CN108392968A - Rubbish loss stench processing system in a kind of garbage transfer station - Google Patents
Rubbish loss stench processing system in a kind of garbage transfer station Download PDFInfo
- Publication number
- CN108392968A CN108392968A CN201810327029.9A CN201810327029A CN108392968A CN 108392968 A CN108392968 A CN 108392968A CN 201810327029 A CN201810327029 A CN 201810327029A CN 108392968 A CN108392968 A CN 108392968A
- Authority
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- China
- Prior art keywords
- ozone
- outer case
- rubbish
- transfer station
- wind turbine
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- 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.)
- Granted
Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 116
- 238000012545 processing Methods 0.000 title claims abstract description 86
- 238000012546 transfer Methods 0.000 title claims abstract description 39
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 title claims abstract description 26
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 137
- 238000004332 deodorization Methods 0.000 claims abstract description 82
- 238000004140 cleaning Methods 0.000 claims abstract description 48
- 238000004804 winding Methods 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 238000005507 spraying Methods 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 17
- 230000008569 process Effects 0.000 claims abstract description 14
- 230000005587 bubbling Effects 0.000 claims abstract description 11
- 238000003780 insertion Methods 0.000 claims abstract description 4
- 230000037431 insertion Effects 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 33
- 238000007599 discharging Methods 0.000 claims description 26
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 22
- 238000004062 sedimentation Methods 0.000 claims description 12
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 11
- 230000005284 excitation Effects 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 4
- 238000006386 neutralization reaction Methods 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 7
- 238000009434 installation Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 102
- 239000010865 sewage Substances 0.000 description 21
- 239000000126 substance Substances 0.000 description 16
- 239000000243 solution Substances 0.000 description 13
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 238000010586 diagram Methods 0.000 description 12
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- 230000035943 smell Effects 0.000 description 8
- 239000007921 spray Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000009931 harmful effect Effects 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 229910021529 ammonia Inorganic materials 0.000 description 6
- VHRGRCVQAFMJIZ-UHFFFAOYSA-N cadaverine Chemical compound NCCCCCN VHRGRCVQAFMJIZ-UHFFFAOYSA-N 0.000 description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- XOCUXOWLYLLJLV-UHFFFAOYSA-N [O].[S] Chemical compound [O].[S] XOCUXOWLYLLJLV-UHFFFAOYSA-N 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 5
- 230000036541 health Effects 0.000 description 5
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000001569 carbon dioxide Substances 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000010790 dilution Methods 0.000 description 4
- 239000012895 dilution Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 231100000614 poison Toxicity 0.000 description 4
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000003085 diluting agent Substances 0.000 description 3
- 238000004880 explosion Methods 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 230000007096 poisonous effect Effects 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- -1 carbon dioxide Chemical compound 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000002085 irritant Substances 0.000 description 2
- 231100000021 irritant Toxicity 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 230000002186 photoactivation Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- KIDHWZJUCRJVML-UHFFFAOYSA-N putrescine Chemical compound NCCCCN KIDHWZJUCRJVML-UHFFFAOYSA-N 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 208000033999 Device damage Diseases 0.000 description 1
- 239000005700 Putrescine Substances 0.000 description 1
- WJEIYVAPNMUNIU-UHFFFAOYSA-N [Na].OC(O)=O Chemical compound [Na].OC(O)=O WJEIYVAPNMUNIU-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000010793 electronic waste Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- 239000006210 lotion Substances 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
- 235000015961 tonic Nutrition 0.000 description 1
- 230000001256 tonic effect Effects 0.000 description 1
- 229960000716 tonics Drugs 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000005406 washing Methods 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
- B01D53/34—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
- 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
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/38—Removing components of undefined structure
- B01D53/40—Acidic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—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
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biomedical Technology (AREA)
- Dispersion Chemistry (AREA)
- Toxicology (AREA)
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a kind of garbage transfer stations,Disclose rubbish loss stench processing system in a kind of garbage transfer station,Solves the negative effect of the foul gas of rubbish loss in garbage transfer station to the environment of environment in station and surrounding,It includes ozone generating-device,Deodorization chamber * winding paper and processing pond,The first active wind turbine is connected between ozone generating-device and deodorization chamber * winding paper,Deodorization chamber * winding paper includes the ultraviolet generation device and spraying and cleaning apparatus of outer case and installation in the outer case,Outer case bottom carries smelly liquid collecting pit,Smelly liquid collecting pit bottom is connect by smelly liquid pump with processing pond,Outer case is also associated with the second active wind turbine,Second active wind turbine is connected with bubbling pipe,Bubbling pipe insertion process bottom of pond portion,Processing pond is closed and with the excessive tracheae at connection top,Exhaust gas processing device includes outer housing and the low-temperature plasma component in outer housing and ultraviolet lamp,The generation of follow-up foul gas is reduced while removing foul gas,Efficiently thoroughly.
Description
Technical field
The present invention relates to a kind of garbage transfer station, more particularly to rubbish loss Odor control system in a kind of garbage transfer station
System.
Background technology
As people's living standard is continuously improved, the municipal refuse generated in life process also constantly increases, need into
Row centralized processing.Municipal refuse is with going to centralized processing such as sanitary filling field, composting plant, incinerator, the mistake for recycling station
It needs to carry out integrating collection and garbage classification by garbage transfer station in journey.
The classification of rubbish can be divided into material rubbish group, organic waste group, inorganic refuse group, poisonous and harmful rubbish group.Material
Rubbish group includes glass, magnetism or nonmagnetic metal, waste paper, rubber, plastics；Organic waste group is mainly garbage, biology
Rubbish, inorganic refuse group include boiler ash sediment, brick and tile, ceramics etc.；Poisonous and harmful rubbish group include old and useless battery, waste fluorescent light tube,
The electronic waste of the waste electrical equipments such as insecticide container, expired medicament, clinical waste and useless television set, phone, computer.Wherein have
Machine rubbish group can wait the decomposition of hair tonics ferment to generate some with foul smell in garbage transporting or during the storage of garbage transfer station
Substance such as ammonia, cadaverine, hydrogen sulfide, methyl mercaptan and poisonous and harmful rubbish group in may carry foul smell substance such as diformazan two
Sulphur, carbon disulfide and styrene etc..
The substance of these foul smells significantly reduces in garbage transfer station working environment quality and to garbage transfer station
Around environment bring negative effect, therefore the system that rubbish loss foul smell is handled in a kind of garbage transfer station of needs.
Invention content
In view of the deficiencies of the prior art, it is an object of the present invention to provide rubbish loss Odor controls in a kind of garbage transfer station
System reduces the substance of the foul smell in rubbish, improves working environment quality in garbage transfer station and reduces garbage transfer station
The negative effect of ambient enviroment.
The present invention above-mentioned technical purpose technical scheme is that：
Rubbish loss stench processing system in a kind of garbage transfer station, including ozone generating-device, deodorization chamber * winding paper, processing pond and tail gas
Processing unit, is connected with the first active wind turbine between the ozone generating-device and deodorization chamber * winding paper, the deodorization chamber * winding paper includes outer case
With the ultraviolet generation device and spraying and cleaning apparatus of installation in the outer case, the outer case bottom carries smelly liquid collecting pit,
The smelly liquid collecting pit bottom is connect by smelly liquid pump with processing pond, and the outer case is also associated with the second active wind turbine, described
Second active wind turbine is connected with bubbling pipe, and the bubbling pipe insertion process bottom of pond portion, the processing pond is closed and its top carries
Connect the excessive tracheae of exhaust gas processing device, the exhaust gas processing device include outer housing and the low temperature in outer housing etc. from
Sub-component and ultraviolet lamp.
By using above-mentioned technical proposal, ozone generating-device generates ozone and is sent into deodorization chamber * winding paper by the first active wind turbine
It is interior, the shape ozone atmosphere in deodorization chamber * winding paper；
After rubbish enters deodorization chamber * winding paper, foul gas and rubbish surface attachment of the loss in ozone atmosphere are volatilizable to go out stench
The substance of gas resolves into gas such as carbon dioxide, ammonia and the sulphur oxidation of small molecule under the ozone oxidation of ultraviolet photoactivation
At the substance without foul smell after closing object etc. or being aoxidized；
The indoor air of deodorization takes out smelly room as the first deodorization tail gas by the discharge of the second active wind turbine, and coordinates the first active wind turbine
The air for carrying ozone in deodorization chamber * winding paper is replaced, ozone concentration is kept；
Deodorization chamber * winding paper is in the deodorization course of work, and effusion exudation instills smelly liquid collecting pit in rubbish, and deodorization chamber * winding paper periodically starts
Spraying and cleaning apparatus cleaning showers liquid cleans deodorization chamber * winding paper, contains with volatile foul gas in effusion and cleaning solution after cleaning
Substance or dissolved with foul gas, the sewage that the two mixes in smelly liquid collecting pit is delivered to by smelly liquid pump in processing pond；
First deodorization tail gas of the second active wind turbine discharge still also has the ozone of high level, and deodorization tail gas is passed through right in processing pond
Sewage carries out oxidation processes, improves ozone utilization rate, while removing soluble easily in water in deodorization tail gas and with irritant or toxic
Harmful gas, such as ammonia, methanol and oxygen sulfur compound, reduce the burden of exhaust gas processing device；
The gas that processing pond is gone out simultaneously enters tail gas deodorization device as the second deodorization tail gas, and the second deodorization tail gas is passing through place
Its interior water content improves after managing pond, and acting on for low-temperature plasma component can generate more free hydroxyl in exhaust gas processing device
Base so that the reactions such as remaining organic principle for being not readily dissolved in water such as putrescine, cadaverine aoxidize in the second deodorization tail gas, so that
Tail gas no foul smell is discharged, ultraviolet lamp is then used to activate the ozone in the second deodorization tail gas, accelerates its reaction, reduces discharge tail gas
In ozone, avoid not that the ozone that voluntarily decomposes causes harmful effect to environment in time；
Thus this system to the foul gas of rubbish loss and distributes the source material of foul gas and handles, and deodorization chamber * winding paper
It is interior to also act as bactericidal effect using ultraviolet light, slow down rubbish and ferment during terminal is stored in short term, removes foul gas
Reduce the generation of follow-up foul gas simultaneously, for the more existing method handled only for foul gas, more efficiently and
Foul gas loss is to the baneful influence of environment when reducing rubbish point transporting from garbage transfer station to final process.
Preferably, the cleaning solution of the spraying and cleaning apparatus cleaning deodorization chamber * winding paper is akaline liquid.
By using above-mentioned technical proposal, ozone is in ultraviolet light activation with extremely strong oxidisability, and meeting is externally
The metal surface of cabinet wall and deodorization indoor set carries out oxidation and forms fine and close peroxide films, uses the cleaning of alkalinity
Liquid prevents damage peroxide films, and outer case inner wall and deodorization indoor set is avoided to suffer erosion；Simultaneously using the clear of alkalinity
The sewage that washing lotion obtains equally is in alkalinity, improves the absorbability that processing pond decomposes foul gas the sour gas generated.
Preferably, the cleaning solution of the spraying and cleaning apparatus is sodium carbonate liquor.
By using above-mentioned technical proposal, the cleaning solution of spraying and cleaning apparatus is sodium carbonate liquor etc..Sodium carbonate liquor is certainly
Spraying and cleaning apparatus spray and under when, sodium carbonate liquor can absorb in outer case in air by foul gas or volatilization effluvium
The water-soluble gas such as ammonia that the substance decomposition of body generates, sour gas such as carbon dioxide, oxynitrides and oxygen sulfur compound,
Clean air environment in outer case；When sodium carbonate liquor is fallen into demarcation strip and smelly liquid collecting tank, sodium carbonate is collected with smelly liquid
In slot and the sewage of separation plate surface neutralizes, and release carbon dioxide forms bubble, and softening the spot of solidification makes it fall into smelly liquid
Collecting pit；Sewage after cleaning in smelly liquid collecting pit is in alkalinity, and the heavy metal ion in sewage precipitates after combining carbonate, carries
53 effect of high sedimentation basin；The sewage of alkalinity is pumped by sewage pump in processing pond, and first formed with next batch garbage disposal removes
Smelly tail gas mixes, and improves treatment tank absorption efficiency.
Preferably, the deodorization chamber * winding paper includes two hoppers that turn, described to turn to be horizontally arranged with open work in hopper
Dynamic door, the dodge gate will turn to be divided into inside hopper the discharging chamber of the feed cavity and lower section of top, turn hopper described in two and be divided into
One end of material feeding box and feed box, the discharging chamber of the material feeding box and outer case is tightly connected and the upper end of its feed cavity carry into
Expect hermatic door, the feed cavity of the feed box and the other end of outer case are tightly connected and the bottom of its discharging chamber is close with discharging
Closure door, the outer case is interior to carry conveyer belt, and one end of the conveyer belt is located at below the discharging chamber of material feeding box, and the other end is located at
Above the feed cavity of feed box, the conveyer belt is transmitted from material feeding box to feed box direction.
By using above-mentioned technical proposal, feeding seal door is opened, after rubbish puts into the feed cavity of material feeding box, closes charging
Hermatic door and the dodge gate for opening material feeding box, rubbish enter outer case and fall on a moving belt, is conveyed through by transmission belt outer
Babinet is simultaneously fallen into the feed cavity of feed box；The dodge gate for opening feed box, the rubbish in the feed cavity of feed box is sent into out
The dodge gate of feed box is closed after the discharging chamber of hopper, then opens discharging hermatic door, and the rubbish after deodorization is sent to garbage truck
Or temporary storage point, thus avoid outer case from including a large amount of loss when rubbish is put into of the air with ozone；
Coordinate the transmission of conveyer belt simultaneously, it can be achieved that successional rubbish deodorization work, improves the working efficiency, processing of this system
Load, and constantly into new rubbish in deodorization chamber * winding paper, the foul gas of loss and the substance of volatilization foul gas constantly with
Ozone reaction improves the ozone utilization rate that ozone generator generates.
Preferably, the first active wind turbine is located at it close to the side of material feeding box with respect to the second active wind turbine.
By using above-mentioned technical proposal, both material feeding box and feed box are in contrast, certainly outer during feed box discharging
The air capacity of babinet loss from inside to outside is much larger than in material feeding box fill process from the air capacity of outer case loss from inside to outside, and thus the
One active wind turbine and the second active wind turbine are located at the direction of transfer phase of air-flow direction and conveyer belt in outer case between the two
Together, it is less than in outer case close to material feeding box side close to ozone content in the air of feed box side in outer case, reduces deodorization
The amount of room garbage feeding and ozone mutually outer loss when discharging reduces ozone and loses, cost-effective；It reduces simultaneously empty around feed box
Ozone concentration in gas avoids causing damages to workers ' health and generating possible security risk.
Preferably, the tail gas unit includes circulation ozone concentration detector and circulating fan, the outer housing packet
The plasma chamber of connection and ultraviolet room are included, the low-temperature plasma component and circulation ozone concentration detector are installed on plasma
Room, the ultraviolet lamp are installed on ultraviolet room, the circulating fan connection plasma chamber and outer case.
It is right for larger larger or continuous processing the system of design of garbage treatment quantity by using above-mentioned technical proposal
Ozone concentration requires high in deodorization chamber * winding paper, and ozone is through its concentration of circulation ozone concentration detector when the second tail gas enters in plasma chamber
Still higher, the second deodorization tail gas that part is handled to decomposition organic principle by circulating fan through plasma chamber is used as diluent
It is filled in outer case, improves ozone utilization rate；Ultraviolet room processing load is reduced simultaneously, it is cost-effective.
Preferably, the outer case quantity is more than air in one and outer case and is not attached to lead to, each outer case
It is each provided with the second active wind turbine and bubbling pipe.
By using above-mentioned technical proposal, increases outer case quantity to improve system and handle load.
Preferably, the ultraviolet generation device damages part of coming down to a lower group by ozone excitation component and ozone and forms, the ozone
Excitation component includes several ultraviolet irradiation lamps being evenly distributed on along conveyer belt direction of transfer inside outer case, the ozone damage drop
Component includes the intensive heating tube being arranged in outer case close to feed box side.
By using above-mentioned technical proposal, ozone damages part of coming down to a lower group and heats air close to the side of feed box in outer case, adds
Substance in fast ozone and rubbish occurs oxidation and accelerates ozone decomposed simultaneously, reduces ozone concentration, reduces feed box discharging process
When the air that goes out of loss in ozone concentration, avoid causing damages to workers ' health and generating possible security risk.
Preferably, the outer case quantity be more than one and the two adjacent outer cases in air communication, not with institute
Stating outer case that the first active wind turbine is directly connected to, it close to one end of material feeding box is connected with ozone supplementary device.
By using above-mentioned technical proposal, increases outer case quantity and utilized with improving system processing load and improving ozone
Rate, while ozone supplementary device is segmented supplemental ozone, prevents to ensure that each outer case dust removing effects cause and the first active wind
The excessively high lower explosion limit for reaching ozone of ozone concentration in the outer case that machine is directly connected to.
Preferably, the two adjacent outer case communicating positions be located at the first rotation wind turbine and ozone damage come down to a lower group part it
Between side or ozone supplementary device and ozone damage come down to a lower group the side between part.
By using above-mentioned technical proposal, guarantee maintains to have from the air that a upper outer case flows into next outer case
Ozone concentration, while reducing ozone and damaging part load of coming down to a lower group, reduce the cost that ozone damages part of coming down to a lower group.
Preferably, including elevator pump, sedimentation basin and run-off, elevator pump connection processing pond and sedimentation basin, institute
It states and is separated by overflow plate between sedimentation basin and run-off.
By using above-mentioned technical proposal, subsequent processing is carried out to the sewage in processing pond, reach after discharge standard into
Row discharge, environmental protection.
In conclusion the invention has the advantages that：
1. the foul gas of pair rubbish loss and the source material for distributing foul gas are handled, and using purple in deodorization chamber * winding paper
Outer light also acts as bactericidal effect, slows down rubbish and ferments during terminal is stored in short term, is reduced while removing foul gas
The generation of follow-up foul gas for the more existing method handled only for foul gas, more efficiently and reduces rubbish
Baneful influence of the foul gas loss to environment when point transports from garbage transfer station to final process；
2 at the same the gas that is gone out of processing pond enter tail gas deodorization device as the second deodorization tail gas, the second deodorization tail gas is passing through
Its interior water content improves after processing pond, and acting on for low-temperature plasma component can generate more dissociate in exhaust gas processing device
Hydroxyl improves vent gas treatment effect；
3. the ozone of loss and discharge is controlled and handled in pair course of work, ozone loss is reduced, it is cost-effective, and keep away
Exempt to cause damages to workers ' health and generate possible security risk；
4. the cleaning solution that spraying and cleaning apparatus cleans deodorization chamber * winding paper is akaline liquid.Avoid outer case inner wall and deodorization chamber * winding paper built-in
The sewage set and suffered erosion, while being obtained using the cleaning solution of alkalinity is equally in alkalinity, improves processing pond and is decomposed to foul gas
The absorbability of the sour gas of generation；
5. the transmission of material feeding box and treatment box cooperation conveyer belt is, it can be achieved that successional rubbish deodorization work, improves this system
Working efficiency, processing load and ozone utilization rate；
6. for larger larger or continuous processing the system of design of garbage treatment quantity, the second tail gas of part is as ozone in outer case
Diluent recycle, improve ozone utilization rate, while reducing ultraviolet room processing load, it is cost-effective；
7, increase outer case quantity to improve treatment effeciency and be improved the route that cycle of ozone utilizes and mend using ozone
It fills and sets, improve ozone utilization rate, while preventing the excessively high lower explosion limit for reaching ozone of ozone concentration, and reduce ozone damage drop
Component load reduces the cost that ozone damages part of coming down to a lower group.
Description of the drawings
Fig. 1 is the attachment structure schematic diagram of stench processing system in embodiment one；
Fig. 2 is the structural schematic diagram of stench processing system in embodiment one；
Fig. 3 is the structural schematic diagram one of deodorization chamber * winding paper in embodiment one；
Fig. 4 is the structural schematic diagram two of deodorization chamber * winding paper in embodiment one；
Fig. 5 is the structural schematic diagram of deodorization chamber * winding paper, the second active wind turbine and processing pond in embodiment one；
Fig. 6 is the structural schematic diagram of exhaust gas processing device in embodiment one；
Fig. 7 is the structural schematic diagram of sedimentation basin and run-off in embodiment one；
Fig. 8 is the structural schematic diagram of deodorization chamber * winding paper in embodiment three；
Fig. 9 is the attachment structure schematic diagram of stench processing system in example IV；
Figure 10 is the attachment structure schematic diagram of stench processing system in embodiment five；
Figure 11 is the structural schematic diagram of exhaust gas processing device in embodiment five；
Figure 12 is the attachment structure schematic diagram of stench processing system in embodiment six.
Reference numeral：1, ozone generating-device；11, room occurs；111, air inlet；112, air outlet；12, ozone generation group
Part；13, deduster；14, dilution air；2, the first active wind turbine；3, deodorization chamber * winding paper；31, outer case；311, gas-tight door；312, smelly
Liquid collecting pit；3121, smelly liquid pump；313, flase floor；314, offgas outlet；315, conveyer belt；32, ultraviolet generation device；321、
Ozone excitation component；3211, ultraviolet irradiation lamp；322, ozone damages part of coming down to a lower group；3221, heating tube；333, spraying and cleaning apparatus；
331, cleaning fluid tank；332, liquid pump is cleaned；333, spray head；34, turn hopper；34a, material feeding box；34b, feed box；341, movable
Door；342, feed cavity；343, discharging chamber；344, feeding seal door；345, discharge hermatic door；4, the second active wind turbine；41, it is bubbled
Pipe；5, processing pond；51, overflow tracheae；52, blow-off pipe；521, elevator pump；53, sedimentation basin；54, run-off；541, delivery pipe；55、
Overflow plate；6, exhaust gas processing device；61, outer housing；611, plasma chamber；6111, low-temperature plasma component；612, ultraviolet room；
6121, ultraviolet lamp；62, circulation ozone concentration detector；63, circulating fan；7, ozone supplementary device.
Specific implementation mode
Below in conjunction with attached drawing, invention is further described in detail.
Embodiment one,
In conjunction with shown in attached drawing 1, rubbish loss stench processing system in a kind of garbage transfer station, including ozone generating-device 1, first
Active wind turbine 2, dilution air 14, deodorization chamber * winding paper 3, the second active wind turbine 4 and processing pond 5.
In conjunction with shown in attached drawing 1 and attached drawing 2, ozone generating-device 1 is smelly in room 11 including room 11 occurs and mounted on occurring
Oxygen generating assembly 12, ozone generating assembly 12 prepare ozone by principle of air.It includes air inlet 111 and air outlet that room 11, which occurs,
112, air inlet 111 can select to be directly connected to outside air or connection deduster 13 according to outside air quality, and selection herein connects
Connect deduster 13.Air outlet 112 connects the air inlet 111 of the first active wind turbine 2.The air inlet 111 of dilution air 14 and dedusting
Device 13 is to connection.
In conjunction with shown in attached drawing 3 and attached drawing 4, deodorization chamber * winding paper 3 includes outer case 31 and the ultraviolet generation in outer case 31
Device 32 and spraying and cleaning apparatus 333.Outer case 31 is closed babinet, is provided at both ends with the gas-tight door of sealable lid conjunction
311, the first active wind turbine 2 is communicated with outer case 31 with the air outlet 112 of dilution air 14.The bottom of outer case 31 is provided with
The flase floor 313 for walking and placing rubbish is stamped in smelly liquid collecting pit 312,312 top of smelly liquid collecting pit.Rubbish is placed on grid
After in panel, the effusion that rubbish surface penetrates instills in smelly liquid collecting pit 312.
Ultraviolet generation device 32 is made of ozone excitation component 321, ozone excitation component 321 be include ultraviolet irradiation lamp
3211, uniformly the upper top surface inside outer case 31 is fixed in arrangement to ultraviolet irradiation lamp 3211.
Spraying and cleaning apparatus 333 includes the cleaning fluid tank 331 being located at outside outer case 31, cleaning liquid pump 332, several uniform rows
Cloth is fixed on the spray head 333 of the upper top surface inside outer case 31.Cleaning fluid tank 331, cleaning liquid pump 332 and spray head 333 according to
It is secondary by piping connection, control valve is installed on pipeline.The arrangement of spray head 333 and ultraviolet irradiation lamp 3211 is according to practical feelings
Depending on condition, but and meets 333 height of spray head and be respectively positioned on the lower section of ultraviolet irradiation lamp 3211.Cleaning solution choosing in cleaning fluid tank 331
With the cleaning solution of alkalinity.
In conjunction with shown in attached drawing 1 and attached drawing 3, spraying and cleaning apparatus 333 periodically starts, clear to carrying out spraying inside outer case 31
It washes, the cleaning solution after cleaning flows into smelly liquid collecting pit 312 and is mixed into sewage with effusion.After effusion and cleaning in cleaning solution
Containing with volatile foul gas substance or dissolved with foul gas, can distribute or volatilize foul gas.Smelly liquid collecting pit
312 are pumped to sewage in processing pond 5 equipped with smelly liquid pump 3121, smelly liquid pump 3121.
In conjunction with shown in attached drawing 4 and attached drawing 5, outer case 31 also carries offgas outlet 314, and offgas outlet 314 and second is actively
The air inlet 111 of wind turbine 4 connects, and babinet is denoted as the first deodorization tail gas from 314 gone out gas of offgas outlet.Second active wind turbine 4
Air outlet 112 be connected with bubbling pipe 41, below liquid level in 41 insertion process pond 5 of bubbling pipe.5 upper end of processing pond seals, together
When processing in addition to being connected with bubbling pipe 41, the upper end is connected with excessive tracheae 51 and bottom is connected with blow-off pipe 52.
In conjunction with shown in attached drawing 5 and attached drawing 6, the tracheae 51 that overflows is connect with exhaust gas processing device 6 to be seen, the tracheae 51 that overflows flows at tail gas
The gas of reason device 6 is denoted as the second deodorization tail gas.Exhaust gas processing device 6 include outer housing 61, outer housing 61 include connection etc.
Ion chamber 611 and ultraviolet room 612.The useful low-temperature plasma component 6111 that low-temperature plasma occurs of installation in plasma chamber 611,
Low-temperature plasma component 6111 can reach discharge voltage to gas applied voltage, keep gas breakdown, generation include electronics, it is various
Mixture including ion, atom and free radical.Ultraviolet lamp 6121 is installed in ultraviolet room 612.
In conjunction with shown in attached drawing 7, blow-off pipe 52 is connected with elevator pump 521, and elevator pump 521 connects sedimentation basin 53, sedimentation basin 53
It has been disposed adjacent run-off 54.Separated by overflow plate 55 between neutralization precipitation pond 53 and run-off 54, run-off 54 is connected with
Delivery pipe 541, sewage are discharged in the interior precipitation of sedimentation basin 53, supernatant liquor overflow to run-off 54, then by blow-off pipe 52.
Among the above ozone generating assembly 12, gas-tight door 311, low-temperature plasma component 6111 structure be the prior art,
And the innovative point of non-present invention, therefore be not set forth in detail herein.
The operation principle of embodiment one：
Ozone generating-device 1 generates ozone and is sent into deodorization chamber * winding paper 3 by the first active wind turbine 2, the shape ozone gas in deodorization chamber * winding paper 3
Atmosphere；
After rubbish enters deodorization chamber * winding paper 3, foul gas and rubbish surface attachment of the loss in ozone atmosphere are volatilizable to be gone out to dislike
The substance of odour resolves into the gas of small molecule under the ozone oxidation of ultraviolet photoactivation, such as carbon dioxide, oxynitrides
With oxygen sulfur compound etc.；
Air in deodorization chamber * winding paper 3 takes out smelly room as the first deodorization tail gas by the discharge of the second active wind turbine 4, and coordinates the first active wind
Machine 2 replaces the air that ozone is carried in deodorization chamber * winding paper 3, keeps ozone concentration；
Deodorization chamber * winding paper 3 is in the deodorization course of work, and effusion exudation instills smelly liquid collecting pit 312 in rubbish, and deodorization chamber * winding paper 3 is regular
Start 333 cleaning showers liquid of spraying and cleaning apparatus and clean deodorization chamber * winding paper 3, contains in effusion and cleaning solution after cleaning and carry volatile evil
The substance of odour or dissolved with foul gas, the sewage that the two mixes in smelly liquid collecting pit 312 is delivered to by smelly liquid pump 3121
In processing pond 5；
First deodorization tail gas of the second active wind turbine 4 discharge still also has the ozone of high level, deodorization tail gas to be passed through in processing pond 5
Oxidation processes are carried out to sewage, improve ozone utilization rate, while being removed soluble easily in water in deodorization tail gas and with irritant or have
The harmful gas of poison, such as ammonia, oxynitrides and oxygen sulfur compound, reduce the burden of exhaust gas processing device 6；
The gas that processing pond 5 is gone out simultaneously enters tail gas deodorization device as the second deodorization tail gas, and the second deodorization tail gas is passing through
Its interior water content improves after processing pond 5, and acting on for low-temperature plasma component 6111 can generate more in exhaust gas processing device 6
Free hydroxyl group so that in the second deodorization tail gas remaining organic principle for being not readily dissolved in water such as styrene, cadaverine etc. react oxygen
Change, so that discharge tail gas no foul smell, ultraviolet lamp 6121 is then used to activate the ozone in the second deodorization tail gas, and it is anti-to accelerate it
It answers, reduces the ozone in discharge tail gas, the ozone not decomposed voluntarily in time is avoided to cause harmful effect to environment；
Sewage in processing pond 5 passes through 54 subsequent processing of neutralization precipitation pond 53 and run-off, is being arranged after reaching discharge standard
It puts, environmental protection；
Thus this system to the foul gas of rubbish loss and distributes the source material of foul gas and handles, and deodorization chamber * winding paper
Bactericidal effect is also acted as using ultraviolet light in 3, slows down rubbish and ferments during terminal is stored in short term, remove foul gas
Reduce the generation of follow-up foul gas simultaneously, for the more existing method handled only for foul gas, more efficiently and
Foul gas loss is to the baneful influence of environment when reducing rubbish point transporting from garbage transfer station to final process.
Embodiment two,
Rubbish loss stench processing system in a kind of garbage transfer station, based on being improved on the basis of embodiment one.Spray
The cleaning solution of cleaning device 333 is sodium carbonate liquor etc..Sodium carbonate liquor from spraying and cleaning apparatus 333 spray and under when, carbonic acid
Sodium solution can absorb in outer case 31 water solubility generated by the substance decomposition of foul gas or the foul gas that volatilizees in air
Gas such as ammonia, sour gas such as carbon dioxide, oxynitrides and oxygen sulfur compound clean air environment in outer case 31.
When sodium carbonate liquor is fallen into demarcation strip and smelly liquid collecting tank, in sodium carbonate and smelly liquid collecting tank and demarcation strip
The sewage on surface neutralizes, and release carbon dioxide forms bubble, and softening the spot of solidification makes it fall into smelly liquid collecting pit 312；Cleaning
The sewage in smelly liquid collecting pit 312 is in alkalinity afterwards, and the heavy metal ion in sewage precipitates after combining carbonate, improves sedimentation basin
53 effects；The sewage of alkalinity is pumped by sewage pump in processing pond 5, the first deodorization tail gas phase formed with next batch garbage disposal
Mixing improves treatment tank 5 its absorption efficiency.
Embodiment three,
In conjunction with shown in attached drawing 8, rubbish loss stench processing system in a kind of garbage transfer station, based on the basis of embodiment one
It is improved.Deodorization chamber * winding paper 3 further includes two and turns hopper 34 and conveyer belt 315 is arranged in the outer case 31.
Turn to be horizontally arranged with open dodge gate 341 in hopper 34, dodge gate 341 is horizontal positioned will to turn 34 inside points of hopper
It is divided into the discharging chamber 343 of the feed cavity 342 and lower section of top.When dodge gate 341 is closed, feed cavity 342 and discharging chamber 343 are mutual not
Connection.Outer case 31 is elongated, and two turn the both ends that hopper 34 is located at outer case 31, respectively material feeding box 34a and goes out
Hopper 34b.One end of the discharging chamber 343 of material feeding box 34a and outer case 31 is tightly connected and the upper end of its feed cavity 342 carry into
Expect hermatic door 344, the feed cavity 342 of feed box 34b is tightly connected with the other end of outer case 31 and the bottom of its discharging chamber 343
With discharging hermatic door 345.
Conveyer belt 315 is transmitted from material feeding box 34a to the directions feed box 34b, and one end is located at the discharging chamber of material feeding box 34a
343 lower sections, the other end are located at 342 top of feed cavity of feed box 34b.
First active wind turbine, 2 opposite second active wind turbine 4 is located at it close to the side of material feeding box 34a.Material feeding box 34a and go out
In contrast both hopper 34b, charging are much larger than during feed box 34b dischargings from the air capacity of the loss from inside to outside of outer case 31
From the air capacity of the loss from inside to outside of outer case 31 in case 34a fill process.Thus the first active wind turbine 2 and the second active wind turbine 4
It is identical with the direction of transfer of conveyer belt 315 to be located at air-flow direction in outer case 31 between the two, in outer case 31 it is close go out
In the air of the sides hopper 34b ozone content less than close to the sides material feeding box 34a, reduce in outer case 31 3 rubbish of deodorization chamber * winding paper into
Expect with the amount of ozone mutually outer loss when discharging, reduce ozone and lose, it is cost-effective；It reduces in feed box 34b surrounding airs simultaneously
Ozone concentration, avoid causing damages to workers ' health and generating possible security risk.
Ultraviolet generation device 32 further includes that ozone damages part 322 of coming down to a lower group, and it includes intensive be arranged in outer container that ozone, which damages part 322 of coming down to a lower group,
Heating tube 3221 of the body 31 close to the sides feed box 34b.Ozone damages one of part 322 of coming down to a lower group in outer case 31 close to feed box 34b
Air is heated in side, accelerates ozone and is aoxidized with the substance in rubbish；Accelerate ozone decomposed simultaneously, reduce ozone concentration, reduces
Ozone concentration in the air that loss goes out when feed box 34b discharging processes, avoids causing damages to workers ' health and generating possibility
Security risk.
The operation principle of embodiment three：
Feeding seal door 344 is opened, after rubbish puts into the feed cavity 342 of material feeding box 34a, feeding seal door 344 is closed and opens
The dodge gate 341 of material feeding box 34a, rubbish enter outer case 31 and fall on conveyer belt 315, and outer container is conveyed through by transmission belt
Body 31 is simultaneously fallen into the feed cavity 342 of feed box 34b；
Rubbish in the feed cavity 342 of feed box 34b is sent into going out for feed box 34b by the dodge gate 341 for opening feed box 34b
The dodge gate 341 of feed box 34b is closed after expecting chamber 343, then opens discharging hermatic door 345, the rubbish after deodorization is sent to rubbish
Thus rubbish vehicle or temporary storage point avoid outer case 31 from including a large amount of loss when rubbish is put into of the air with ozone；
Simultaneously coordinate conveyer belt 315 transmission, it can be achieved that successional rubbish deodorization work, improve this system working efficiency,
Load is handled, and constantly into rubbish new in deodorization chamber * winding paper 3, the foul gas of loss and the substance of volatilization foul gas are not
Disconnected and ozone reaction improves the ozone utilization rate that ozone generator generates.
Example IV,
In conjunction with shown in attached drawing 9, rubbish loss stench processing system in a kind of garbage transfer station, based on the basis of embodiment one
It is improved.31 quantity of outer case is more than air in one and outer case 31 and is not attached to lead to, and each outer case 31 is each provided with
Second active wind turbine 4 and bubbling pipe 41 increase by 31 quantity of outer case to improve system and handle load.
Embodiment five,
In conjunction with shown in attached drawing 10 and attached drawing 11, rubbish loss stench processing system in a kind of garbage transfer station is based on embodiment
It is improved on the basis of two.Tail gas unit includes circulation ozone concentration detector 62 and circulating fan 63, circulation ozone concentration
Detector 62 is installed on plasma chamber 611, and circulating fan 63 connects plasma chamber 611 and outer case 31.
The operation principle of embodiment five：
For larger larger or continuous processing the system of design of garbage treatment quantity, height is required to ozone concentration in deodorization chamber * winding paper 3, the
Two tail gas enter ozone when in plasma chamber 611, and through circulation ozone concentration detector 62, its concentration is still higher, passes through circulated air
The second deodorization tail gas that part is handled decomposition organic volatile by machine 63 through plasma chamber 611 is filled with outer case 31 as diluent
It is interior, improve ozone utilization rate；Ultraviolet room 612 is reduced simultaneously handles load, it is cost-effective.
Embodiment six,
In conjunction with shown in attached drawing 12, rubbish loss stench processing system in a kind of garbage transfer station, the basis based on embodiment two
On be improved.31 quantity of outer case is more than one, and particular number can be depending on actual conditions, and 31 quantity of outer case is herein
Three.In addition to the outer case 31 being directly connected to the first active wind turbine 2, other outer cases 31 are connected close to one end of material feeding box 34a
There are ozone supplementary device 7, ozone supplementary device 7 identical as ozone generating-device 1.
The outer case 31 being directly connected to the first active wind turbine 2 its be located at the first rotation wind turbine and ozone damage and come down to a lower group part 322
Between side with and its adjacent another outer case 31 is located at ozone supplementary device 7 and ozone damage is come down to a lower group between part 322 side
Face is connected.
Two outer cases 31 not being connected to directly with the first active wind turbine 2 are located at ozone supplementary device 7 and ozone at it
The side damaged between part 322 of coming down to a lower group is connected.
The operation principle of embodiment six：
Increase by 31 quantity of outer case to improve treatment effeciency and be improved the route that cycle of ozone utilizes and mend using ozone
It fills and sets 7, improve ozone utilization rate, while preventing the excessively high lower explosion limit for reaching ozone of ozone concentration, and reduce ozone damage
It comes down to a lower group 322 load of part, reduces ozone damage and come down to a lower group the cost of part 322.
This specific embodiment is only explanation of the invention, is not limitation of the present invention, people in the art
Member can as needed make the present embodiment the modification of not creative contribution after reading this specification, but as long as at this
It is all protected by Patent Law in the right of invention.
Claims (10)
1. rubbish loss stench processing system in a kind of garbage transfer station, which is characterized in that including ozone generating-device（1）, remove
Smelly room（3）, processing pond（5）And exhaust gas processing device（6）, the ozone generating-device（1）And deodorization chamber * winding paper（3）Between be connected with
One active wind turbine（2）, the deodorization chamber * winding paper（3）Including outer case（31）With mounted on outer case（31）Interior ultraviolet generation device
（32）And spraying and cleaning apparatus（333）, the outer case（31）Bottom carries smelly liquid collecting pit（312）, the smelly liquid collection
Pond（312）Bottom passes through smelly liquid pump（3121）With processing pond（5）Connection, the outer case（31）It is also associated with the second active wind turbine
（4）, the second active wind turbine（4）It is connected with bubbling pipe（41）, the bubbling pipe（41）Insertion process pond（5）Bottom, it is described
Processing pond（5）Closed and its top is with connection exhaust gas processing device（6）Excessive tracheae（51）, the exhaust gas processing device（6）
Including outer housing（61）With mounted on outer housing（61）Interior low-temperature plasma component（6111）And ultraviolet lamp（6121）.
2. rubbish loss stench processing system in a kind of garbage transfer station according to claim 1, which is characterized in that described
Spraying and cleaning apparatus（333）Clean deodorization chamber * winding paper（3）Cleaning solution is akaline liquid.
3. rubbish loss stench processing system in a kind of garbage transfer station according to claim 1, which is characterized in that described
Spraying and cleaning apparatus（333）Cleaning solution is sodium carbonate liquor.
4. rubbish loss stench processing system in a kind of garbage transfer station according to claim 1, which is characterized in that described
Deodorization chamber * winding paper（3）Turn hopper including two（34）, described to turn hopper（34）Inside it is horizontally arranged with open dodge gate（341）, institute
State dodge gate（341）It will turn hopper（34）Inside is divided into the feed cavity of top（342）With the discharging chamber of lower section（343）, two institutes
It states and turns hopper（34）It is divided into material feeding box（34a）And feed box（34b）, the material feeding box（34a）Discharging chamber（343）With outer case
（31）One end be tightly connected and its feed cavity（342）Upper end carry feeding seal door（344）, the feed box（34b）'s
Feed cavity（342）With outer case（31）The other end be tightly connected and its discharging chamber（343）Bottom with discharging hermatic door
（345）, the outer case（31）It is interior to carry conveyer belt（315）, the conveyer belt（315）One end be located at material feeding box（34a）'s
Discharging chamber（343）Lower section, the other end are located at feed box（34b）Feed cavity（342）Top, the conveyer belt（315）From charging
Case（34a）To feed box（34b）It transmits in direction.
5. rubbish loss stench processing system in a kind of garbage transfer station according to claim 4, which is characterized in that described
First active wind turbine（2）Opposite second active wind turbine（4）Positioned at it close to material feeding box（34a）Side.
6. rubbish loss stench processing system in a kind of garbage transfer station according to claim 1 or 3, which is characterized in that
The tail gas unit includes circulation ozone concentration detector（62）And circulating fan（63）, the outer housing（61）Including connection
Plasma chamber（611）With ultraviolet room（612）, the low-temperature plasma component（6111）With circulation ozone concentration detector（62）Peace
Loaded on plasma chamber（611）, the ultraviolet lamp（6121）It is installed on ultraviolet room（612）, the circulating fan（63）Connection etc. from
Seed cell（611）And outer case（31）.
7. rubbish loss stench processing system in a kind of garbage transfer station according to claim 3, which is characterized in that described
Ultraviolet generation device（32）By ozone excitation component（321）Part of coming down to a lower group is damaged with ozone（322）Composition, the ozone excitation component
（321）Including several along conveyer belt（315）Direction of transfer is evenly distributed on outer case（31）Internal ultraviolet irradiation lamp（3211）,
The ozone damages part of coming down to a lower group（322）It is arranged in outer case including intensive（31）Close to feed box（34b）The heating tube of side
（3221）.
8. rubbish loss stench processing system in a kind of garbage transfer station according to claim 7, which is characterized in that described
Outer case（31）Quantity is more than one and the two adjacent outer cases（31）Interior air communication, not with the first active wind turbine
（2）The outer case being directly connected to（31）It is close to material feeding box（34a）One end be connected with ozone supplementary device（7）.
9. rubbish loss stench processing system in a kind of garbage transfer station according to claim 8, which is characterized in that adjacent
Two outer cases（31）Communicating position is located at the first rotation wind turbine and damages part of coming down to a lower group with ozone（322）Between side or ozone
Supplementary device（7）Part of coming down to a lower group is damaged with ozone（322）Between side.
10. rubbish loss stench processing system in a kind of garbage transfer station according to claim 1, which is characterized in that packet
Include elevator pump（521）, neutralization precipitation pond（53）And run-off（54）, the elevator pump（521）Connection processing pond（5）And sedimentation basin
（53）, the sedimentation basin（53）And run-off（54）Between pass through overflow plate（55）Separate.
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