CN106215687A - Biofilter odor treating device and method - Google Patents
Biofilter odor treating device and method Download PDFInfo
- Publication number
- CN106215687A CN106215687A CN201610671415.0A CN201610671415A CN106215687A CN 106215687 A CN106215687 A CN 106215687A CN 201610671415 A CN201610671415 A CN 201610671415A CN 106215687 A CN106215687 A CN 106215687A
- Authority
- CN
- China
- Prior art keywords
- biofilter
- water
- air
- spray column
- spray
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
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
- B01D53/84—Biological processes
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/90—Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
-
- 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)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Molecular Biology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
nullThe present invention relates to odor treatment device technical field，A kind of rational in infrastructure、Working stability、Biofilter odor treating device that treatment effeciency is high and method，It is characterized in that being provided with spray column、Biofilter、Anaerobic reation pool、Aerobic reaction pond、Air-dissolving air-float mechanism、Cooling tower、Tank，The most pending foul smell sends into spray column through air inlet pipe，Water in tank enters spray column through water inlet pipe，Gas after process enters biofilter through spray column top，The liquid that biofilter and spray column are discharged is sequentially sent to anaerobic reation pool、Aerobic reaction pond carries out biochemical treatment，Discharge water in aerobic reaction pond completes solid-liquid separation through air-dissolving air-float mechanism，Water sends into tank，The present invention is compared with prior art，Can effectively remove the odorant in gas，Reduce human body and the density of infection of environment，There is treatment effeciency high、Stable and reliable operation、The significantly advantage such as non-secondary pollution discharge.
Description
Technical field
The present invention relates to odor treatment device technical field, a kind of rational in infrastructure, working stability, process effect
Biofilter odor treating device that rate is high and method.
Background technology
Foul smell makes people's spirit dysphoria, absent-minded, and work efficiency reduces, it is judged that unable to do what one wishes, hypomnesis,
Affect the thinking activities of brain.Stench is serious, to respiratory system, blood circulation, digestive system, endocrine system to the harm of human body
System and nervous system etc. adversely affect.Rising after blood pressure being made to occur falling before such as pungent odors such as ammonia, pulse are first
The phenomenon accelerated after slowing down.Often in contact with stench, people's anorexia can be made, feel sick, even vomit, and then develop into digestive function and subtract
Move back.Stimulated by a kind of several low concentration odorants for a long time, the obstacle such as anosmia, olfactory fatigue can be caused.Stench makes
Cranial nerve is constantly upset and damages.
Process foul smell technology and have the operation experience of decades, along with raising and the environmental protection of domestic economy level
The reinforcement of consciousness, is the most just starting to rise and in moving towards flourishing trend.At present, main process foul smell technology
Active carbon adsorption, thermal oxidation method, oxonium ion group process foul smell method, chemical washing method, Biological fitler method etc., wherein adsorb
Desorption processes: activated carbon is the most traditional material processing organic exhaust gas, and it has good absorption and makees part VOCs
With, and can be with desorption and regeneration.But it is high that subject matter is operating cost, and after-treatment bothers.For fish meal factory, it is not appropriate for
Use this method.Reason is: molecular weight is less than 45 and the high material volatilized stably should not be adsorbed by activated carbon, substantially due to fish
Powder factory waste gas is not suitable for, with the material of activated carbon adsorption, using activated carbon adsorption to be difficult to up to standard containing ammonia, hydrogen sulfide, amine etc..
Organic gas in catalysis combustion catalysis burning decomposable asymmetric choice net waste gas, is degraded into carbon dioxide and water.But it is big that subject matter is energy consumption,
The treatment operating costs generally burned is more than 6 times of activated carbon operating cost, is the 15 ~ 20 of biological treatment foul smell method
Times.Odorant pollutant in waste gas, by oxides such as chlorine, chlorine dioxide, ozone, is aoxidized and degrades by chemical oxidation.Main
Wanting the problem to be: (1) consumes a large amount of chemical agent, operating cost is high；(2) strong oxidizer, corrosive equipment, equipment investment are used
Costly.Biological fitler method biofiltration technique have employed liquid and absorbs and the compound action of biological treatment.First foul smell is filled out
Material absorption and sorption, foul smell is absorbed by microorganism as nutrient substance, metabolism and utilization, is degraded into by odor pollution thing simultaneously
Water and carbon dioxide.Biofiltration processes foul smell technique, has non-secondary pollution, and operating cost is low, it is simple to the advantages such as maintenance.
Summary of the invention
The present invention is directed to shortcoming and defect present in prior art, it is proposed that a kind of reliable operation, treatment effeciency are high
Biofilter odor treating device and method.
The present invention can be reached by following measures:
A kind of biofilter odor treating device, it is characterised in that be provided with spray column, biofilter, anaerobic reation pool, aerobic instead
Ying Chi, air-dissolving air-float mechanism, cooling tower, tank, the most pending foul smell sends into spray column through air inlet pipe, the water in tank
Entering spray column through water inlet pipe, the gas after process enters biofilter, biofilter and spray column row through spray column top
The liquid gone out is sequentially sent to anaerobic reation pool, aerobic reaction pond carries out biochemical treatment, and the discharge water in aerobic reaction pond is through molten
Gas air supporting mechanism completes solid-liquid separation, and water sends into tank.
In the present invention, spray column is internal containing ceramic packing, and spray liquid, from circulating water pool, enters spray to filling out from tower top
On material, gas enters from the bottom of tower, is discharged into biofilter from top；Described ceramic packing uses the ceramic ripple being parallel to each other
Sheet superposition, forms the corrugated plate packing module that thickness is 5cm, can use many group corrugated plate packing modules.
In the present invention, the side of biofilter is provided with air inlet, and middle part is provided with packing layer, and bottom is collection conduit and domatic,
The side relative with air inlet is provided with gas outlet, and top is provided with water spray and waters mechanism, is provided with humidity, temperature, PH in packing layer
Sensor, controls pump and water pipe by control system, it is ensured that properly functioning.
Biofilter of the present invention is to calculate according to total foul smell capacity hourly, and two groups in parallel, can modularity
Manufacture, spelling group.
Being provided with the dividing plate for supporting biologic packing material in biofilter of the present invention, aperture is at 8MM-12MM.
Biologic packing material of the present invention is compounded mix, be organic filler and inert filler 1: 1 mixing post blend by volume and
Becoming, filler forms pH value buffer environment by collocation, and pH value controls between 6-8.
Inorganic filler in biologic packing material of the present invention has and is not limited to activated carbon, lava stone, zeolite, perlite, Vermiculitum, pottery
Grain and silicate bead and city solid waste garbage compost and plastic flakes (1.5cm × 1.0cm)
Organic filler in the present invention is divided into natural organic filler and synthetic macromolecule organic filler, has and is not limited to heap
Natural or after artificial suitably process the filler such as fertilizer, wood flour, bamboo charcoal, bagasse, cocoanut fiber, bark and corn cob.
Anaerobic reation pool of the present invention uses biological fluidized bed design, interior input K1 type HDPE environmental-friendly biological stuffing, is provided with latent
Water mixing pump, outlet uses the rustless steel grid of aperture 8MM.
Aerobic reaction pond of the present invention is designed for biological fluidized bed, interior input K1 type HDPE environmental-friendly biological stuffing, is provided with employing
The disk aerator of 150MM-250MM diameter, spacing 0.5M, outlet outlet uses the rustless steel grid of aperture 8MM.
Zhong Fuqi of the present invention air supporting mechanism includes flotation tank, water pump, pneumatics tank, air compressor machine.
The invention allows for a kind of biofilter odor treatment method, it is characterised in that foul smell first passes through spray column, spray
Drenching tower and include ceramic packing layer, be beneficial to contact mass transfer between gas-liquid two-phase, spray liquid is from circulating water pool, from tower top through spraying
On filler, and flowing down along filling surface, gas is sent into from the bottom of tower, after gas location mode is distributed, with liquid in adverse current continuously
By the space of packing layer, it is discharged into subsequent bio filter tank from top, foul smell of degrading further；Spray scrubber spray liquid is inhaled
After receiving the pollutant in waste gas, enter hypoxia response pond and aerobic reaction tank, microbial biochemical reaction in reaction tank, pollute
Thing is degraded, and after wastewater biochemical processes, through dissolved-air air-float method, it is achieved solid-liquid separation, the water after separation is transported to cold
But tower, flows back to tank after cooling, recycle.
After in the present invention, spray scrubber is to foul waste gas pretreatment, residue foul smell is humidified, homoiothermic, dedusting, then use
Air exhauster will be delivered to biofilter and processes, after foul gas enters biofilter module, through absorption, the suction of packing microbial
Receive and degraded, after being removed by foul smell composition, enter air.
Pouring water in biofilter in the present invention, uses factory's reuse water, recycles, and not outer row, biofilter is adopted
With modularized design, can be with superposition, to save space.
The present invention compared with prior art, can effectively remove the odorant in gas, reduces human body and environment
Density of infection, has the significantly advantage such as treatment effeciency height, stable and reliable operation, non-secondary pollution discharge.
Accompanying drawing illustrates:
Accompanying drawing 1 is the structural representation of the present invention.
Reference: spray column 1, biofilter 2, anaerobic reation pool 3, aerobic reaction pond 4, air-dissolving air-float mechanism 5, cooling
Tower 6, tank 7, gas outlet 8, water spray pouring mechanism 9, submersible stirring pump 10, rustless steel grid 11, disk aerator 12.
Detailed description of the invention:
The present invention is further illustrated below in conjunction with the accompanying drawings.
As shown in drawings, the present invention proposes a kind of biofilter odor treating device, it is characterised in that be provided with spray column
1, biofilter 2, anaerobic reation pool 3, aerobic reaction pond 4, air-dissolving air-float mechanism 5, cooling tower 6, tank 7, the most pending
Foul smell sends into spray column 1 through air inlet pipe, and the water in tank 7 enters spray column 1 through water inlet pipe, and the gas after process is through spray column
1 top enters biofilter 2, the liquid that biofilter 2 and spray column 1 are discharged be sequentially sent to anaerobic reation pool 3, aerobic instead
Answering pond 4 to carry out biochemical treatment, the discharge water in aerobic reaction pond 3 completes solid-liquid separation through air-dissolving air-float mechanism 5, and water sends into water storage
Pond.
In the present invention, spray column 1 is internal containing ceramic packing, and spray liquid, from circulating water pool, enters spray to filling out from tower top
On material, gas enters from the bottom of tower, is discharged into biofilter from top；Described ceramic packing uses the ceramic ripple being parallel to each other
Sheet superposition, forms the corrugated plate packing module that thickness is 5cm, can use many group corrugated plate packing modules.
In the present invention, the side of biofilter 2 is provided with air inlet, and middle part is provided with packing layer, and bottom is collection conduit and slope
Face, top is provided with gas outlet 8, and top is provided with water spray and waters mechanism 9, is provided with humidity, temperature, PH sensor in packing layer, logical
Cross control system and control pump and water pipe, it is ensured that be properly functioning.
Biofilter 2 of the present invention is to calculate according to total foul smell capacity hourly, and two groups in parallel, can modularity
Manufacture, spelling group.
Being provided with the dividing plate for supporting biologic packing material in biofilter of the present invention, aperture is at 8MM-12MM.
Biologic packing material of the present invention is compounded mix, be organic filler and inert filler 1: 1 mixing post blend by volume and
Becoming, filler forms pH value buffer environment by collocation, and pH value controls between 6-8.
Inorganic filler in biologic packing material of the present invention has and is not limited to activated carbon, lava stone, zeolite, perlite, Vermiculitum, pottery
Grain and silicate bead and city solid waste garbage compost and plastic flakes (1.5cm × 1.0cm)
Organic filler in the present invention is divided into natural organic filler and synthetic macromolecule organic filler, has and is not limited to heap
Natural or after artificial suitably process the filler such as fertilizer, wood flour, bamboo charcoal, bagasse, cocoanut fiber, bark and corn cob.
Anaerobic reation pool of the present invention uses biological fluidized bed design, interior input K1 type HDPE environmental-friendly biological stuffing, is provided with latent
Water mixing pump 10, outlet uses the rustless steel grid 11 of aperture 8MM.
Aerobic reaction pond of the present invention is designed for biological fluidized bed, interior input K1 type HDPE environmental-friendly biological stuffing, is provided with employing
The disk aerator 12 of 150MM-250MM diameter, spacing 0.5M, outlet outlet uses the rustless steel grid 11 of aperture 8MM.
Zhong Fuqi of the present invention air supporting mechanism includes flotation tank, water pump, pneumatics tank, air compressor machine.
The invention allows for a kind of biofilter odor treatment method, it is characterised in that foul smell first passes through spray column, spray
Drenching tower and include ceramic packing layer, be beneficial to contact mass transfer between gas-liquid two-phase, spray liquid is from circulating water pool, from tower top through spraying
On filler, and flowing down along filling surface, gas is sent into from the bottom of tower, after gas location mode is distributed, with liquid in adverse current continuously
By the space of packing layer, it is discharged into subsequent bio filter tank from top, foul smell of degrading further；Spray scrubber spray liquid is inhaled
After receiving the pollutant in waste gas, enter hypoxia response pond and aerobic reaction tank, microbial biochemical reaction in reaction tank, pollute
Thing is degraded, and after wastewater biochemical processes, through dissolved-air air-float method, it is achieved solid-liquid separation, the water after separation is transported to cold
But tower, flows back to tank after cooling, recycle.
After in the present invention, spray scrubber is to foul waste gas pretreatment, residue foul smell is humidified, homoiothermic, dedusting, then use
Air exhauster will be delivered to biofilter and processes, after foul gas enters biofilter module, through absorption, the suction of packing microbial
Receive and degraded, after being removed by foul smell composition, enter air.
Pouring water in biofilter in the present invention, uses factory's reuse water, recycles, and not outer row, biofilter is adopted
With modularized design, can be with superposition, to save space.
The present invention compared with prior art, can effectively remove the odorant in gas, reduces human body and environment
Density of infection, has the significantly advantage such as treatment effeciency height, stable and reliable operation, non-secondary pollution discharge.
Claims (9)
1. a biofilter odor treating device, it is characterised in that be provided with spray column, biofilter, anaerobic reation pool, aerobic
Reaction tank, air-dissolving air-float mechanism, cooling tower, tank, the most pending foul smell sends into spray column through air inlet pipe, in tank
Water enters spray column through water inlet pipe, and the gas after process enters biofilter, biofilter and spray column through spray column top
The liquid discharged is sequentially sent to anaerobic reation pool, aerobic reaction pond carries out biochemical treatment, the discharge water warp in aerobic reaction pond
Air-dissolving air-float mechanism completes solid-liquid separation, and water sends into tank.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that spray column is internal containing pottery
Porcelain filling, spray liquid from circulating water pool, enters spray to filler from tower top, and gas enters from the bottom of tower, discharge from top into
Enter biofilter；Described ceramic packing uses the ceramic corrugated plate superposition being parallel to each other, and forms the corrugated plate packing that thickness is 5cm
Module, is provided with corrugated plate packing module more than two in spray column.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that the side of biofilter sets
Having air inlet, middle part to be provided with packing layer, bottom is collection conduit and domatic, and the side relative with air inlet is provided with gas outlet, top
Portion is provided with water spray and waters mechanism, is provided with humidity, temperature, PH sensor in packing layer, controls pump and moisturizing by control system
Pipeline, it is ensured that properly functioning；Described biofilter is provided with many groups and is used in series.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that set in described biofilter
Having the dividing plate for supporting biologic packing material, aperture is at 8MM-12MM；Described biologic packing material is compounded mix, is organic filler and lazy
Property filler by volume 1: 1 mixing post blend form, filler by collocation formed pH value buffer environment, pH value control to 6-8 it
Between；Inorganic filler in biologic packing material has and is not limited to activated carbon, lava stone, zeolite, perlite, Vermiculitum, haydite and silicate
Bead and city solid waste garbage compost and plastic flakes, size is 1.5cm × 1.0cm, and organic filler is divided into natural organic fill out
Material and synthetic macromolecule organic filler, have and be not limited to compost, wood flour, bamboo charcoal, bagasse, cocoanut fiber, bark and jade
Natural or after artificial suitably process the filler such as meter Xin.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that anaerobic reation pool uses raw
Fluidized beds designs, interior input K1 type HDPE environmental-friendly biological stuffing, is provided with submersible stirring pump, and outlet uses aperture 8MM not
Rust steel grating.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that aerobic reaction pond is biological
Design of Fluidized bed, interior input K1 type HDPE environmental-friendly biological stuffing, it is provided with the disk aerator using 150MM-250MM diameter,
Away from 0.5M, outlet outlet uses the rustless steel grid of aperture 8MM.
A kind of biofilter the most according to claim 1 odor treating device, it is characterised in that Fu Qi air supporting mechanism includes
Flotation tank, water pump, pneumatics tank, air compressor machine.
8. a biofilter odor treatment method, it is characterised in that foul smell first passes through spray column, spray column includes ceramic packing
Layer, is beneficial to contact mass transfer between gas-liquid two-phase, and spray liquid is from circulating water pool, from tower top through spray to filler, and along filler
Surface flows down, and gas is sent into from the bottom of tower, after gas location mode is distributed, with liquid in the sky countercurrently continuing through packing layer
Gap, is discharged into subsequent bio filter tank from top, foul smell of degrading further；Spray scrubber spray liquid absorbs the pollution in waste gas
After thing, entering hypoxia response pond and aerobic reaction tank, microbial biochemical reaction in reaction tank, pollutant are degraded, useless
After water biochemical treatment, through dissolved-air air-float method, it is achieved solid-liquid separation, the water after separation is transported to cooling tower, flows after cooling
Return tank, recycle.
A kind of biofilter the most according to claim 8 odor treatment method, it is characterised in that spray scrubber is to stench
After waste gas pretreatment, residue foul smell humidify, homoiothermic, dedusting, then with air exhauster will be delivered to biofilter process, effluvium
After body enters biofilter module, through packing microbial absorption, absorb and degrade, after foul smell composition is removed, enter greatly
Gas；Biofilter pouring water, uses factory's reuse water, recycles, not outer row, and biofilter uses modularized design,
Can be with superposition, to save space.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610671415.0A CN106215687A (en) | 2016-08-16 | 2016-08-16 | Biofilter odor treating device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610671415.0A CN106215687A (en) | 2016-08-16 | 2016-08-16 | Biofilter odor treating device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106215687A true CN106215687A (en) | 2016-12-14 |
Family
ID=57547573
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610671415.0A Pending CN106215687A (en) | 2016-08-16 | 2016-08-16 | Biofilter odor treating device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106215687A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107215946A (en) * | 2017-05-23 | 2017-09-29 | 江苏和顺环保有限公司 | Miniature water process ozone reaction unit |
| CN107285568A (en) * | 2017-07-24 | 2017-10-24 | 浙江富阳华天纸业有限公司 | A kind of pulping wastewater treatment method of low foul smell discharge |
| CN107486129A (en) * | 2017-08-31 | 2017-12-19 | 安徽青花坊瓷业股份有限公司 | A kind of ceramic corrugated filler structure of scrubbing tower |
| CN107551800A (en) * | 2017-10-10 | 2018-01-09 | 百环境投资江苏有限公司 | A kind of stench processing system |
| CN107596906A (en) * | 2017-10-10 | 2018-01-19 | 百环境投资江苏有限公司 | A kind of stench processing system |
| CN108079769A (en) * | 2017-12-21 | 2018-05-29 | 广州百海工程机械有限公司 | Exhaust gas spray cleaning device and deodoration system |
| CN109621700A (en) * | 2018-10-26 | 2019-04-16 | 中国联合工程有限公司 | A kind of bacteria filter system and its working method handling garbage odor |
| CN112007506A (en) * | 2020-08-28 | 2020-12-01 | 成都达源环保工程有限公司 | Pharmaceutical chemical sewage and organic waste gas combined biological treatment method |
| CN112807987A (en) * | 2021-01-15 | 2021-05-18 | 郑州市污水净化有限公司 | Deodorization system and method for improving municipal sludge heat drying tail gas treatment effect |
| CN112915775A (en) * | 2021-04-06 | 2021-06-08 | 广东省南方环保生物科技有限公司 | Sludge drying odor treatment method and device |
| CN112999861A (en) * | 2021-03-12 | 2021-06-22 | 产学研(广州)环境服务有限公司 | High-efficient circulation regeneration microbial degradation VOCs device |
| CN114349283A (en) * | 2022-01-12 | 2022-04-15 | 沈阳师范大学 | Rural domestic sewage purification device and sewage purification method based on biodegradation |
| CN115212679A (en) * | 2022-07-25 | 2022-10-21 | 广东工业大学 | Ammonia-containing odor gas and washing liquid recycling system and method based on anaerobic ammonia oxidation |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204752412U (en) * | 2015-06-25 | 2015-11-11 | 安庆市虹泰新材料有限责任公司 | Industrial waste water , waste gas treatment system |
| CN105289231A (en) * | 2015-10-19 | 2016-02-03 | 江苏奥琳斯邦热能设备有限公司 | Waste gas treatment system |
-
2016
- 2016-08-16 CN CN201610671415.0A patent/CN106215687A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204752412U (en) * | 2015-06-25 | 2015-11-11 | 安庆市虹泰新材料有限责任公司 | Industrial waste water , waste gas treatment system |
| CN105289231A (en) * | 2015-10-19 | 2016-02-03 | 江苏奥琳斯邦热能设备有限公司 | Waste gas treatment system |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107215946A (en) * | 2017-05-23 | 2017-09-29 | 江苏和顺环保有限公司 | Miniature water process ozone reaction unit |
| CN107285568A (en) * | 2017-07-24 | 2017-10-24 | 浙江富阳华天纸业有限公司 | A kind of pulping wastewater treatment method of low foul smell discharge |
| CN107486129A (en) * | 2017-08-31 | 2017-12-19 | 安徽青花坊瓷业股份有限公司 | A kind of ceramic corrugated filler structure of scrubbing tower |
| CN107551800A (en) * | 2017-10-10 | 2018-01-09 | 百环境投资江苏有限公司 | A kind of stench processing system |
| CN107596906A (en) * | 2017-10-10 | 2018-01-19 | 百环境投资江苏有限公司 | A kind of stench processing system |
| CN108079769A (en) * | 2017-12-21 | 2018-05-29 | 广州百海工程机械有限公司 | Exhaust gas spray cleaning device and deodoration system |
| CN109621700A (en) * | 2018-10-26 | 2019-04-16 | 中国联合工程有限公司 | A kind of bacteria filter system and its working method handling garbage odor |
| CN112007506A (en) * | 2020-08-28 | 2020-12-01 | 成都达源环保工程有限公司 | Pharmaceutical chemical sewage and organic waste gas combined biological treatment method |
| CN112807987A (en) * | 2021-01-15 | 2021-05-18 | 郑州市污水净化有限公司 | Deodorization system and method for improving municipal sludge heat drying tail gas treatment effect |
| CN112999861A (en) * | 2021-03-12 | 2021-06-22 | 产学研(广州)环境服务有限公司 | High-efficient circulation regeneration microbial degradation VOCs device |
| CN112915775A (en) * | 2021-04-06 | 2021-06-08 | 广东省南方环保生物科技有限公司 | Sludge drying odor treatment method and device |
| CN112915775B (en) * | 2021-04-06 | 2022-11-29 | 广东省南方环保生物科技有限公司 | Sludge drying odor treatment method and device |
| CN114349283A (en) * | 2022-01-12 | 2022-04-15 | 沈阳师范大学 | Rural domestic sewage purification device and sewage purification method based on biodegradation |
| CN115212679A (en) * | 2022-07-25 | 2022-10-21 | 广东工业大学 | Ammonia-containing odor gas and washing liquid recycling system and method based on anaerobic ammonia oxidation |
| CN115212679B (en) * | 2022-07-25 | 2023-09-22 | 广东工业大学 | Ammonia-containing odor based on anaerobic ammonia oxidation and washing liquid circulation regeneration system and method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106215687A (en) | Biofilter odor treating device and method | |
| CN108854355A (en) | A kind of system and method for sewage treatment plant's foul smell Collecting and dealing | |
| CN203342649U (en) | Combined type integrated deodorization equipment | |
| CN204429097U (en) | A kind of biofilter odor purification system | |
| CN202497818U (en) | Multi-level comprehensive treatment system for foul gas | |
| CN104874285A (en) | Composite biological deodorizing system and method for processing large amount high density stink | |
| CN200995119Y (en) | Dust-collecting deodorization purifier by multifunctional combined method | |
| CN104147921B (en) | A kind of apparatus and method of the activated carbon combined method processing foul gas of biofiltration | |
| CN101011591A (en) | Method and apparatus for treating malodorous gas by using composite microorganism and nano composite carrier | |
| CN201940172U (en) | Biological formaldehyde purifier | |
| CN103611416B (en) | The odor removal of reciprocating living beings filter bed composite alkali liquor | |
| CN104001421A (en) | Composite biological deodorizing process and apparatus using bubbleless aeration pretreatment | |
| CN111530270A (en) | Efficient biological treatment device and treatment method for waste gas | |
| CN205796953U (en) | A kind of biological deodorizing tower | |
| CN202478818U (en) | Novel biological trickling filtering tower for decomposing organic odor | |
| CN109078479A (en) | A kind of compound bio method processing sewage plant exhaust device and waste gas processing method | |
| CN101332403B (en) | Compound soil odor purification filter bed | |
| CN101940874B (en) | Biofilter tower exhaust gas purification system | |
| CN208893851U (en) | A kind of system of sewage treatment plant's foul smell Collecting and dealing | |
| CN104147919A (en) | Low pH waste gas biological purification reactor and waste gas treatment process | |
| CN216630325U (en) | Biological filter column deodorization system for efficient deodorization | |
| CN105084654A (en) | Sewage deodorization method | |
| CN101612521A (en) | A kind of ecological odor biodegradation purifying device | |
| CN104609539A (en) | Sewage-farm aeration tank effluent gas processing method | |
| CN210620387U (en) | Double-effect nitrogen and phosphorus removal device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161214 |