CN106914113A - A kind of chlorobenzene exhaust-gas treatment tank - Google Patents
A kind of chlorobenzene exhaust-gas treatment tank Download PDFInfo
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- CN106914113A CN106914113A CN201710127728.4A CN201710127728A CN106914113A CN 106914113 A CN106914113 A CN 106914113A CN 201710127728 A CN201710127728 A CN 201710127728A CN 106914113 A CN106914113 A CN 106914113A
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- wash water
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- 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
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- 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
- B01D53/77—Liquid phase processes
- B01D53/79—Injecting reactants
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- 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
- 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
- B01D53/86—Catalytic processes
- B01D53/8659—Removing halogens or halogen compounds
- B01D53/8662—Organic halogen compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
- B01D2251/304—Alkali metal compounds of sodium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/604—Hydroxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- 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
Abstract
The present invention relates to a kind of chlorobenzene exhaust-gas treatment tank, photochemical catalytic oxidation area, Di Lv areas, alkali cleaning area, dehumidifier, activated carbon adsorption layer and exhaust fan are followed successively by bottom-up；Photochemical catalytic oxidation area is located at foot, and ultraviolet light generator and catalytic unit are provided with photochemical catalytic oxidation area, and ultraviolet light generator includes controller, ballast and ultraviolet tube；Catalytic unit is aluminium base TiO2Net, is enclosed in outside ultraviolet tube, and photochemical catalytic oxidation area bottom is provided with exhaust inlet pipe and waste gas gas distribution pipe；Di Lv areas are provided with originally water spray system, filler, drop filtrate aggregation apparatus and drop filtrate and store groove；Alkali cleaning area is provided with waste gas alkali cleaning component, and waste gas alkali cleaning component includes that alkali wash water spray equipment, alkali wash water store groove and alkali wash water circulating pump；Alkali cleaning area top is provided with dehumidifier；Dehumidifier top is provided with activated carbon adsorption layer；Exhaust fan is installed at the conical tank body of topmost.
Description
Technical field
The present invention relates to technical field of waste gas treatment, especially a kind of chlorobenzene exhaust-gas treatment tank.
Background technology
Pollutant in chlorobenzene waste gas includes chlorobenzene, 1,2- dichloro-benzenes, 1,3- dichloro-benzenes, trichloro-benzenes, tetrachlorobenzene etc. totally 12
Homologue is planted, they are widely used in all trades and professions, and including materials synthesis, agricultural chemicals, medicine etc., most of such material is difficult quilt
Institute of Micro-biology degrades, easily Enriching accumulation in the environment, and major part has carcinogenic, teratogenesis, mutagenesis etc. to people and biology
Toxic action.
The processing method of chlorobenzene waste gas has absorption method, condensation method, membrane separation process and bioanalysis etc..
Absorption method refers to be fixed one or more different component Adsorption Concentrations in waste gas using porosu solid adsorbent
In its surface, the purpose for other components separate is reached, be the most ripe method of current most widely used, technology, general selection is inhaled
Attached ability is strong, raw material is sufficient and reproducible adsorbent, such as activated carbon.The method purification efficiency is high, pollutants removal rate is high, nothing two
Secondary pollution and equipment is simple, beneficial to realizing automation, easy to operate；Have the disadvantage that adsorption capacity not high is unsuitable for processing high concentration
Waste gas, adsorbent is required to waste gas component, is easily failed when having other impurities, is frequently changed adsorbent and is also resulted in great number cost.
Condensation method is the physical property under condition of different temperatures using material with different saturated vapor pressures, by reducing
System temperature improves the process that system pressure makes the organic matter in steam condition condense and be separated from waste gas.Should
Without being related to complex separations technology, process is simple to have the disadvantage the certain pressure of processing procedure needs and temperature, treatment low concentration gives up method
Gas high cost.
Membrane separation process comes across eighties of last century sixties earliest, at that time mainly for desalting processing and desalinization, and
It is now widely used in every profession and trade, such as petrochemical industry, pharmacy.The method is mainly led to using waste gas each component under pressure promotion
Speed when crossing selective membrane is different, so that target contaminant is separated with other components.The method simple structure, low energy consumption is high
The rate of recovery and non-secondary pollution, but the price of critical component film is high, and difficult in maintenance, processing speed is slow, so at present can't
Reach large-scale application.
Biochemical method waste gas is the new Organic Waste Gas Pollution control technology for developing rapidly in recent years, biological earliest
Method is to be applied to deodorization treatment.Early 1980s are risen in Holland and Germany, gradually receive the U.S., Japan and other Europe
The attention of man of the U.S., has currently turned into one of main method of VOCs treatment.
Chlorobenzene exhaust gas constituents are complicated, and qualified discharge is difficult to realize using above-mentioned single method.
The content of the invention
The technical problem to be solved in the present invention is：Overcome chlorobenzene waste gas fully complicated, difficult to realize using single method
A kind of difficulty of qualified discharge, there is provided chlorobenzene exhaust-gas treatment tank.
The technical solution adopted for the present invention to solve the technical problems is：A kind of chlorobenzene exhaust-gas treatment tank, bottom-up
It is followed successively by photochemical catalytic oxidation area, Di Lv areas, alkali cleaning area, dehumidifier, activated carbon adsorption layer and exhaust fan.
Described photochemical catalytic oxidation area is located at foot；Ultraviolet light generator is provided with described photochemical catalytic oxidation area and is urged
Makeup is put；Described ultraviolet light generator includes controller, ballast and ultraviolet tube；Described catalytic unit is aluminium base
TiO2Net, is enclosed in outside ultraviolet tube, and photochemical catalytic oxidation area bottom is provided with exhaust inlet pipe and waste gas gas distribution pipe；Described purple
Outer light lamp tube is high intensity, the ultraviolet tube of high ozone.
Described Di Lv areas are provided with originally water spray system, filler, drop filtrate aggregation apparatus and drop filtrate and store groove；It is described
Originally water spray system be helical form spray equipment, the liquid that ejects is presented vaporific, and mixing together between water smoke, does not stay
Dead angle；Described filler is by wood chip, activated carbon, haydite, hollow plastic beads according to volume ratio 1:1:1:1 is mixed；It is described
Drop filtrate to store the cross section of groove be circle, drop filtrate stores groove top and is provided with drop filtrate aggregation apparatus, described drop filtrate
The lower end diameter of aggregation apparatus stores the diameter of groove topmost less than drop filtrate, and drop filtrate aggregation apparatus can assemble back drop filtrate
It flow to drop filtrate and stores groove.
Described alkali cleaning area is provided with waste gas alkali cleaning component, and described waste gas alkali cleaning component sprays including superposed alkali wash water
Shower device, the alkali wash water positioned at bottom store groove and the alkali wash water that stores alkali wash water in groove pumps into the alkali of alkali wash water spray equipment
Washing lotion circulating pump.
Described alkali wash water spray equipment is helical form spray equipment, and the liquid for ejecting is presented vaporific, and between water smoke
Mixing together, does not stay dead angle, is conducive to expanding the contact area of waste gas and solution, improves absorptivity and assimilation effect.
The cross section that described alkali wash water stores groove is circle, and alkali wash water stores groove top and is provided with alkali wash water aggregation apparatus,
The lower end diameter of described alkali wash water aggregation apparatus stores the diameter of groove topmost less than alkali wash water, and alkali wash water aggregation apparatus can make
Alkali wash water aggregation is back to alkali wash water and stores groove.
Further, described waste gas alkali cleaning component is also equipped with alkali wash water adding set and tapping equipment, described alkali cleaning
Liquid adding set includes alkali cleaning flow container and agitating device, and alkali wash water adding set connects alkali wash water with valve and circulates by pipeline
Pump.
The alkali wash water that described waste gas alkali cleaning component is used is sodium hydroxide solution；The matched proportion density root of described alkali wash water
Exhausted air quantity and exhaust gas concentration experiment according to treatment determines.
Described alkali cleaning area top is provided with dehumidifier, and dehumidifier is to be collected the big drop in gas, and is allowed to return
Return, reduce the moisture in gas, its operation principle is that gas enters dehumidifier, by a series of bends, from top discharge, and water
Due to the effect of its quality and kinetic energy, when by racetrack portion, straight line falls drop, collides the surface of dehumidifier, and to again
Rebounded under power effect；Further preferred equipment, described dehumidifier is deflection plate dehumidifier or overflowing board dehumidifier.
Described dehumidifier top is provided with activated carbon adsorption layer, and activated carbon is set in described activated carbon adsorption layer, activity
Charcoal requirement have the advantages that hole prosperity, specific surface area is big, adsorption rate is fast, friction resistant, resistance to flushing, as by the long period
Operation, it is found that activated carbon becomes sticky, and just needs to change activated carbon in time during gas velocity reduction.
Specifically, described chlorobenzene exhaust-gas treatment tank middle and lower part is conical tank body for cylinder, upper end, on the tank body
Offer observation port and maintenance replacement port, tank body volume size can according to pending gas flow number depending on, using vertical perpendicular
It is straight to place.
For ease of the clean gas discharge for having processed, pacify at the conical tank body of described chlorobenzene exhaust-gas treatment tank topmost
Equipped with exhaust fan.
The beneficial effects of the invention are as follows, chlorobenzene waste gas is initially entered in photochemical catalytic oxidation area, high intensity, high ozone it is ultraviolet
Light lamp tube sends high energy UV light beam and ozone, irradiates chlorobenzene waste gas, in the presence of catalytic unit, chlorobenzene waste gas is carried out
Collaboration is decomposed, and the pollutant in gas is broken down into the material of small molecule；Most organic matter is converted into more simple water
Good, the degradable material of dissolubility；Gas ascends into Di Lv areas, and the microorganism during the pollutant in gas is filled absorbs drop
Solution；Gas continues rising and is contacted with the alkali wash water of alkali wash water spray equipment ejection, and the polluter in gas is sent out with NaOH
Biochemical reaction, reaction product stores in groove with alkali wash water inflow bottom alkali wash water；Gas subsequently into dehumidifier, in gas
Drop be blocked herein；Then gas enters activated carbon adsorption layer, and the material and drop being mingled with gas are at this
In be intercepted absorb, so far chlorobenzene waste gas be processed into cleaning gas, realize qualified discharge.
Brief description of the drawings
The present invention is further described with reference to the accompanying drawings and examples.
Fig. 1 is the structural representation of the chlorobenzene exhaust-gas treatment tank of embodiments of the invention；
In Fig. 1：1. photochemical catalytic oxidation area, 1-1. ultraviolet light generators, 1-2. catalytic units, 1-3. exhaust inlet pipes, 1-
4. waste gas gas distribution pipe, 2. Di Lv areas, 2-1. originally water spray system, 2-2. fillers, 2-3. drop filtrate aggregation apparatus, the filter of 2-4. drops
Liquid stores groove, 3. alkali cleaning area, 3-1. alkali wash water spray equipments, and 3-2. alkali wash waters store groove, 3-3. alkali wash water circulating pumps, 3-4. alkali
Washing lotion adding set, 3-5. alkali wash water aggregation apparatus, 4. dehumidifier, 5. activated carbon adsorption layer, 6. exhaust fan.
Specific embodiment
In conjunction with the accompanying drawings, the present invention is further explained in detail.These accompanying drawings are simplified schematic diagram, only with
Illustration illustrates basic structure of the invention, therefore it only shows the composition relevant with the present invention.
Of the invention a kind of chlorobenzene exhaust-gas treatment tank as shown in Figure 1, be followed successively by bottom-up photochemical catalytic oxidation area 1,
Di Lv areas 2, alkali cleaning area 3, dehumidifier 4, activated carbon adsorption layer 5 and exhaust fan 6.
Described photochemical catalytic oxidation area 1 is located at the foot of whole device；It is provided with ultraviolet in described photochemical catalytic oxidation area 1
Optical generator 1-1 and catalytic unit 1-2；Described ultraviolet light generator 1-1 includes controller, ballast and ultraviolet tube；
Described catalytic unit 1-2 is aluminium base TiO2Net, is enclosed in outside ultraviolet tube；The bottom of photochemical catalytic oxidation area 1 is provided with waste gas and enters
Tracheae 1-3 and waste gas gas distribution pipe 1-4；Described ultraviolet tube is high intensity, the ultraviolet tube of high ozone.
Described Di Lv areas 2 are provided with originally water spray system 2-1, filler 2-2, drop filtrate aggregation apparatus 2-3 and drop filtrate
Store groove 2-4；Described originally water spray system 2-1 is helical form spray equipment, and the liquid for ejecting is presented vaporific, and water smoke
Between mixing together, do not stay dead angle；Described filler 2-2 is by wood chip, activated carbon, haydite, hollow plastic beads according to volume ratio
1:1:1:1 is mixed；The cross section that described drop filtrate stores groove 2-4 is circle, and drop filtrate stores groove top and is provided with drop filter
Liquid aggregation apparatus 2-3, the lower end diameter of described drop filtrate aggregation apparatus stores the diameter of groove topmost, drop filter less than drop filtrate
Liquid aggregation apparatus can make drop filtrate assemble be back to drop filtrate store groove.
Described alkali cleaning area 3 is provided with waste gas alkali cleaning component, and described waste gas alkali cleaning component includes being located at waste gas alkali cleaning component
The alkali wash water spray equipment 3-1 on top, the alkali wash water positioned at waste gas alkali cleaning component bottom store groove 3-2 and alkali wash water are stored into groove
In alkali wash water pump into the alkali wash water circulating pump 3-3 of alkali wash water spray equipment.
Described alkali wash water spray equipment 3-1 is helical form spray equipment；The liquid that ejects is presented vaporific, and water smoke it
Between mixing together, do not stay dead angle, be conducive to expanding the contact area of waste gas and solution, improve absorptivity and assimilation effect.
The cross section that described alkali wash water stores groove 3-2 is circle, and alkali wash water stores groove 3-2 tops and is provided with alkali wash water aggregation
The lower end diameter of device 3-5, described alkali wash water aggregation apparatus 3-5 stores the diameter of groove 3-2 topmosts, alkali cleaning less than alkali wash water
Liquid aggregation apparatus 3-5 can assemble alkali wash water to be back to alkali wash water and store groove 3-2.
Further, described waste gas alkali cleaning component is also equipped with alkali wash water adding set 3-4 and tapping equipment, described alkali
Washing lotion adding set 3-4 includes alkali cleaning flow container and agitating device, and alkali wash water adding set connects alkali wash water by pipeline with valve
Circulating pump.
The alkali wash water that described waste gas alkali cleaning component is used is sodium hydroxide solution；The matched proportion density root of described alkali wash water
Exhausted air quantity and exhaust gas concentration experiment according to treatment determines.
The described top of alkali cleaning area 3 is provided with dehumidifier 4, and dehumidifier 4 is to be collected the big drop in gas, and is allowed to
Return, reduce the moisture in gas, its operation principle is that gas enters dehumidifier 4, by a series of bends, from top discharge,
And water droplet is due to the effect of its quality and kinetic energy, when by racetrack portion, straight line falls, and collides the surface of dehumidifier, and
Rebounded under to Action of Gravity Field.Dehumidifier 4 is deflection plate dehumidifier or overflowing board dehumidifier.
The described top of dehumidifier 4 is provided with activated carbon adsorption layer 5, and activated carbon is set in described activated carbon adsorption layer 5, living
Property charcoal requirement have the advantages that hole prosperity, specific surface area is big, adsorption rate is fast, friction resistant, resistance to flushing, such as by the long period
Operation, find activated carbon become sticky, gas velocity reduction when just need to change activated carbon in time.
Specifically, described chlorobenzene exhaust-gas treatment tank middle and lower part is conical tank body for cylinder, upper end, on the tank body
Offer observation port and maintenance replacement port, tank body volume size can according to pending gas flow number depending on, using vertical perpendicular
It is straight to place.
For ease of the clean gas discharge for having processed, pacify at the conical tank body of described chlorobenzene exhaust-gas treatment tank topmost
Equipped with exhaust fan 6.
Chlorobenzene waste gas is initially entered in photochemical catalytic oxidation area 1, and high intensity, the ultraviolet tube of high ozone send high energy ultraviolet
Light light beam and ozone, irradiate chlorobenzene waste gas, in the presence of catalytic unit 1-2, collaboration decomposition are carried out to chlorobenzene waste gas, in gas
Pollutant be broken down into the material of small molecule；Most organic matter is converted into more simple good water solubility, degradable
Material；Gas ascends into Di Lv areas 2, and the microorganism during the pollutant in gas is filled absorbs degraded；Gas continues to rise
The alkali wash water sprayed with alkali wash water spray equipment 3-1 is contacted, and the polluter in gas chemically reacts with NaOH, instead
Product is answered to be flowed into during bottom alkali wash water stores groove 3-2 with alkali wash water；Gas exists subsequently into dehumidifier 4, the drop in gas
Here it is blocked；Then gas enters activated carbon adsorption layer 5, and the material and drop being mingled with gas are intercepted herein
Absorb, so far chlorobenzene waste gas is processed into the gas of cleaning, realizes qualified discharge.
With above-mentioned according to desirable embodiment of the invention as enlightenment, by above-mentioned description, relevant staff is complete
Various changes and amendments can be carried out without departing from the scope of the technological thought of the present invention' entirely.The technology of this invention
Property scope is not limited to the content on specification, it is necessary to its technical scope is determined according to right.
Claims (1)
1. a kind of chlorobenzene exhaust-gas treatment tank, it is characterised in that：It is sequentially provided with photochemical catalytic oxidation area (1), drop filter upwards from pot bottom
Area (2), alkali cleaning area (3), dehumidifier (4), activated carbon adsorption layer (5) and exhaust fan (6)；
Foot of the described photochemical catalytic oxidation area (1) positioned at whole device；It is provided with ultraviolet in described photochemical catalytic oxidation area (1)
Optical generator (1-1) and catalytic unit (1-2)；Described ultraviolet light generator (1-1) includes controller, ballast and ultraviolet light
Fluorescent tube；Described catalytic unit (1-2) is aluminium base TiO2Net, is enclosed in outside ultraviolet tube；Photochemical catalytic oxidation area (1) bottom sets
There are exhaust inlet pipe (1-3) and waste gas gas distribution pipe (1-4)；Described ultraviolet tube is high intensity, the ultraviolet lamp of high ozone
Pipe；
Described Di Lv areas (2) are provided with originally water spray system (2-1), filler (2-2), drop filtrate aggregation apparatus (2-3) and drop
Filtrate stores groove (2-4)；Described originally water spray system (2-1) is helical form spray equipment, and the liquid for ejecting is presented mist
Mixing together between shape, and water smoke, does not stay dead angle；Described filler (2-2) is by wood chip, activated carbon, haydite, hollow plastic beads
According to volume ratio 1:1:1:1 is mixed；The cross section that described drop filtrate stores groove (2-4) is circle, and drop filtrate stores groove
Top is provided with drop filtrate aggregation apparatus (2-3), and the lower end diameter of described drop filtrate aggregation apparatus stores groove most less than drop filtrate
The diameter on top, drop filtrate aggregation apparatus can make drop filtrate assemble be back to drop filtrate store groove；
Described alkali cleaning area (3) is provided with waste gas alkali cleaning component, and described waste gas alkali cleaning component sprays including superposed alkali wash water
Shower device (3-1), the alkali wash water positioned at bottom store groove (3-2) and the alkali wash water that stores alkali wash water in groove pumps into alkali wash water spray
The alkali wash water circulating pump (3-3) of shower device；
Described alkali wash water spray equipment (3-1) is helical form spray equipment；The liquid for ejecting is presented vaporific, and between water smoke
Mixing together, does not stay dead angle, is conducive to expanding the contact area of waste gas and solution, improves absorptivity and assimilation effect；
The cross section that described alkali wash water stores groove (3-2) is circle, and alkali wash water stores groove (3-2) top and is provided with alkali wash water aggregation
Device (3-5), the lower end diameter of described alkali wash water aggregation apparatus (3-5) stores the straight of groove (3-2) topmost less than alkali wash water
Footpath, alkali wash water aggregation apparatus (3-5) can be assembled alkali wash water to be back to alkali wash water and store groove (3-2)；
Further, described waste gas alkali cleaning component is also equipped with alkali wash water adding set (3-4) and tapping equipment, described alkali cleaning
Liquid adding set (3-4) includes alkali cleaning flow container and agitating device, and alkali wash water adding set connects alkali wash water by pipeline with valve
Circulating pump；
The alkali wash water that described waste gas alkali cleaning component is used is sodium hydroxide solution；The matched proportion density of described alkali wash water is according to place
Exhausted air quantity and the exhaust gas concentration experiment of reason determine；
Described alkali cleaning area (3) top is provided with dehumidifier (4), and dehumidifier (4) is to be collected the big drop in gas, and is made
Return, reduce the moisture in gas, its operation principle is that gas enters dehumidifier (4), by a series of bends, from top row
Go out, and water droplet is due to the effect of its quality and kinetic energy, when by racetrack portion, straight line falls, and collides the surface of dehumidifier, and
Rebounded under to Action of Gravity Field；Dehumidifier (4) is deflection plate dehumidifier or overflowing board dehumidifier；
Described dehumidifier (4) top is provided with activated carbon adsorption layer (5), and activated carbon is set in described activated carbon adsorption layer (5),
Activated carbon requirement have the advantages that hole prosperity, specific surface area is big, adsorption rate is fast, friction resistant, resistance to flushing, such as by it is more long when
Between operation, find activated carbon become sticky, gas velocity reduction when just need to change activated carbon in time；
Specifically, described chlorobenzene exhaust-gas treatment tank middle and lower part is conical tank body for cylinder, upper end, opened up on the tank body
Have observation port and maintenance replacement port, tank body volume size can according to pending gas flow number depending on, put vertically using vertical
Put；
For ease of the clean gas discharge for having processed, it is provided with the conical tank body of described chlorobenzene exhaust-gas treatment tank topmost
Exhaust fan (6).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710127728.4A CN106914113A (en) | 2017-03-06 | 2017-03-06 | A kind of chlorobenzene exhaust-gas treatment tank |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710127728.4A CN106914113A (en) | 2017-03-06 | 2017-03-06 | A kind of chlorobenzene exhaust-gas treatment tank |
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Cited By (6)
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|---|---|---|---|---|
| CN108187483A (en) * | 2018-01-26 | 2018-06-22 | 常州大学 | A kind of naphthalene tail-gas deep treating column |
| CN108310940A (en) * | 2018-01-30 | 2018-07-24 | 河南省诚建检验检测技术股份有限公司 | A kind of building materials monomer and product burns experimental rig burning waste gas purification system |
| CN109647189A (en) * | 2019-01-24 | 2019-04-19 | 福建热心环保科技有限公司 | One kind being based on light-catalysed VOC waste gas treatment equipment |
| CN109663477A (en) * | 2018-12-30 | 2019-04-23 | 安徽广信农化股份有限公司 | A kind of method for treatment of waste material preparing ethyl chloroformate |
| CN110721563A (en) * | 2019-08-29 | 2020-01-24 | 武汉时泰环保科技有限公司 | Chlorine-containing organic waste gas purification treatment process |
| CN113457359A (en) * | 2021-07-13 | 2021-10-01 | 中国矿业大学 | Device and method for treating organic waste gas by coupling ultraviolet light catalysis with microorganisms |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101444700A (en) * | 2008-12-04 | 2009-06-03 | 上海大学 | Method for improving purification of insoluble organic waste gas of biological trickling filter tower |
| CN101850213A (en) * | 2009-12-31 | 2010-10-06 | 南京大学 | Biotrickling filter for treating waste gas and treating method thereof |
| CN202169138U (en) * | 2010-10-08 | 2012-03-21 | 中山大学 | Device for biological treatment of high-temperature malodorous waste gases |
| CN102423611A (en) * | 2011-10-20 | 2012-04-25 | 广州狮岭皮革皮具产业研究中心有限公司 | Method for removing VOCs by UV light catalytic oxidation cooperating with biofiltration |
| CN202778234U (en) * | 2012-08-28 | 2013-03-13 | 佛山市新泰隆环保设备制造有限公司 | Combined-type organic waste gas treatment device |
| CN103239986A (en) * | 2013-05-17 | 2013-08-14 | 北京帝力伟业科技开发有限公司 | Biological filtering device and technology for treating organic waste gas |
| CN103752166A (en) * | 2013-12-30 | 2014-04-30 | 哈尔滨工业大学深圳研究生院 | Biology-atomization combined deodorization process and device for removing odor |
| CN104001413A (en) * | 2013-02-27 | 2014-08-27 | 上海化学工业区中法水务发展有限公司 | Processing method for malodorous gas of chemical area sewage plant |
| CN104548899A (en) * | 2014-12-15 | 2015-04-29 | 常州大学 | Integral odor treatment device for sewage treatment plant |
| CN104628226A (en) * | 2015-01-15 | 2015-05-20 | 常州大学 | Integrated farm waste treatment system |
| CN104923067A (en) * | 2015-06-06 | 2015-09-23 | 常州大学 | Integrated CS2 exhaust air treatment device |
| CN204735096U (en) * | 2015-06-11 | 2015-11-04 | 杨洁 | NOx exhaust treatment device |
| CN105498524A (en) * | 2016-01-22 | 2016-04-20 | 冯愚斌 | Container-type low-concentration organic waste gas purification treatment device |
| CN105999962A (en) * | 2016-07-12 | 2016-10-12 | 包禾欣 | Asphalt flue gas purification treatment equipment |
| CN106039983A (en) * | 2016-07-13 | 2016-10-26 | 盐城工学院 | Biofilm formation starting method of biotrickling system for degrading hydrophobic and volatile organic compounds |
| CN106268233A (en) * | 2016-09-06 | 2017-01-04 | 常州大学 | CH3nH2(g) emission-control equipment |
-
2017
- 2017-03-06 CN CN201710127728.4A patent/CN106914113A/en active Pending
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101444700A (en) * | 2008-12-04 | 2009-06-03 | 上海大学 | Method for improving purification of insoluble organic waste gas of biological trickling filter tower |
| CN101850213A (en) * | 2009-12-31 | 2010-10-06 | 南京大学 | Biotrickling filter for treating waste gas and treating method thereof |
| CN202169138U (en) * | 2010-10-08 | 2012-03-21 | 中山大学 | Device for biological treatment of high-temperature malodorous waste gases |
| CN102423611A (en) * | 2011-10-20 | 2012-04-25 | 广州狮岭皮革皮具产业研究中心有限公司 | Method for removing VOCs by UV light catalytic oxidation cooperating with biofiltration |
| CN202778234U (en) * | 2012-08-28 | 2013-03-13 | 佛山市新泰隆环保设备制造有限公司 | Combined-type organic waste gas treatment device |
| CN104001413A (en) * | 2013-02-27 | 2014-08-27 | 上海化学工业区中法水务发展有限公司 | Processing method for malodorous gas of chemical area sewage plant |
| CN103239986A (en) * | 2013-05-17 | 2013-08-14 | 北京帝力伟业科技开发有限公司 | Biological filtering device and technology for treating organic waste gas |
| CN103752166A (en) * | 2013-12-30 | 2014-04-30 | 哈尔滨工业大学深圳研究生院 | Biology-atomization combined deodorization process and device for removing odor |
| CN104548899A (en) * | 2014-12-15 | 2015-04-29 | 常州大学 | Integral odor treatment device for sewage treatment plant |
| CN104628226A (en) * | 2015-01-15 | 2015-05-20 | 常州大学 | Integrated farm waste treatment system |
| CN104923067A (en) * | 2015-06-06 | 2015-09-23 | 常州大学 | Integrated CS2 exhaust air treatment device |
| CN204735096U (en) * | 2015-06-11 | 2015-11-04 | 杨洁 | NOx exhaust treatment device |
| CN105498524A (en) * | 2016-01-22 | 2016-04-20 | 冯愚斌 | Container-type low-concentration organic waste gas purification treatment device |
| CN105999962A (en) * | 2016-07-12 | 2016-10-12 | 包禾欣 | Asphalt flue gas purification treatment equipment |
| CN106039983A (en) * | 2016-07-13 | 2016-10-26 | 盐城工学院 | Biofilm formation starting method of biotrickling system for degrading hydrophobic and volatile organic compounds |
| CN106268233A (en) * | 2016-09-06 | 2017-01-04 | 常州大学 | CH3nH2(g) emission-control equipment |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108187483A (en) * | 2018-01-26 | 2018-06-22 | 常州大学 | A kind of naphthalene tail-gas deep treating column |
| CN108310940A (en) * | 2018-01-30 | 2018-07-24 | 河南省诚建检验检测技术股份有限公司 | A kind of building materials monomer and product burns experimental rig burning waste gas purification system |
| CN109663477A (en) * | 2018-12-30 | 2019-04-23 | 安徽广信农化股份有限公司 | A kind of method for treatment of waste material preparing ethyl chloroformate |
| CN109647189A (en) * | 2019-01-24 | 2019-04-19 | 福建热心环保科技有限公司 | One kind being based on light-catalysed VOC waste gas treatment equipment |
| CN110721563A (en) * | 2019-08-29 | 2020-01-24 | 武汉时泰环保科技有限公司 | Chlorine-containing organic waste gas purification treatment process |
| CN113457359A (en) * | 2021-07-13 | 2021-10-01 | 中国矿业大学 | Device and method for treating organic waste gas by coupling ultraviolet light catalysis with microorganisms |
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