CN203591691U - Deodorization device adopting photocatalytic oxidation and biological degradation - Google Patents
Deodorization device adopting photocatalytic oxidation and biological degradation Download PDFInfo
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- CN203591691U CN203591691U CN201320719636.2U CN201320719636U CN203591691U CN 203591691 U CN203591691 U CN 203591691U CN 201320719636 U CN201320719636 U CN 201320719636U CN 203591691 U CN203591691 U CN 203591691U
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- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 23
- 230000003647 oxidation Effects 0.000 title claims abstract description 22
- 230000001699 photocatalysis Effects 0.000 title claims abstract description 22
- 238000004332 deodorization Methods 0.000 title abstract description 8
- 230000015556 catabolic process Effects 0.000 title abstract description 6
- 238000006731 degradation reaction Methods 0.000 title abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 244000005700 microbiome Species 0.000 claims abstract description 7
- 230000003197 catalytic effect Effects 0.000 claims description 27
- 238000006065 biodegradation reaction Methods 0.000 claims description 18
- 238000007146 photocatalysis Methods 0.000 claims description 17
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 14
- 238000001179 sorption measurement Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 8
- 229910021529 ammonia Inorganic materials 0.000 claims description 7
- 230000001877 deodorizing effect Effects 0.000 claims description 7
- 239000002912 waste gas Substances 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000005259 measurement Methods 0.000 claims description 5
- 241000628997 Flos Species 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 239000002028 Biomass Substances 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000012360 testing method Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 20
- 230000000694 effects Effects 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 4
- 239000003205 fragrance Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000010170 biological method Methods 0.000 description 2
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- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
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- 238000013033 photocatalytic degradation reaction Methods 0.000 description 2
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- 238000005406 washing Methods 0.000 description 2
- 206010058467 Lung neoplasm malignant Diseases 0.000 description 1
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- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
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- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
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- 229920002521 macromolecule Polymers 0.000 description 1
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- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
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- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
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- 230000008786 sensory perception of smell Effects 0.000 description 1
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- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a deodorization device adopting photocatalytic oxidation and biological degradation, which comprises a photocatalytic deodorization mechanism and a bio-trickling filter. According to the deodorization device, as the photocatalytic oxidation is combined with the biological degradation, the load is reduced; therefore, the growth of the micro-organism is facilitated; the biological reaction is accelerated by heating gas; the entire staying time is shortened; the deodorization efficiency is improved.
Description
Technical field
The utility model relates to deodorization technology field, is specifically related to a kind of photochemical catalytic oxidation and biodegradation odor removal.
Background technology
Stench is a kind of form of atmosphere pollution, directly acts on people's sense of smell, and contaminated air can cause One's spirits are drooping depressed, the inefficiency of people, and even the incidence of disease of the malignant tumour such as lung cancer is also relevant with room air pollution.Oneself becomes the one in the typical public hazards in seven kinds of the world todays (atmosphere pollution, water pollution, soil pollution, noise pollution, vibration, land subsidence, stench) stench.Within 1993, China has formulated " emission standard for odor pollutants " (GB14554-93), standard is pointed out: odorant pollutant refers to that all stimulate olfactory organ to cause the gaseous matter that people are unhappy and damage living environment, and specifically lists the discharge standard of 9 kinds of odorant pollutants (hydrogen sulfide, methyl mercaptan, first sulphur vinegar, methyl disulfide vinegar, carbon disulfide, ammonia, front three glue, styrene, odor concentration).
On the method for odor treatment is main at present, be to adopt physics, chemistry and biological means, or the combination of this several method.Wherein physical method mainly comprises masking method, absorption process, absorption method, has the advantages such as simple to operate, instant effect.But this method is suitable treatment low concentration, odorant among a small circle only, and cost high, there is secondary pollution; Chemical method mainly comprises chemical washing method, oxidizing process, burning method, has the advantages such as efficiency is high, applied widely, but the method exists the defects such as deodorizing facility investment is high, operating cost is expensive, the duration is short.Biological method is to grow up on the basis of the 50's of 20th century soil deodorization method, and it utilizes the metabolic degradation effect of microorganism, and odorant decomposition and inversion is become to carbon dioxide CO
2, water H
2o, nitrogen N H
3, harmless or few harmful substances such as sulfate.Conventional biological deodorization technique has biofiltration process, biological washing method, bio-trickling method and aeration type bioanalysis.Biological method has the advantages such as processing speed is fast, wide adaptability, non-secondary pollution, but the method there is screening and cultivate bacterial classification difficulty, the defect such as slow takes effect.
Photocatalyst catalytic degradation technology is under photochemical catalyst, to produce electron-hole pair by UV-irradiation, with the H of adsorption
2o and O
2reaction generates the very strong free radical (OH of oxidisability
-) and superoxide ion free radical (O
2 -), can be various organic-inorganic foul gas as class, benzene class, Ammonia, nitrogen oxide, sulfide and other VOC(Volatile Organic Compounds of waking up, volatile organic matter) type organic and inorganic matter be reduced into CO under the effect of photochemical catalytic oxidation
2, H
2o and other nontoxic material.Due in photocatalysis oxidation reaction process without any additive, can not produce secondary pollution, photocatalytic degradation is subject to people's attention gradually.The application of photocatalysis technology aspect odor purification, is mainly the constraint that is subject to activity and efficiency and the photocatalytic coating technology of photochemical catalyst, is difficult to industrialization.
Utility model content
In order to overcome the deficiencies in the prior art, the purpose of this utility model is to provide a kind of photochemical catalytic oxidation and biodegradation odor removal, by photochemical catalytic oxidation and biodegradation combination, cut down load and be conducive to growth of microorganism, heated air is accelerated biological respinse, shorten total residence time, improved odor removal efficient.
For addressing the above problem, the technical scheme that the utility model adopts is as follows:
A kind of photochemical catalytic oxidation and biodegradation odor removal, comprise photocatalysis deodorizing mechanism and bio-trickling filter,
Described photocatalysis deodorizing mechanism comprises reaction chamber, and described reaction chamber bottom is provided with waste gas inlet port, and its top is provided with gas outlet; In reaction chamber, be fixed with respectively from the bottom to top adsorption layer and photocatalysis assembly, adsorption layer and reaction chamber bottom and sidewall form inlet chamber, and top and the sidewall of photocatalysis assembly and reaction chamber form air cavity; Described photocatalysis assembly comprise at least two groups by lower from upper staggered uviol lamp and catalytic module;
Described bio-trickling filter is made up of left chamber, right chamber and torus, and the bottom of left chamber and right chamber is communicated with torus respectively; At the Lower Half filled biomass filler respectively of left chamber and right chamber, top is respectively equipped with spray head; The sidewall of left chamber is provided with the air inlet being communicated with gas outlet, and the top of right chamber is provided with floss hole.
Described in such scheme, in catalytic module, load has titanium deoxide catalyst.Described adsorption layer is active carbon layer.Described biologic packing material is the filler that load has microorganism.
Preferably, photochemical catalytic oxidation described in the utility model and biodegradation odor removal, also comprise online humidity measurement instrument, and online humidity tester test side is connected in reaction chamber.
Preferably, photochemical catalytic oxidation described in the utility model and biodegradation odor removal, also comprise a blower fan, and blower fan one end connects collects airduct, and the other end connects waste gas inlet port by pipeline.
On the basis of such scheme, as one of the present utility model preferred embodiment, on described pipeline, be provided with online H2S detector and online ammonia detector.
In such scheme, preferred embodiment, the area load of described bio-trickling filter is greater than 500m
3/ m
2h.
Compared to existing technology, the beneficial effects of the utility model are: photochemical catalytic oxidation described in the utility model and biodegradation odor removal, after processing, after waste gas, hydrogen sulfide and the ammonia of the gas of discharge are far superior to " emission standard for odor pollutants ", and can keep in stable scope; Whole plant area is little, invests lowly, can be used for the foul smell processing in the places such as sewage pumping station, garbage transfer station, sewage treatment plant, sludge treatment field, feed-processing plant; Total odor removal efficient reaches 99%.
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Accompanying drawing explanation
Fig. 1 is preferred structural representation of the present utility model.
The specific embodiment
As shown in Figure 1, photochemical catalytic oxidation described in the utility model and biodegradation odor removal, comprise photocatalysis deodorizing mechanism 1 and bio-trickling filter 2;
Described photocatalysis deodorizing mechanism comprises reaction chamber, and described reaction chamber bottom is provided with waste gas inlet port, and its top is provided with gas outlet; In reaction chamber, be fixed with respectively from the bottom to top adsorption layer 13 and photocatalysis assembly, adsorption layer 13 forms inlet chamber with reaction chamber bottom and sidewall, and top and the sidewall of photocatalysis assembly and reaction chamber form air cavity; Described photocatalysis assembly comprise at least two groups by lower from upper staggered uviol lamp 11 and catalytic module 12;
Described bio-trickling filter 2 is made up of left chamber, right chamber and torus, and the bottom of left chamber and right chamber is communicated with torus respectively; At the Lower Half filled biomass filler 21 respectively of left chamber and right chamber, top is respectively equipped with spray head 22; The sidewall of left chamber is provided with the air inlet being communicated with gas outlet, and the top of right chamber is provided with floss hole 23.
On the basis of such scheme, in described catalytic module, load has titanium deoxide catalyst.
On the basis of such scheme, in a preferred embodiment, photochemical catalytic oxidation described in the utility model and biodegradation odor removal, also comprise online humidity measurement instrument 4, and online humidity tester detects 4 ends and is connected in reaction chamber.In the time that the humidity of online humidity measurement instrument demonstration is less than 30%, need to starts humidifier and increase the humidity in reaction chamber.
On the basis of such scheme, in another preferred embodiment, photochemical catalytic oxidation described in the utility model and biodegradation odor removal, also comprise a blower fan 3, and blower fan one end connects collects airduct 7, and the other end connects waste gas inlet port by pipeline.
As one of the present utility model preferred embodiment, on described pipeline, be provided with online H2S detector 5 and online ammonia detector 6.
Operation principle of the present utility model is: foul smell is after collecting airduct 7 collections, enter into light-catalyzed reaction mechanism by blower fan 3 pressurizations, online H2S detector 5 and online ammonia detector 6 can on-line monitoring odor concentration situations of change, in reaction chamber, there is photocatalytic degradation in foul smell, having by uviol lamp 11 and load OH free radical or the oxygen radical that the catalytic module 12 of titanium deoxide catalyst produces is little molecule or odorless material by foul smell macromolecules degradation, because uviol lamp 11 also has heat effect, foul smell can greatly improve biodegradable efficiency after preliminary treatment like this, the humidity of online humidity measurement instrument in can on-line monitoring reaction chamber changes, when humidity is enabled humidifier lower than 30% time, guarantee the treatment effect in reaction chamber, in bio-trickling filter 2, can in shorter time, complete foul smell degraded by the microorganism of biologic packing material load, in processing procedure, supplement the required moisture of microorganism by spray head 22, process foul smell up to standard and discharge through floss hole 23.
Above-mentioned embodiment is only preferred embodiment of the present utility model; the scope that can not limit with this utility model protection, the variation of any unsubstantiality that those skilled in the art does on basis of the present utility model and replacement all belong to the utility model scope required for protection.
Claims (7)
1. photochemical catalytic oxidation and a biodegradation odor removal, comprise photocatalysis deodorizing mechanism and bio-trickling filter, it is characterized in that:
Described photocatalysis deodorizing mechanism comprises reaction chamber, and described reaction chamber bottom is provided with waste gas inlet port, and its top is provided with gas outlet; In reaction chamber, be fixed with respectively from the bottom to top adsorption layer and photocatalysis assembly, adsorption layer and reaction chamber bottom and sidewall form inlet chamber, and top and the sidewall of photocatalysis assembly and reaction chamber form air cavity; Described photocatalysis assembly comprise at least two groups by lower from upper staggered uviol lamp and catalytic module;
Described bio-trickling filter is made up of left chamber, right chamber and torus, and the bottom of left chamber and right chamber is communicated with torus respectively; At the Lower Half filled biomass filler respectively of left chamber and right chamber, top is respectively equipped with spray head; The sidewall of left chamber is provided with the air inlet being communicated with gas outlet, and the top of right chamber is provided with floss hole.
2. photochemical catalytic oxidation according to claim 1 and biodegradation odor removal, is characterized in that: in described catalytic module, load has titanium deoxide catalyst.
3. photochemical catalytic oxidation according to claim 1 and biodegradation odor removal, is characterized in that: it also comprises online humidity measurement instrument, and online humidity tester test side is connected in reaction chamber.
4. photochemical catalytic oxidation according to claim 1 and biodegradation odor removal, is characterized in that: it also comprises a blower fan, and blower fan one end connects collects airduct, and the other end connects waste gas inlet port by pipeline.
5. photochemical catalytic oxidation according to claim 4 and biodegradation odor removal, is characterized in that: on described pipeline, be provided with online H2S detector and online ammonia detector.
6. photochemical catalytic oxidation according to claim 1 and biodegradation odor removal, is characterized in that: described adsorption layer is active carbon layer.
7. photochemical catalytic oxidation according to claim 1 and biodegradation odor removal, is characterized in that: described biologic packing material is the filler that load has microorganism.
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CN201320719636.2U CN203591691U (en) | 2013-11-14 | 2013-11-14 | Deodorization device adopting photocatalytic oxidation and biological degradation |
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CN201320719636.2U CN203591691U (en) | 2013-11-14 | 2013-11-14 | Deodorization device adopting photocatalytic oxidation and biological degradation |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103599684A (en) * | 2013-11-14 | 2014-02-26 | 深圳市利源水务设计咨询有限公司 | Photocatalysis oxidization and biological degradation deodorizing device and deodorizing process |
CN105498477A (en) * | 2015-12-09 | 2016-04-20 | 上海市政工程设计研究总院(集团)有限公司 | Method for treating high-concentration odor |
CN105833687A (en) * | 2016-04-29 | 2016-08-10 | 广东工业大学 | Deodorizing device |
CN108126471A (en) * | 2016-12-01 | 2018-06-08 | 上海惠志环保科技有限公司 | The concentration photodissociation bioremediation of VOCs exhaust gas |
CN108554023A (en) * | 2018-05-21 | 2018-09-21 | 台州创投环保科技有限公司 | A kind of device that gas with foreign flavor is purified using composite microbial bacteria |
CN113578011A (en) * | 2021-08-26 | 2021-11-02 | 济南大学 | Constant-temperature efficient oxidative biodegradation coupling gas purification system and method |
-
2013
- 2013-11-14 CN CN201320719636.2U patent/CN203591691U/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103599684A (en) * | 2013-11-14 | 2014-02-26 | 深圳市利源水务设计咨询有限公司 | Photocatalysis oxidization and biological degradation deodorizing device and deodorizing process |
CN105498477A (en) * | 2015-12-09 | 2016-04-20 | 上海市政工程设计研究总院(集团)有限公司 | Method for treating high-concentration odor |
CN105498477B (en) * | 2015-12-09 | 2018-04-10 | 上海市政工程设计研究总院(集团)有限公司 | A kind of method suitable for high concentration Odor control |
CN105833687A (en) * | 2016-04-29 | 2016-08-10 | 广东工业大学 | Deodorizing device |
CN108126471A (en) * | 2016-12-01 | 2018-06-08 | 上海惠志环保科技有限公司 | The concentration photodissociation bioremediation of VOCs exhaust gas |
CN108554023A (en) * | 2018-05-21 | 2018-09-21 | 台州创投环保科技有限公司 | A kind of device that gas with foreign flavor is purified using composite microbial bacteria |
CN108554023B (en) * | 2018-05-21 | 2020-05-22 | 王攀 | Device capable of purifying peculiar smell gas by utilizing compound microorganism bacteria |
CN113578011A (en) * | 2021-08-26 | 2021-11-02 | 济南大学 | Constant-temperature efficient oxidative biodegradation coupling gas purification system and method |
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