank, ozone filter screen;The cavitation liquid exhaust gas scrubber is connected with oil gas purification electric field equipment by air hose, described
Oil gas purifies electric field equipment and is connected with photooxidation cracking cabinet by air hose, and the exhaust gas concentration detection sensor is installed on described
Photooxidation cracking cabinet inlet, the dust-proof filter wet web are installed in the slot of photooxidation cracking cabinet inlet, and the high energy is purple
Outside line lamp group module is installed in the photooxidation cracking cabinet by certain amount and spacing, and the ozone supply module presses certain amount
It is installed on spacing in the photooxidation cracking cabinet and is in the rear end of the high energy ultraviolet lamp group module, the TiO2Catalysis
Net is uniformly installed between each high energy ultraviolet lamp group module and between each ozone supply module, the microcontroller control
System is installed in the photooxidation cracking cabinet Intelligent control cabinet, and the air-introduced machine is installed at the photooxidation cracking cabinet air outlet simultaneously
And the air outlet of the air-introduced machine accesses the dry method flue gas integrated treatment tank, the ozone filter screen is installed on the dry method cigarette
In the exhaust outlet of gas integrated treatment tank;Postposition exhaust gas concentration detection sensor is installed after the ozone filter screen, last
Position before exhaust outlet is provided with three-way electromagnetic switch valve, and the tracheae of three-way electromagnetic switch valve connection is washed with cavitation liquid exhaust gas
The air inlet duct side for washing device is connected, as the gas concentration after handling does not reach the minimum exhaust gas concentration discharge of default
Standard, the single-chip computer control system record this gas component, and when vent gas treatment for carrying out same sample ingredient next time is intelligently controlled
Single-chip computer control system control high energy ultraviolet lamp group module and ozone supply module in cabinet processed, the shape of the fluorescent tube of every group of unlatching
Shape is arranged according to the upper level of corresponding concentration scale.
Compared to the prior art, the present invention is a kind of can be taken using the intelligent tail gas photooxidation cracker of cavitation liquid technology
Beneficial effect be:
1. the liquid cavitation of the cavitation liquid exhaust gas scrubber of autonomous Design can will be big in the exhaust gas of plant emissions
Molecular contaminants decompose under microcosmic localized hyperthermia's high pressure, and the exhaust gas for simultaneously flowing through the cavitation liquid exhaust gas scrubber can be cold
But, in favor of the processing to exhaust gas below.In combination with oil gas purify electric field equipment to the fluid dust in rubber plant's exhaust gas into
Row preliminary treatment, is conducive to improve below the efficiently treatment effeciency of photooxidation cracking cabinet.
2. using cavitation liquid exhaust gas scrubber, oil gas purification electric field equipment, there is rough dusting effect, be conducive to extend
High energy ultraviolet lamp group module, the service life of ozone supply module, improve VOCs treatment effect;Sent out by experimental study
Now the service life of lamp group module can be extended 33%, VOCs treatment effect promoting 28%.
3. using dust-proof filter wet web, there is further dedusting to filter wet effect, protection high energy ultraviolet lamp group module, ozone supply
To module, excessive moisture is avoided to cause the accidental discharge of energetic ion lamp module, it is suitable in efficient photooxidation cracking cabinet to ensure
Working environment;
4. cracking cabinet inlet by this intelligent and high-efficiency photooxidation using the control program of autonomous optimization design detects pollutant
The feedback signal of the sensor of concentration, control high energy ultraviolet lamp group module, the regular stacked switch of ozone supply module,
The quantity for opening lamp group module can be controlled as needed, achieveed the purpose that on the premise of VOCs treatment is up to standard energy saving;
5. high energy ultraviolet lamp group module, ozone supply module use modularized design, using 5 fluorescent tubes of a module simultaneously
The scheme of row, maintenance need to only take out corresponding module when replacing, not influence the work of other modules;
6. the gas mobilization dynamic of whole system is provided by suction type air-introduced machine, due to the presence of negative pressure, intelligent and high-efficiency light
Oxygen cracks cabinet or even the undressed organic exhaust gas of whole system and will not leak;
7. last processing step is done using dry method flue gas integrated treatment tank, can be to avoid secondary caused by conventional wet technique
Pollution problem, realizes ultra-clean discharge.
8. finally using ozone filter screen in package unit, can be by the unconsumed ozone reduction generated in whole system
Oxygen, ensure that the zero-emission of ozone.
Based on such scheme, the present invention is also made that following improvement:
The cavitation liquid exhaust gas scrubber is based on Hydrodynamic cavitation principle, empty compared to ultrasonic cavitation technology, waterpower
Change improves the luminous efficiency of cavitation, and good energy-conserving effect high to the capacity usage ratio of exhaust-gas treatment.
The lamp group module includes the equally distributed high energy ultraviolet lamp group module of array and ozone supply module, described smelly
Oxygen supply module is located at after high energy ultraviolet lamp group module.In this improvement project, first with high energy ultraviolet lamp group module pair
Organic exhaust gas macromolecular implements chain scission, further oxidation of the ozone supply module to the small molecule exhaust gas after chain rupture.
Lamp group module is arranged by certain amount and spacing, and then realizes the efficient process to exhaust gas.
The single-chip computer control system is turned on and off high energy ultraviolet lamp group module and ozone supply according to exhaust gas concentration
Corresponding fluorescent tube in module, the fluorescent tube layout that high energy ultraviolet lamp group module and ozone supply the module fluorescent tube is opened follow sky
Between distributing homogeneity principle.The feedback letter for detecting the sensor of exhaust gas concentration in cabinet inlet is cracked by photooxidation in this improvement project
Number, it is regular using control programme-control high energy ultraviolet lamp group module, the ozone supply module of the autonomous optimization design of microcontroller
Combination open and close.The principle that the unlatching of fluorescent tube follows uniform spatial distribution is to ensure the uniformity of reaction.
The photooxidation cracking cabinet inlet is equipped with dust-proof filter wet web.Dust-proof filter wet web is used in this improvement project, to exhaust gas
Further dedusting filter is wet, and protection photooxidation cracking cabinet, avoids excessive moisture from causing the accidental discharge of lamp group module, ensure that photooxidation is split
Solve the suitable working environment of cabinet.
TiO is evenly distributed between the lamp group module2Catalysis net.In TiO in this improvement project2The catalysis of catalysis net
Highly efficient destruction and oxidation are carried out to the macromolecular of organic exhaust gas under effect, improve efficiency.
The high energy ultraviolet lamp group module, ozone supply module are equipped with several fluorescent tubes arranged side by side.In this improvement project
Using modularized design, each module is made of side by side several fluorescent tubes, and maintenance need to only take out corresponding module when replacing can not shadow
Ring the work of other modules.
The air-introduced machine is suction type air-introduced machine.The gas mobilization dynamic of package unit is drawn by suction type in this improvement project
Wind turbine provides, and due to the presence of negative pressure, ensures that undressed organic exhaust gas will not be outer in photooxidation cracking cabinet or even package unit
Let out, cause the pollution of environment.
Brief description of the drawings
Fig. 1:A kind of intelligent tail gas photooxidation cracker three-dimensional structure diagram using cavitation liquid technology of the invention
Fig. 2:Inside a kind of photooxidation cracking cabinet of intelligent tail gas photooxidation cracker using cavitation liquid technology of the invention
Three-dimensional structure diagram
Fig. 3:A kind of high energy ultraviolet lamp group of intelligent tail gas photooxidation cracker using cavitation liquid technology of the invention
Module three-dimensional structure diagram
Fig. 4:A kind of high energy ultraviolet lamp group of intelligent tail gas photooxidation cracker using cavitation liquid technology of the invention
Module and ozone supply module lamp group structure chart
In figure:1- cavitation liquid exhaust gas scrubbers, 2- oil gas purification electric field equipment, 3- exhaust gas concentration detection sensors,
4- photooxidations crack cabinet, the dust-proof filter wet webs of 5-, 6- high energy ultraviolet lamp group modules, 7- ozone supply modules, 8-TiO2Catalysis net, 9-
Intelligent control cabinet, 10- suction type air-introduced machines, 11- dry method flue gas integrated treatment tanks, 12- ozone filter screens, 13- postposition exhaust gas are dense
Spend detection sensor, 14- three-way electromagnetic switch valves.
Embodiment
The specific implementation to the present invention is further described below in conjunction with the accompanying drawings.
As shown in Figure 1,2,3, 4, a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology, including cavitation liquid
Body exhaust gas scrubber 1, oil gas purification electric field equipment 2, exhaust gas concentration detection sensor 3, photooxidation cracking cabinet 4, dust-proof filter wet web
5th, high energy ultraviolet lamp group module 6, ozone supply module 7, TiO2Catalysis net 8, single-chip computer control system, suction type air-introduced machine
10th, dry method flue gas integrated treatment tank 11, ozone filter screen 12;The air inlet and exhaust outlet of cavitation liquid exhaust gas scrubber 1 with
Factory's exhaust outlet and oil gas purification electric field equipment 2 connect respectively, and oil gas purification 2 exhaust outlet of electric field equipment and photooxidation cracking cabinet 4 are logical
Air hose connection is crossed, exhaust gas concentration detection sensor 3 is installed on 4 inlet of photooxidation cracking cabinet, and dust-proof filter wet web 5 is split installed in photooxidation
In the slot for solving 4 inlet of cabinet, high energy ultraviolet lamp group module 6 is installed in photooxidation cracking cabinet 4 by certain amount and spacing, smelly
Oxygen supply module 7 is installed in photooxidation cracking cabinet 4 and after high energy ultraviolet lamp group module 6 by certain amount and spacing
End, TiO2Catalysis net 8 is uniformly installed between each high energy ultraviolet lamp group module 6 and between each ozone supply module 7, monolithic
Machine control system is installed in photooxidation cracking 4 Intelligent control cabinet 9 of cabinet, and suction type air-introduced machine 10 is installed on photooxidation cracking 4 outlet air of cabinet
At mouthful and suction type air-introduced machine 10 air outlet access dry method flue gas integrated treatment tank 11, in dry method flue gas integrated treatment tank 12
Exhaust ports ozone filter screen 12 is installed, postposition exhaust gas concentration detection sensor is installed after the ozone filter screen 12
13, the position before last exhaust outlet is provided with three-way electromagnetic switch valve 14, the tracheae that three-way electromagnetic switch valve 14 connects with
The air inlet duct side of cavitation liquid exhaust gas scrubber 1 is connected, as the gas concentration after processing does not reach default
Minimum exhaust gas concentration discharge standard, the single-chip computer control system in the Intelligent control cabinet 9 record this gas component at the same time, under
Once carry out the single-chip computer control system control high energy ultraviolet lamp group mould during vent gas treatment of same sample ingredient in Intelligent control cabinet 9
Block 6 and ozone supply module 7, the shape of the fluorescent tube of every group of unlatching is arranged according to the upper level of corresponding concentration scale, with such
Push away, untill maximum concentration grade.
As shown in Fig. 2, the Intelligent control cabinet 9 for installing SCM system is additionally provided with photooxidation cracking cabinet 4;Photooxidation cracks
Cabinet 4 includes supplying according to spacing and the equally distributed high energy ultraviolet lamp group module 6 of quantity and ozone supply module 7, the ozone
It is located to module 7 after high energy ultraviolet lamp group module 6;The lamp group mould of high energy ultraviolet lamp group module 6, ozone supply module 7
TiO is equipped between block2Catalysis net.High energy ultraviolet lamp group module uses 254nm wavelength+185nm wavelength double waves in the present embodiment
Section efficiency ultraviolet lamp handles exhaust gas, first, using O under the conditions of ultraviolet lamp UVD185nm band ultraviolets2Autoreactivity is given birth to
Into oxonium ion and ozone O3Carry out redox reaction exhaust gas, second, cracking organic waste using the high energy of 254nm band ultraviolets
Gas, third, scribbling TiO using the irradiation of 254nm ultraviolets2Catalysis net generation-OH aoxidize organic exhaust gas.Humidity influences TiO2Urge
Change the catalytic efficiency of net, TiO2Surface hydrophilic, to water strong adsorption, when water content increases, hydrone is with toluene molecule in TiO2
Adsorption competes, and hinders absorption of the toluene molecule in catalyst surface active position so that and surface reaction rate declines, therefore,
By the setting for the filter screen that dehumidifies in the present embodiment, filter wet process is carried out to exhaust gas.
In Fig. 2, high energy ultraviolet lamp group module 6 and ozone supply module 7 devise 5 groups;High energy ultraviolet lamp group mould
Block 6 be mounted with 4 groups, ozone supply module 7 be mounted with 3 groups, shown in Fig. 3,4 fluorescent tubes arranged side by side are equipped with each lamp group module.
High energy ultraviolet lamp group module includes 3 groups including 4 groups, ozone supply module, and every group of lamp group includes 4 fluorescent tubes, control
Fluorescent tube open method processed is:
When exhaust gas concentration is 0-150mg/m3;In high energy ultraviolet lamp group module, every group is only opened 1 fluorescent tube, and all
The lamp strip position that the fluorescent tube that group is opened is opened differs, and arranges integral into " W " or " M " type;In ozone supply module, only open
1 fluorescent tube among first group and the 3rd group, the lamp strip position of unlatching are staggered;
When exhaust gas concentration is 150-200mg/m3, in high energy ultraviolet lamp group module, 2 fluorescent tubes of every group of unlatching, integral into
“>" and "<" staggered;In ozone supply module, 2 fluorescent tubes in first group and second group, the lamp strip position of unlatching are opened
“>" or "<" type;
When exhaust gas concentration is 200-250mg/m3, in high energy ultraviolet lamp group module, first group and the 3rd group of fluorescent tube it is whole
Open, second group and the 4th group is opened 2 fluorescent tubes and fluorescent tube is staggered;In ozone supply module, every group is opened 2 lamps
Pipe, integral into ">" and "<" staggered;
When exhaust gas concentration is 250mg/m3More than, all fluorescent tubes of high energy ultraviolet lamp group module are opened;Ozone supply mould
In block, first group of fluorescent tube is all turned on, and second group and the 3rd group of fluorescent tube open 2 fluorescent tubes, second and third group of fluorescent tube arrangement is in
“>" or "<" type.
As shown in Figure 1,2,3, 4, the work of a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology of the invention
It is as mode:First can be by the useless of plant emissions by the liquid cavitation of the cavitation liquid exhaust gas scrubber of autonomous Design
Macromolecule contaminant decomposes under microcosmic localized hyperthermia's high pressure in gas, simultaneously flows through the useless of the cavitation liquid exhaust gas scrubber
Gas can cool down, and in favor of the processing to exhaust gas below, the exhaust gas by preliminary treatment can be passed through in oil gas purification electric field equipment 2,
High energy electron, ion, excited state particle and the freedom with strong oxidizing property that oil gas purification electric field equipment 2 produces under high voltages
Base interacts with the pollutant in exhaust gas, larger contaminant molecule, fluid etc. is decomposed in the extremely short time,
With the O that caused a large amount of hydroxys (- OH) are extremely strong with active oxygen (- O) isoreactivity free radical and oxidisability3, with pernicious gas
Molecule chemically reacts, and waits follow up device further to locate for small-molecule substance the larger contaminant degradation of molecule first
Reason, subsequent exhaust gas enter efficient photooxidation cracking cabinet babinet 4, and organic exhaust gas is successively by the further dedusting filter of dust-proof filter wet web 5
Wet effect, high energy ultraviolet lamp group 6 chain scission to organic exhaust gas macromolecular of module, after ozone supply module 7 is to chain rupture
The further oxidation of small molecule exhaust gas and in this process TiO2The catalytic action that catalysis net 8 participates in, organic exhaust gas
Substantially it is broken down into CO2、H2O, sulfur oxide, nitrogen oxide etc., are installed on efficient photooxidation cracking cabinet case in processing procedure
The exhaust gas concentration detection sensor 3 of 4 inlet of body can detect pollutant concentration in real time and signal is fed back to microcontroller control system
System, single-chip computer control system is according to input-signal judging respective concentration scope and enables the control program of autonomous optimization design and controls
High energy ultraviolet lamp group module 6 processed, 7 regular stacked switch of ozone supply module realize the energy-efficient place to organic exhaust gas
Reason, the gas after processing realize sulphur, nitrogen oxygen under the action of suction type air-introduced machine 10 into dry method flue gas integrated treatment tank 11
The fixation of compound, being provided with ozone filter screen 12 in the exhaust outlet of dry method flue gas integrated treatment tank 11 will can generate in whole system
Unconsumed ozone reduction be oxygen, ensure that the zero-emission of ozone, needed before the discharge of gas after treatment through later
The detection of exhaust gas concentration detection sensor 13 is put, the detection data meeting Real-time Feedback of postposition exhaust gas concentration detection sensor 13 is to intelligence
Energy switch board 9, the gas concentration after such as handling do not reach the minimum exhaust gas concentration discharge standard of default, then Intelligent control cabinet
9 pipe switch that can control three-way electromagnetic switch valve 14 that gas is discharged into air side are closed, so that untreated gas up to standard
Body is conveyed again by pipeline to be given to leading portion processing equipment and handles again, until the detection of postposition exhaust gas concentration detection sensor 13
Numerical value meets the concentration standard value of default, and Intelligent control cabinet 9 can just control three-way electromagnetic switch valve 14 to open gas and be discharged into
The pipe switch of air, while single-chip computer control system control high energy ultraviolet lamp group module 6 and ozone in Intelligent control cabinet 9
The fluorescent tube of 7 every groups of unlatchings of supplying module, its fluorescent tube are arranged shape according to the arrangement of the upper level of corresponding concentration scale, are finally realized
Ultra-clean discharge after VOCs treatment.
Embodiments above is merely to illustrate the technical solution being not intended to limit the present invention.Any of spirit of the present invention is not departed from
Modification or local replacement, should all cover among scope of the presently claimed invention.
Claims (9)
- A kind of 1. intelligent tail gas photooxidation cracker using cavitation liquid technology, it is characterised in that:Including cavitation liquid exhaust gas Wash mill, oil gas purification electric field equipment, exhaust gas concentration detection sensor, photooxidation cracking cabinet, dust-proof filter wet web, high energy ultraviolet Lamp group module, ozone supply module, TiO2Catalysis net, single-chip computer control system, suction type air-introduced machine, dry method flue gas integrated treatment Tank, ozone filter screen;The cavitation liquid exhaust gas scrubber is connected with oil gas purification electric field equipment by air hose, described Oil gas purifies electric field equipment and is connected with photooxidation cracking cabinet by air hose, and the exhaust gas concentration detection sensor is installed on described Photooxidation cracking cabinet inlet, the dust-proof filter wet web are installed in the slot of photooxidation cracking cabinet inlet, and the high energy is purple Outside line lamp group module is installed in the photooxidation cracking cabinet by certain amount and spacing, and the single-chip computer control system is installed on institute In the Intelligent control cabinet for stating photooxidation cracking cabinet, the air-introduced machine is installed at the photooxidation cracking cabinet air outlet and the negative pressure The air outlet of formula air-introduced machine accesses the dry method flue gas integrated treatment tank, and it is comprehensive that the ozone filter screen is installed on the dry method flue gas In the exhaust outlet for closing process tank;Postposition exhaust gas concentration detection sensor is installed after the ozone filter screen, is vented finally Position before mouthful is provided with three-way electromagnetic switch valve, and tracheae and the washing of cavitation liquid exhaust gas of the connection of three-way electromagnetic switch valve fill The air inlet duct side put is connected, as the gas concentration after handling does not reach the minimum exhaust gas concentration discharge mark of default Standard, the pipe switch that Intelligent control cabinet controls three-way electromagnetic switch valve that gas is discharged into air side are closed, and gas passes through pipeline Conveying is given to leading portion processing equipment and handles again again, and the single-chip computer control system can be anti-according to exhaust gas concentration detection sensor The combination open and close of the information control lamp group module of feedback.
- 2. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1, its feature exist In:The lamp group module includes the equally distributed high energy ultraviolet lamp group module of array and ozone supply module, and the ozone supplies It is located to module after high energy ultraviolet lamp group module.
- 3. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 2, its feature exist In:The single-chip computer control system is turned on and off in high energy ultraviolet lamp group module and ozone supply module according to exhaust gas concentration Corresponding fluorescent tube, the fluorescent tube layout that high energy ultraviolet lamp group module and ozone supply the module fluorescent tube is opened follow spatial distribution Uniformity principle.
- 4. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1 or 2, its feature It is:The photooxidation cracking cabinet inlet is equipped with the dust-proof filter wet web of changeable type.
- 5. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1 or 2, its feature It is:TiO is evenly distributed between the high energy ultraviolet lamp group module2Catalysis net.
- 6. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1 or 2, its feature It is:Several fluorescent tubes arranged side by side are equipped with each lamp group module.
- 7. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1, its feature exist In:The air-introduced machine is suction type air-introduced machine.
- 8. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 1, its feature exist In:The high energy ultraviolet lamp group module includes 3 groups including 4 groups, ozone supply module, and every group of lamp group includes 4 fluorescent tubes, control Fluorescent tube open method is:When exhaust gas concentration is 0-150mg/m3;In high energy ultraviolet lamp group module, every group is only opened 1 fluorescent tube, and all groups of unlatchings Fluorescent tube open lamp strip position differ, integral into " W " or " M " type arrange;In ozone supply module, first group is only opened It is staggered with 1 fluorescent tube in the 3rd group of centre, the lamp strip position of unlatching;When exhaust gas concentration is 150-200mg/m3, in high energy ultraviolet lamp group module, 2 fluorescent tubes of every group of unlatching, integral into ">" and “<" staggered;In ozone supply module, open first group and second group in 2 fluorescent tubes, unlatching lamp strip position ">" or “<" type;When exhaust gas concentration is 200-250mg/m3, in high energy ultraviolet lamp group module, first group and the 3rd group of fluorescent tube are all turned on, Second group and the 4th group is opened 2 fluorescent tubes and fluorescent tube is staggered;In ozone supply module, every group is opened 2 fluorescent tubes, whole Body into ">" and "<" staggered;When exhaust gas concentration is 250mg/m3More than, all fluorescent tubes of high energy ultraviolet lamp group module are opened;In ozone supply module, First group of fluorescent tube is all turned on, and second group and the 3rd group of fluorescent tube open 2 fluorescent tubes, second and third group of fluorescent tube arrangement in ">" or “<" type.
- 9. a kind of intelligent tail gas photooxidation cracker using cavitation liquid technology according to claim 8, its feature exist In:When the gas concentration after processing does not reach the minimum exhaust gas concentration discharge standard of default, the microcontroller control system System records this gas component, carries out the single-chip computer control system in Intelligent control cabinet during the vent gas treatment of same sample ingredient next time High energy ultraviolet lamp group module and ozone supply module are controlled, the shape of the fluorescent tube of every group of unlatching is according to corresponding concentration scale Upper level is arranged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711266285.3A CN108014595A (en) | 2017-12-05 | 2017-12-05 | A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711266285.3A CN108014595A (en) | 2017-12-05 | 2017-12-05 | A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108014595A true CN108014595A (en) | 2018-05-11 |
Family
ID=62078260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711266285.3A Pending CN108014595A (en) | 2017-12-05 | 2017-12-05 | A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108014595A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111001241A (en) * | 2019-12-31 | 2020-04-14 | 佛山市三水秉发金属制品有限公司 | Organic waste gas treatment equipment and treatment method |
CN112546776A (en) * | 2020-11-23 | 2021-03-26 | 珠海格力智能装备有限公司 | Air conditioning system pipeline piece welding waste gas treatment device and use method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060081541A1 (en) * | 2004-10-20 | 2006-04-20 | Five Star Technologies, Inc. | Water treatment processes and devices utilizing hydrodynamic cavitation |
CN105056721A (en) * | 2015-07-24 | 2015-11-18 | 安徽红太阳新材料有限公司 | Novel waste rubber desulphurization waste gas three-stage energy-saving green treatment process method |
CN105233668A (en) * | 2015-10-15 | 2016-01-13 | 深圳市百欧森环保科技开发有限公司 | Waste gas photolysis treatment equipment |
CN106310929A (en) * | 2015-06-19 | 2017-01-11 | 十堰东环环保设备有限公司 | Photocatalytic compound exhaust gas treatment system |
CN107051092A (en) * | 2017-06-12 | 2017-08-18 | 广州薪光合环保技术有限公司 | Waste gas treatment equipment |
CN207786253U (en) * | 2017-12-05 | 2018-08-31 | 青岛科技大学 | A kind of tail gas photooxidation cracker using cavitation liquid technology |
-
2017
- 2017-12-05 CN CN201711266285.3A patent/CN108014595A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060081541A1 (en) * | 2004-10-20 | 2006-04-20 | Five Star Technologies, Inc. | Water treatment processes and devices utilizing hydrodynamic cavitation |
CN106310929A (en) * | 2015-06-19 | 2017-01-11 | 十堰东环环保设备有限公司 | Photocatalytic compound exhaust gas treatment system |
CN105056721A (en) * | 2015-07-24 | 2015-11-18 | 安徽红太阳新材料有限公司 | Novel waste rubber desulphurization waste gas three-stage energy-saving green treatment process method |
CN105233668A (en) * | 2015-10-15 | 2016-01-13 | 深圳市百欧森环保科技开发有限公司 | Waste gas photolysis treatment equipment |
CN107051092A (en) * | 2017-06-12 | 2017-08-18 | 广州薪光合环保技术有限公司 | Waste gas treatment equipment |
CN207786253U (en) * | 2017-12-05 | 2018-08-31 | 青岛科技大学 | A kind of tail gas photooxidation cracker using cavitation liquid technology |
Non-Patent Citations (1)
Title |
---|
张龙等: "绿色化学", 华中科技大学出版社 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111001241A (en) * | 2019-12-31 | 2020-04-14 | 佛山市三水秉发金属制品有限公司 | Organic waste gas treatment equipment and treatment method |
CN112546776A (en) * | 2020-11-23 | 2021-03-26 | 珠海格力智能装备有限公司 | Air conditioning system pipeline piece welding waste gas treatment device and use method |
CN112546776B (en) * | 2020-11-23 | 2022-04-22 | 珠海格力智能装备有限公司 | Air conditioning system pipeline piece welding waste gas treatment device and use method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107983120A (en) | A kind of intelligent tail gas photooxidation cracking treating device using oil gas purification techniques | |
CN108211686A (en) | A kind of tail gas photooxidation cracking purification method | |
CN108096969A (en) | A kind of tail gas photooxidation method for cracking treatment based on vaporizing oil-gas purification techniques | |
CN108543418A (en) | It is a kind of can multistage-combination insertion slot type purification exhaust gas device | |
CN207786305U (en) | A kind of tail gas photooxidation cracking treating device using oil gas purification techniques | |
CN210635915U (en) | Kitchen garbage fermentation treatment and odor purification system | |
CN104258726B (en) | A kind of device of photocatalysis treatment volatile organic matter | |
CN108176171A (en) | A kind of tail gas photooxidation method for cracking treatment using cavitation fluid purification technology | |
CN207786253U (en) | A kind of tail gas photooxidation cracker using cavitation liquid technology | |
CN207430012U (en) | A kind of oil field TREATMENT OF VOCs device | |
CN108014595A (en) | A kind of intelligent tail gas photooxidation cracker using cavitation liquid technology | |
CN215901278U (en) | VOCs recovery processing is with activated carbon fiber adsorption regenerating unit | |
CN112807962A (en) | Chemical waste gas treatment system | |
CN110559827B (en) | Treatment process of papermaking waste gas | |
CN205796920U (en) | A kind of two sections of bioanalysises and the symphyogenetic emission-control equipment of photocatalytic method | |
CN207786340U (en) | A kind of intelligence tail gas photooxidation cracking purifier | |
CN107983149A (en) | A kind of intelligence tail gas photooxidation cracking purifier | |
CN216295623U (en) | Waste gas treatment separation and purification device | |
CN115722052A (en) | Device and method for removing volatile organic compounds in industrial waste gas | |
CN214862444U (en) | Integrated waste gas treatment device of integrated form | |
CN215027575U (en) | High-efficient deodorizing device of sewage treatment plant | |
CN215233244U (en) | Waste gas treatment equipment for sewage treatment station of paper mill | |
CN213061520U (en) | Exhaust deodorization system of papermaking workshop | |
CN210674748U (en) | Purify organic waste gas's device in coordination | |
CN210206407U (en) | Novel combined type stink and VOCs combined treatment equipment for industrial and mining enterprises |
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 |