CN108483645A - A kind for the treatment of sewage by using biological membrane method and its technique - Google Patents
A kind for the treatment of sewage by using biological membrane method and its technique Download PDFInfo
- Publication number
- CN108483645A CN108483645A CN201810274858.5A CN201810274858A CN108483645A CN 108483645 A CN108483645 A CN 108483645A CN 201810274858 A CN201810274858 A CN 201810274858A CN 108483645 A CN108483645 A CN 108483645A
- Authority
- CN
- China
- Prior art keywords
- layer
- sewage
- bacterium
- metazoa
- primary sound
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
Abstract
The invention discloses a kind for the treatment of sewage by using biological membrane method and its technique, biomembrane is made of anaerobic layer, aerobic layer, carrier and filter material layer, and sewage degradation step is as follows:Step 1:Biofilm:Bacterium, organic pollution, primary sound animal and metazoa is prevented to pass through biomembrane;Step 2:Absorption:Adsorption layer is made of working lining and supporting layer, is first adsorbed to bacterium, organic pollution, primary sound animal and metazoa, and adsorption layer kills bacterium, primary sound animal and metazoa after absorption, forms it into waste material layer;Step 3:Demoulding:It is cooperated by internal cause and external cause, bacterium, organic pollution, primary sound animal and the metazoa after being killed on adsorption layer is cleared up.The treating sewage by using biological membrane method and its technique are embedded in the cell in biomembrane due to population effect, have stronger antitoxin sexuality, the antitoxin sexuality of specific ionization cell is eager to excel 50~500 times, therefore biomembrane changes with stronger adaptability water quality.
Description
Technical field
The present invention relates to sewage water treatment method technical field, specially a kind for the treatment of sewage by using biological membrane method and its technique.
Background technology
Biofilm is a kind of waste water aerobic biologic treating technique side by side with activated sludge process, is a kind of fixed embrane method,
It is the manual of sewage self-purification of water process and reinforcing, mainly removes deliquescent in waste water and colloidal organic pollution.
Traditional cannot effectively improve the population effect of cell in biomembrane, therefore reduce the poison resistance of free cell, and
Traditional biomembrane cannot effectively reduce the content of sludge in sewage after treated sewage, improve Treatment of Sludge intensity.
Invention content
The purpose of the present invention is to provide a kind for the treatment of sewage by using biological membrane method and its techniques, are lacked with solving existing technology
It falls into and inaccessiable technology requires.
To achieve the above object, the present invention provides the following technical solutions:A kind for the treatment of sewage by using biological membrane method and its technique,
Biomembrane is made of anaerobic layer, aerobic layer, carrier and filter material layer, and sewage degradation step is as follows:Step 1:Biofilm:Prevention bacterium,
Organic pollution, primary sound animal and metazoa pass through biomembrane;Step 2:Absorption:Adsorption layer is by working lining and supporting layer group
At first being adsorbed to bacterium, organic pollution, primary sound animal and metazoa, adsorption layer is dynamic to bacterium, primary sound after absorption
Object and metazoa are killed, and waste material layer is formed it into;Step 3:Demoulding:It is cooperated by internal cause and external cause, to adsorption layer
On kill after bacterium, organic pollution, primary sound animal and metazoa cleared up.
Preferably, after the sewage flows through biomembrane, filler is mutually mixed by cobble, clinker and coke granule and is formed, ovum
The microorganism of stone, clinker and a coke absorption part, microorganism largely breed in cobble, clinker and coke surface, gradual shape
One is formed at one layer of satiny mucus shape film layer, and then to bacterium, organic pollution, primary sound animal and the metazoa in sewage
Layer barrier, can only be such that its hydrone passes through.
Preferably, the adsorption layer overall thickness is set as 1.8~2.0m, and work layer thickness is 1.3~1.6m, grain size between
Between 25~40mm, support layer thickness is 0.2m, and between 70~80mm, adsorption layer constantly thickeies grain size, generates layering, is inhaled
Attached layer surface is aerobic microbiological, and inside is no oxygen animalcule, and aerobic microbiological carries out organic pollution to resolve into inorganic matter,
The nutrient in water is reduced, for mucus shape film layer to bacterium, primary sound animal and metazoa, no oxygen animalcule, bacterium, primary sound are dynamic
Object and metazoa largely consume the nutrition inside adsorption layer, and bacterium, primary sound animal and metazoa voluntarily inactivate.
Preferably, the microorganism of the biological film inner layer cannot get sufficient nutrition and enter endogenous metabolism, form it into
Waste material layer;Microorganism loses the adhesive capacity between adsorption layer not in secreting mucus matter, gas of the waste material layer in sewage
Under the action of bubble disturbance and hydraulic shear so that blocked up waste material layer is detached from carrier, and absorption surface can rapidly have been grown newly
Waste material layer continues to purify sewage.
Preferably, it is discharged one end water sampling through biomembrane for described pair, is detected in water using COD ammonia nitrogen total phosphorus tachymeters
The content of COD, the content to judge the organic matter in water outlet judge whether sewage disposal reaches whether within critical field
Mark.
Compared with prior art, beneficial effects of the present invention are as follows:
1. adaptable:The cell in biomembrane is embedded in due to population effect, has stronger antitoxin sexuality, specific ionization thin
The antitoxin sexuality of born of the same parents is eager to excel 50~500 times, therefore biomembrane changes with stronger adaptability water quality.
2. the aerobic decomposable process for supporting bacterium well of absorption layer surface can be divided into two stages:First stage mainly will
Organic matter is converted into CO2、H2O、NH3Deng;Second stage, mainly NH3It is converted into NO2And NO3, with aerobic method treated sewage,
Peculiar smell in water removal can drop, and it is shorter to handle required time.
3. microorganism treatment dirt-removing power is up to 90% or more, water quality that treated is good, and the COD in water is total by COD ammonia nitrogens
Phosphorus tachymeter detects, and the COD in water is significantly reduced, and can be exhausted directly in the Nature.
Specific implementation mode
Below in conjunction with the present invention, technical scheme in the embodiment of the invention is clearly and completely described, it is clear that
Described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based on the implementation in the present invention
Example, every other embodiment obtained by those of ordinary skill in the art without making creative efforts belong to
The scope of protection of the invention.
The present invention provides a kind of technical solution:A kind for the treatment of sewage by using biological membrane method and its technique, biomembrane by anaerobic layer,
Aerobic layer, carrier and filter material layer composition, sewage degradation step are as follows:Step 1:Biofilm:Prevent bacterium, organic pollution, primary sound
Animal and metazoa pass through biomembrane;Step 2:Absorption:Adsorption layer is made of working lining and supporting layer, first to bacterium, organic
Pollutant, primary sound animal and metazoa are adsorbed, and adsorption layer carries out bacterium, primary sound animal and metazoa after absorption
It kills, forms it into waste material layer;Step 3:Demoulding:Cooperated by internal cause and external cause, to after being killed on adsorption layer bacterium,
Organic pollution, primary sound animal and metazoa are cleared up.
After sewage flows through biomembrane, filler is mutually mixed by cobble, clinker and coke granule and is formed, cobble, clinker and coke
The microorganism of a charcoal absorption part, microorganism largely breeds in cobble, clinker and coke surface, gradually form one layer it is satiny
Mucus shape film layer, and then one layer of barrier is formed to bacterium, organic pollution, primary sound animal and the metazoa in sewage, it can only
Its hydrone is set to pass through.
Adsorption layer overall thickness is set as 1.8~2.0m, and work layer thickness is 1.3~1.6m, grain size between 25~40mm,
Support layer thickness is 0.2m, and between 70~80mm, adsorption layer constantly thickeies grain size, generates layering, absorption layer surface is preferably
Oxygen animalcule, inside are no oxygen animalcule, and aerobic microbiological carries out organic pollution to resolve into inorganic matter, reduces the battalion in water
Element is supported, mucus shape film layer is to bacterium, primary sound animal and metazoa, no oxygen animalcule, bacterium, primary sound animal and metazoa
Nutrition inside a large amount of consumption adsorption layers, bacterium, primary sound animal and metazoa voluntarily inactivate.
The microorganism of biological film inner layer cannot get sufficient nutrition and enter endogenous metabolism, form it into waste material layer;Micro- life
Object loses the adhesive capacity between adsorption layer not in secreting mucus matter, bubble disturbance and water of the waste material layer in sewage
Under the action of power shearing force so that blocked up waste material layer is detached from carrier, and absorption surface, which can rapidly grow new waste material layer, to be continued
Sewage is purified.
It is discharged one end water sampling to penetrating biomembrane, the content of the COD in water is detected using COD ammonia nitrogen total phosphorus tachymeters,
Content to judge the organic matter in water outlet judges whether sewage disposal is up to standard whether within critical field.
A kind for the treatment of sewage by using biological membrane method of the present invention and its technique, first make biomembrane, then biomembrane reeve is handled
Chi Zhong is passed through sewage, and the anaerobic layer, aerobic layer, carrier and filter material layer in biomembrane are used in conjunction with each other to organic in sewage
Pollutant decompose and carries out adsorption treatment to bacterium, primary sound animal and metazoa, in the water outlet side COD ammonia of biomembrane
Nitrogen total phosphorus tachymeter is detected, to judge it is up to standard whether sewage is handled.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of variations, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (5)
1. a kind for the treatment of sewage by using biological membrane method and its technique, it is characterised in that:Biomembrane by anaerobic layer, aerobic layer, carrier and
Filter material layer forms, and sewage degradation step is as follows:Step 1:Biofilm:Prevent bacterium, organic pollution, primary sound animal and rear lively
Object passes through biomembrane;Step 2:Absorption:Adsorption layer is made of working lining and supporting layer, first to bacterium, organic pollution, primary sound
Animal and metazoa are adsorbed, and adsorption layer kills bacterium, primary sound animal and metazoa after absorption, makes its shape
At waste material layer;Step 3:Demoulding:Cooperated by internal cause and external cause, to after being killed on adsorption layer bacterium, organic pollution,
Primary sound animal and metazoa are cleared up.
2. a kind for the treatment of sewage by using biological membrane method according to claim 1 and its technique, it is characterised in that:Sewage flows through life
After object film, filler is mutually mixed by cobble, clinker and coke granule and is formed, micro- life of cobble, clinker and a coke absorption part
Object, microorganism largely breed in cobble, clinker and coke surface, gradually form one layer of satiny mucus shape film layer, and then right
Bacterium, organic pollution, primary sound animal and metazoa in sewage form one layer of barrier, its hydrone can only be made to pass through.
3. a kind for the treatment of sewage by using biological membrane method according to claim 1 and its technique, it is characterised in that:Adsorption layer total thickness
Degree is set as 1.8~2.0m, and work layer thickness is 1.3~1.6m, and for grain size between 25~40mm, support layer thickness is 0.2m,
Between 70~80mm, adsorption layer constantly thickeies grain size, generates layering, preferably oxygen animalcule, inside are nothing to absorption layer surface
Oxygen animalcule, aerobic microbiological carry out organic pollution to resolve into inorganic matter, reduce the nutrient in water, mucus shape film layer
To bacterium, primary sound animal and metazoa, no oxygen animalcule, bacterium, primary sound animal and metazoa largely consume in adsorption layer
The nutrition in portion, bacterium, primary sound animal and metazoa voluntarily inactivate.
4. a kind for the treatment of sewage by using biological membrane method according to claim 1 and its technique, it is characterised in that:Biological film inner layer
Microorganism cannot get sufficient nutrition and enter endogenous metabolism, form it into waste material layer;Microorganism not in secreting mucus matter, because
And the adhesive capacity between adsorption layer is lost, under the action of bubble disturbance of the waste material layer in sewage is with hydraulic shear, make
It obtains blocked up waste material layer and is detached from carrier, absorption surface, which can rapidly grow new waste material layer, to be continued to purify sewage.
5. a kind for the treatment of sewage by using biological membrane method according to claim 1 and its technique, it is characterised in that:To through biology
Film is discharged one end water sampling, and the content of the COD in water is detected using COD ammonia nitrogen total phosphorus tachymeters, to judge having in water outlet
The content of machine object judges whether sewage disposal is up to standard whether within critical field.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810274858.5A CN108483645A (en) | 2018-03-30 | 2018-03-30 | A kind for the treatment of sewage by using biological membrane method and its technique |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810274858.5A CN108483645A (en) | 2018-03-30 | 2018-03-30 | A kind for the treatment of sewage by using biological membrane method and its technique |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108483645A true CN108483645A (en) | 2018-09-04 |
Family
ID=63317558
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810274858.5A Pending CN108483645A (en) | 2018-03-30 | 2018-03-30 | A kind for the treatment of sewage by using biological membrane method and its technique |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108483645A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10032685A1 (en) * | 2000-07-05 | 2002-02-14 | Aqu Zentrum Fuer Arbeitssicher | Assembly to treat domestic sewage, for small households without a sewage removal facility, has flexible material forming clarifying body with separate function zones for easy transport and deployment at site |
CN105836900A (en) * | 2016-06-03 | 2016-08-10 | 北京荣蒂盛环境科技有限公司 | Ecological water purifying system |
-
2018
- 2018-03-30 CN CN201810274858.5A patent/CN108483645A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10032685A1 (en) * | 2000-07-05 | 2002-02-14 | Aqu Zentrum Fuer Arbeitssicher | Assembly to treat domestic sewage, for small households without a sewage removal facility, has flexible material forming clarifying body with separate function zones for easy transport and deployment at site |
CN105836900A (en) * | 2016-06-03 | 2016-08-10 | 北京荣蒂盛环境科技有限公司 | Ecological water purifying system |
Non-Patent Citations (1)
Title |
---|
宋志伟等: "《水污染控制工程》", 31 July 2013, 中国矿大出版社 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Soares | Biological denitrification of groundwater | |
Zhao et al. | Nitrate removal from groundwater by cooperating heterotrophic with autotrophic denitrification in a biofilm–electrode reactor | |
CN101704609B (en) | Feedwater treatment method by pre-ozonation and aerated biological activated carbon | |
Wang et al. | The effect of vermifiltration height and wet: dry time ratio on nutrient removal performance and biological features, and their influence on nutrient removal efficiencies | |
Kantawanichkul et al. | Nitrogen removal in a combined system: vertical vegetated bed over horizontal flow sand bed | |
CN104961306B (en) | A kind of processing method of vaccary breeding wastewater | |
Samal et al. | A comparative study of macrophytes influence on performance of hybrid vermifilter for dairy wastewater treatment | |
CN102146342B (en) | Halophilic bacterial agent and preparation method thereof as well as biological treatment system fixed with bacterial agent and application thereof | |
CN1513777A (en) | Permangnate preoxidation and bioactive carbon combined use to remove contamination technique | |
CN102303939A (en) | Front, middle and rear ozone and central aerated biological activated carbon water supply treatment method | |
Hu et al. | Drained water quality in sludge treatment wetlands: effects of earthworm densities and plant species | |
Arora et al. | A comparative study for pathogen removal using different filter media during vermifiltration | |
Gutiérrez‐Sarabia et al. | Slaughterhouse wastewater treatment in a full‐scale system with constructed wetlands | |
CN102464420B (en) | Sewage physical-chemical treatment method | |
CN112047576A (en) | Device for removing resistance genes and nitrogen and phosphorus in wastewater of livestock and poultry farm and operation process thereof | |
CN103319047A (en) | Landfill leachate treatment system | |
CN109354206A (en) | A kind of method of Sewage treatment in constructed wetland | |
CN110526504B (en) | System and method for treating regenerated waste liquid of targeted denitrification and dephosphorization resin | |
Zhao et al. | Optimising the performance of a lab-scale tidal flow reed bed system treating agricultural wastewater | |
CN102583886B (en) | Artificial wetland for treating sewage | |
Jiang et al. | Use of dewatered sludge as microbial inoculum of a subsurface wastewater infiltration system: effect on start-up and pollutant removal | |
Hasnine et al. | An overview of physicochemical and biological treatment of landfill leachate | |
CN109081441A (en) | A kind of system and method for recovering waste water from aquatic culture in original place | |
CN104291444A (en) | System and method for treatment of contact hydrolysis-algae micro-aeration composite wastewater | |
CN108483645A (en) | A kind for the treatment of sewage by using biological membrane method and its technique |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180904 |