CN102329055A - Aquaculture sewage treatment method - Google Patents
Aquaculture sewage treatment method Download PDFInfo
- Publication number
- CN102329055A CN102329055A CN201110265303A CN201110265303A CN102329055A CN 102329055 A CN102329055 A CN 102329055A CN 201110265303 A CN201110265303 A CN 201110265303A CN 201110265303 A CN201110265303 A CN 201110265303A CN 102329055 A CN102329055 A CN 102329055A
- Authority
- CN
- China
- Prior art keywords
- sewage
- flocculation
- treatment
- treatment process
- aquiculture sewerage
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 49
- 238000009360 aquaculture Methods 0.000 title claims abstract description 38
- 244000144974 aquaculture Species 0.000 title abstract description 13
- 238000005189 flocculation Methods 0.000 claims abstract description 50
- 230000016615 flocculation Effects 0.000 claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000000034 method Methods 0.000 claims abstract description 31
- 238000005374 membrane filtration Methods 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 18
- 230000000813 microbial Effects 0.000 claims abstract description 15
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 241000894006 Bacteria Species 0.000 claims abstract description 10
- 239000012528 membrane Substances 0.000 claims abstract description 3
- 238000002360 preparation method Methods 0.000 claims description 14
- -1 aluminium iron Chemical compound 0.000 claims description 8
- 229920001661 Chitosan Polymers 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 4
- 230000000243 photosynthetic Effects 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 238000000108 ultra-filtration Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 238000001471 micro-filtration Methods 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 238000007599 discharging Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 239000008394 flocculating agent Substances 0.000 abstract 1
- 230000014759 maintenance of location Effects 0.000 abstract 1
- 230000037250 Clearance Effects 0.000 description 9
- 230000035512 clearance Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 6
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 241000276438 Gadus morhua Species 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-K [O-]P([O-])([O-])=O Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 4
- 235000019516 cod Nutrition 0.000 description 4
- 239000010452 phosphate Substances 0.000 description 4
- 208000005120 Congenital Preauricular Fistulae Diseases 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 230000001717 pathogenic Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000000050 nutritive Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 239000004599 antimicrobial Substances 0.000 description 1
- 244000052616 bacterial pathogens Species 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 230000001488 breeding Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000000249 desinfective Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003640 drug residue Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000002045 lasting Effects 0.000 description 1
- 230000002503 metabolic Effects 0.000 description 1
- 230000002906 microbiologic Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005429 turbidity Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Abstract
The invention discloses an aquaculture sewage treatment method, which specifically comprises the following steps of: firstly, feeding an microbial agent into sewage discharged from a culture pool, then introducing the sewage into a flocculation basin, and continuously feeding flocculants under the condition of continuous air aeration, wherein the hydraulic retention time is 15-30 minutes; and introducing the sewage subjected to air aeration and flocculation treatment into a membrane device under the action of a constant-flow pump to complete filter treatment, directly discharging permeated clear water or returning the permeated clear water to the culture pool for reutilization, and returning concentrated sewage to the flocculation basin for continuous treatment or directly discharging partial of the concentrated sewage. According to the aquaculture sewage treatment method, a biological treatment technology, a flocculation technology and a modern membrane filtration technology are organically combined, so that water quality is guaranteed, the production efficiency is increased, the production cost is greatly reduced, the advantages of simple process, stable system, small occupancy, low operation cost and the like are achieved, and bacteria and suspended matters in the sewage can be removed, and the purpose of safety recycling is achieved.
Description
Technical field
The present invention relates to sewage treatment area, specifically, relate to a kind of treatment process of aquiculture sewerage.
Background technology
China's aquaculture output occupies first of the world, world's aquaculture ultimate production 70% from China.Traditional aquatic products mode of supporting is not only fought for water resources with the mankind, and the particulate form thing that derives from ight soil and feed, The dissolved metabolic waste, The dissolved nutritive salt, anti-microbial agents and the drug residue etc. that are comprised in the aquaculture wastewater cause after being discharged in a large number and culture water and be close to waters eutrophication and serious water quality deterioration.In the face of the shortage of water resources and water surrounding resource, the growth pattern that must accelerate culture fishery changes, and the aquaculture pattern of seeking a kind of continuable " green " seems particularly important.With the aquaculture wastewater purification treatment technology is that the circulating water cultivation pattern of core is current one of modern aquaculture pattern of approval relatively in the world.Through suitable engineering means; Make aquiculture sewerage obtain sufficient recycle; Reduce environmental pollution; Get rid of environment and extraneous water pollution to culturing the interference and the influence of object, have low water usage amount, high-density, breeding production and do not receive regional climate restriction, resource utilization height, product high-quality and safety, few, the level of automation advantages of higher of disease, be a kind of low-carbon (LC), health, efficiently, the fish production pattern of lasting, environmental protection and coordinated development type.
The circulating water cultivation pattern has obtained widespread usage abroad.Since the seventies in 20th century, some countries as Japan, the U.S., Germany, Canada, Denmark etc. have successively carried out the research of circulating water cultivation water technology to some extent.At present, ozone, ultraviolet ray and water technology such as biological filter and facility are widely used in aquaculture abroad, and develop to mechanize, modernized direction.China starts late in this respect, and the eighties in last century, external circulating water cultivation facility and technology begin to get into China, but because high input and running cost, great majority are introduced facility and are are just laid aside and neglected very soon.China present most industrialized culture system facilities and equipment still is in lower level, and water processing establishment equipment famine, aquaculture wastewater be directly discharging still.
In view of this, the present invention organically combines biological treatment, flocculation technique and modern membrane filtration technique, and a kind of aquiculture sewerage treatment process is provided, and addressing the above problem, and realizes the circulating water cultivation pattern.
Summary of the invention
Present method of the present invention organically combines biological treatment, flocculation technique and modern membrane filtration technique, and a kind of new type purification method that is applied to aquiculture sewerage is provided, and overcomes the deficiency of prior art with this.
Design of the present invention is following:
Aquiculture sewerage has characteristics such as water yield fluctuation is big, change of water quality is big, pollution level is light, pollutant kind is few, the biological process oxygen-consumption is low.It is different with the conventional drinking water treatment that with removal turbidity, colourity and pathogenic micro-organism is purpose that aquaculture wastewater is handled; Also different with complicated component, concentration height and bio-refractory material Industrial Wastewater Treatment how, be more suitable for adopting the integrated method of simple biology, chemistry and physics to handle.Usually the aquaculture wastewater process object mainly includes machine thing (BOD
5, COD), ammonia nitrogen, nitrite nitrogen, total nitrogen, reactive phosphate, suspended solids and pathogenic bacteria etc.Be difficult to get rid of pollutent through the simple physics deposition, simple biological treatment can be removed organism, but not good to the removal effect of nutritive salt.And be that physical sedimentation or biological treatment all can't be removed suspended solids and pathogenic bacteria fully.Prior art has adopted enhanced biological processing, filtration treatment and some disinfections to handle in order to remove above-mentioned pollutent, has increased equipment input and running cost, is difficult to apply.To the characteristics of aquiculture sewerage, it is a kind of new water technology that the present invention handles organic integration to simple biological treatment (only need add microbial preparation one time), flocculation treatment, membrane filtration, reduced investment, and effective, processing costs is lower.The present invention both had been fit to handle continuously, also was fit to discontinuity treatment, and was easy to utilize.
To achieve these goals, solution of the present invention is following:
A kind of aquiculture sewerage treatment process comprises the steps:
(1) adds microbial preparation: the disposable microbial preparation that adds in aquiculture sewerage;
(2) flocculation agent flocculation treatment: again sewage is incorporated in the flocculation basin, in flocculation basin, adds flocculation agent continuously;
(3) air aeration is handled: when adding flocculation agent, with air sewage is continued aeration and handle, the residence time of sewage in flocculation basin is 10～30 minutes;
(4) membrane filtration is handled: sewage is handled through membrane filtration again, accomplishes solid-liquid separation; Separate seeing through primary water, and produce concentrated sewage;
(5) sewage backflow is handled: the concentrated sewage backflow of generation continues to handle in flocculation basin;
In the above-mentioned steps (1), said microbial preparation is photosynthetic bacterium, subtilis or both mixing;
In the above-mentioned steps (2), said flocculation agent is chitosan, aluminium iron polychloride or both mixing.The concentration of said flocculant concentration in sewage is 10～250mg/L;
In the above-mentioned steps (4), described film is microfiltration membrane or ultra-filtration membrane.
Compared with prior art, the present invention has following beneficial effect:
(1) in interpolation microbial preparation step of the present invention, add microbial preparation only need be when handling beginning disposable adding in the aquiculture sewerage.This is because in subsequent processes; Because the crown_interception of film, mikrobe can be accompanied by concentrated sewage and be utilized times without number, just the entire treatment process does not need to add microbial preparation again; Be disposable operation, can improve the utilising efficiency of microbial preparation greatly;
(2) in the present invention, sewage be continuous blow-down to flocculation basin, the process that is to say water treatment is (certainly present method be applicable to the discontinuity water treatment too) that can carry out continuously.Flocculation agent flocculation treatment step and membrane filtration treatment step are accompanied by sewage treatment process to be continued to carry out, thereby can realize the continuous processing of sewage;
(3) in the air aeration treatment step, continue to carry out air aeration in the flocculation treatment process and handle, providing biochemical treatment required oxygen, and can make the part ammonia nitrogen effusion water surface.Thereby improved the effect of biological treatment of sewage greatly.Therefore, the advantage of air aeration processing is: one, stirring is provided; Two, provide microbiological treatment needed oxygen;
(4) in the membrane filtration treatment step, the advantage that adopts membrane filtration to handle is: one, accomplish the separation of pollutent, guarantee that water outlet does not contain pathogenic bacteria etc., need not to increase in addition sterilizing unit; Two, guarantee not running off of microbial preparation, can use repeatedly.In this step, the primary water that sees through directly discharges or returns the breed pond and reuses, thereby has realized recycling of water resources;
(5) in the sewage backflow treatment step, can the concentrated sewage that contain effective mikrobe be turned back to again and continue in the flocculation basin to handle.
Sewage water treatment method of the present invention organically combines biological treatment, flocculation technique and modern membrane filtration technique, and treatment scheme is handled integrated by air aeration processing, flocculation agent flocculation treatment and membrane filtration.Promptly guaranteed water quality, improved production efficiency again, greatly reduced production cost, had advantages such as technology is simple, system stability, occupation of land is little, working cost is low, and can remove bacterium and the suspended substance in the sewage, thereby reach the purpose of safe reuse.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the present invention is made further detailed description, but accompanying drawing and embodiment to should not be construed as be the qualification that the present invention is carried out.
Fig. 1 is the process flow sheet of aquiculture sewerage treatment process of the present invention.
Embodiment
The concrete processing technological flow of aquiculture sewerage treatment process of the present invention is narrated as follows:
(1) adds microbial preparation: the disposable microbial preparation (dosage depends on the influent quality situation) that adds in aquiculture sewerage;
(2) flocculation agent flocculation treatment: again sewage is incorporated in the flocculation basin, in flocculation basin, adds flocculation agent (dosage depends on the influent quality situation) continuously;
(3) air aeration is handled: when adding flocculation agent, with air sewage is continued aeration and handle, the residence time of sewage in flocculation basin is 10～30 minutes;
(4) membrane filtration is handled: sewage is handled through membrane filtration again, accomplishes solid-liquid separation; Separate seeing through primary water, and produce concentrated sewage;
(5) sewage backflow is handled: the concentrated sewage backflow of generation continues to handle in flocculation basin.
Treatment process proposed by the invention can be narrated through following examples particularly:
Embodiment 1:
The concrete processing technological flow of aquiculture sewerage treatment process of the present invention is: add photosynthetic bacterium earlier, accomplish the startup of mikrobe; Adopting chitosan (CTS) again is flocculation agent, and dosage is 100mg/L sewage (m/v), and aquiculture sewerage is 20 minutes at the hydraulic detention time of flocculation basin, adopts micro-filtrate membrane filtration.
Sewage to before and after handling through present method is analyzed, is calculated, and draws pollutants removal rate.Record the water treatment effect: the COD clearance is 50%～65%, and the suspended solids clearance is 90%～95%, and ammonia nitrogen removal frank is 50%～55%, and the nitrite nitrogen removal efficiency is 70%～80%, and the reactive phosphate clearance is 45%～55%.The calculation formula of pollutants removal rate is:
, as follows.
Embodiment 2:
The concrete processing technological flow of aquiculture sewerage treatment process of the present invention is: add subtilis earlier, accomplish the startup of mikrobe.Adopting aluminium iron polychloride (PAFC) again is flocculation agent, and dosage is 30mg/L sewage (m/v),, aquiculture sewerage is 15min at the hydraulic detention time of flocculation basin, adopting the molecular weight that dams is 5000 ultrafiltration membrance filter.Record the water treatment effect: the COD clearance is 60%～70%, and the suspended solids clearance is 95%～100%, and ammonia nitrogen removal frank is 55%～65%, and the nitrite nitrogen removal efficiency is 75%～85%, and the reactive phosphate clearance is 50%～60%.
Embodiment 3:
The concrete processing technological flow of aquiculture sewerage treatment process of the present invention is: add photosynthetic bacterium and subtilis earlier, accomplish the startup of mikrobe.Adopting aluminium iron polychloride (PAFC) and chitosan (CTS) again is flocculation agent; The concentration that adds in sewage is: PAFC 30mg/L sewage (m/v); CTS 15mg/L sewage (m/v); Aquiculture sewerage is 30min at the hydraulic detention time of flocculation basin, and adopting the molecular weight that dams is 5000 ultrafiltration membrance filter.Record the water treatment effect: the COD clearance is 65%～75%, and the suspended solids clearance is 95%～100%, and ammonia nitrogen removal frank is 60%～70%, and the nitrite nitrogen removal efficiency is 80%～90%, and the reactive phosphate clearance is 55%～65%.
Can find out that through the foregoing description method of the present invention organically combines biological treatment, flocculation technique and modern membrane filtration technique, treatment scheme is handled integrated by air aeration processing, flocculation agent flocculation treatment and membrane filtration.Promptly guarantee water quality, improved production efficiency again, greatly reduced production cost, had advantages such as technology is simple, system stability, occupation of land is little, working cost is low, and can remove bacterium and the suspended substance in the sewage, reached the purpose of safe reuse.
The variation that is appreciated that a lot of details is possible, but therefore this do not run counter to scope of the present invention and spirit, and the those of ordinary skill of any affiliated technical field all should be regarded as not breaking away from the category of patent of the present invention to its suitable variation of doing.
Claims (5)
1. an aquiculture sewerage treatment process is characterized in that comprising the steps:
(1) adds microbial preparation: the disposable microbial preparation that adds in aquiculture sewerage;
(2) flocculation agent flocculation treatment: again sewage is incorporated in the flocculation basin, in flocculation basin, adds flocculation agent continuously;
(3) air aeration is handled: when adding flocculation agent, with air sewage is continued aeration and handle, the residence time of sewage in flocculation basin is 10～30 minutes;
(4) membrane filtration is handled: sewage is handled through membrane filtration again, accomplishes solid-liquid separation; Separate seeing through primary water, and produce concentrated sewage;
(5) sewage backflow is handled: the concentrated sewage of generation is back to and continues in the flocculation basin to handle.
2. a kind of aquiculture sewerage treatment process according to claim 1 is characterized in that: in the step (1), said microbial preparation is photosynthetic bacterium, subtilis or both mixing.
3. a kind of aquiculture sewerage treatment process according to claim 1 is characterized in that: in the step (2), said flocculation agent is chitosan, aluminium iron polychloride or both mixing.
4. a kind of aquiculture sewerage treatment process according to claim 1 is characterized in that: in the step (2), the concentration of said flocculant concentration in sewage is 10～250mg/L.
5. a kind of aquiculture sewerage treatment process according to claim 1 is characterized in that: in the step (4), described film is microfiltration membrane or ultra-filtration membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110265303A CN102329055A (en) | 2011-09-08 | 2011-09-08 | Aquaculture sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110265303A CN102329055A (en) | 2011-09-08 | 2011-09-08 | Aquaculture sewage treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102329055A true CN102329055A (en) | 2012-01-25 |
Family
ID=45481051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110265303A Pending CN102329055A (en) | 2011-09-08 | 2011-09-08 | Aquaculture sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102329055A (en) |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897879A (en) * | 2012-09-26 | 2013-01-30 | 暨南大学 | Inorganic-organic composite flocculant, preparation method and application thereof |
| CN103496819A (en) * | 2013-09-18 | 2014-01-08 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Method for sterilization treatment on aquaculture wastewater |
| CN103496820A (en) * | 2013-09-18 | 2014-01-08 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Aquaculture sewage treating method |
| CN103910467A (en) * | 2014-05-14 | 2014-07-09 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Method for processing aquatic product culture waste water |
| CN104193001A (en) * | 2014-09-19 | 2014-12-10 | 盐城工学院 | Aquaculture substrate modifier and preparation method thereof |
| CN105668941A (en) * | 2016-04-01 | 2016-06-15 | 浙江东洋环境工程有限公司 | Circulating plant and method for young shrimp culture water |
| CN106172220A (en) * | 2016-07-27 | 2016-12-07 | 广西陆川县润润养殖有限公司 | A kind of cultural method hybridizing BaMa miniature pig |
| CN107162325A (en) * | 2017-06-01 | 2017-09-15 | 中国水产科学研究院长江水产研究所 | A kind of processing method for cultivating raw water |
| CN107364999A (en) * | 2017-08-09 | 2017-11-21 | 过蕊 | A kind of organic waste-water treating apparatus |
| CN107963744A (en) * | 2017-11-22 | 2018-04-27 | 苏州赛比膜分离科技有限公司 | A kind of sewage treatment process |
| US10034461B2 (en) | 2015-05-21 | 2018-07-31 | Atlantic Sapphire IP, L.L.C. | Systems and methods of intensive recirculating aquaculture |
| CN110950455A (en) * | 2019-11-28 | 2020-04-03 | 中国第一汽车股份有限公司 | Treatment system and treatment method for water-based paint waste cleaning solvent |
| US10959411B2 (en) | 2018-01-04 | 2021-03-30 | Atlantic Sapphire IP, L.L.C. | Bottom grading apparatuses for aquaculture systems |
| CN113149343A (en) * | 2021-03-26 | 2021-07-23 | 北京城市排水集团有限责任公司 | Electrochemical nitrogen and phosphorus removal device and method |
| US11425895B2 (en) | 2020-03-05 | 2022-08-30 | Atlantic Sapphire Ip, Llc | Method for optimization of filtration in an aquaculture system |
| US11484015B2 (en) | 2015-05-21 | 2022-11-01 | Atlantic Sapphire Ip, Llc | Systems and methods of intensive recirculating aquaculture |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1412133A (en) * | 2001-10-15 | 2003-04-23 | 中国市政工程华北设计研究院 | Air-stirring sludge-refluxing chemical flocculation precipitation sewage treatment method |
| CN101219846A (en) * | 2008-01-23 | 2008-07-16 | 哈尔滨工业大学 | Ultrafiltration membrane coagulation /adsorption/bioreactor integrating advanced water treatment method and device |
| JP2009226285A (en) * | 2008-03-21 | 2009-10-08 | Metawater Co Ltd | Flocculation-membrane filtration method |
-
2011
- 2011-09-08 CN CN201110265303A patent/CN102329055A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1412133A (en) * | 2001-10-15 | 2003-04-23 | 中国市政工程华北设计研究院 | Air-stirring sludge-refluxing chemical flocculation precipitation sewage treatment method |
| CN101219846A (en) * | 2008-01-23 | 2008-07-16 | 哈尔滨工业大学 | Ultrafiltration membrane coagulation /adsorption/bioreactor integrating advanced water treatment method and device |
| JP2009226285A (en) * | 2008-03-21 | 2009-10-08 | Metawater Co Ltd | Flocculation-membrane filtration method |
Non-Patent Citations (1)
| Title |
|---|
| 艾翠玲 等: "膜生物反应器在污水处理中的应用研究现状", 《长安大学学报（自然科学版）》 * |
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897879A (en) * | 2012-09-26 | 2013-01-30 | 暨南大学 | Inorganic-organic composite flocculant, preparation method and application thereof |
| CN102897879B (en) * | 2012-09-26 | 2013-11-06 | 暨南大学 | Inorganic-organic composite flocculant, preparation method and application thereof |
| CN103496819A (en) * | 2013-09-18 | 2014-01-08 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Method for sterilization treatment on aquaculture wastewater |
| CN103496820A (en) * | 2013-09-18 | 2014-01-08 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Aquaculture sewage treating method |
| CN103910467A (en) * | 2014-05-14 | 2014-07-09 | 苏州市阳澄湖现代农业产业园特种水产养殖有限公司 | Method for processing aquatic product culture waste water |
| CN104193001A (en) * | 2014-09-19 | 2014-12-10 | 盐城工学院 | Aquaculture substrate modifier and preparation method thereof |
| US10694722B1 (en) | 2015-05-21 | 2020-06-30 | Atlantic Sapphire IP, L.L.C. | Systems and methods of intensive recirculating aquaculture |
| US11484015B2 (en) | 2015-05-21 | 2022-11-01 | Atlantic Sapphire Ip, Llc | Systems and methods of intensive recirculating aquaculture |
| US10034461B2 (en) | 2015-05-21 | 2018-07-31 | Atlantic Sapphire IP, L.L.C. | Systems and methods of intensive recirculating aquaculture |
| CN105668941A (en) * | 2016-04-01 | 2016-06-15 | 浙江东洋环境工程有限公司 | Circulating plant and method for young shrimp culture water |
| CN105668941B (en) * | 2016-04-01 | 2018-11-06 | 浙江东洋环境工程有限公司 | A kind of recycle unit and round-robin method of shrimp seed rearing water |
| CN106172220A (en) * | 2016-07-27 | 2016-12-07 | 广西陆川县润润养殖有限公司 | A kind of cultural method hybridizing BaMa miniature pig |
| CN107162325A (en) * | 2017-06-01 | 2017-09-15 | 中国水产科学研究院长江水产研究所 | A kind of processing method for cultivating raw water |
| CN107364999A (en) * | 2017-08-09 | 2017-11-21 | 过蕊 | A kind of organic waste-water treating apparatus |
| CN107963744A (en) * | 2017-11-22 | 2018-04-27 | 苏州赛比膜分离科技有限公司 | A kind of sewage treatment process |
| US10959411B2 (en) | 2018-01-04 | 2021-03-30 | Atlantic Sapphire IP, L.L.C. | Bottom grading apparatuses for aquaculture systems |
| CN110950455A (en) * | 2019-11-28 | 2020-04-03 | 中国第一汽车股份有限公司 | Treatment system and treatment method for water-based paint waste cleaning solvent |
| US11425895B2 (en) | 2020-03-05 | 2022-08-30 | Atlantic Sapphire Ip, Llc | Method for optimization of filtration in an aquaculture system |
| CN113149343A (en) * | 2021-03-26 | 2021-07-23 | 北京城市排水集团有限责任公司 | Electrochemical nitrogen and phosphorus removal device and method |
| CN113149343B (en) * | 2021-03-26 | 2022-05-17 | 北京城市排水集团有限责任公司 | Electrochemical nitrogen and phosphorus removal device and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102329055A (en) | Aquaculture sewage treatment method | |
| CN102336498B (en) | Nitrogen-phosphorus wastewater treating method by sequencing batch reactor coupled photobioreactor | |
| CN104671615B (en) | A kind of Taihu Lake that is used for enters lake livestock and poultry cultivation sewage treatment process | |
| CN105541003A (en) | Method for treating aquaculture wastewater | |
| CN103466882A (en) | Livestock and poultry breeding wastewater treatment technology | |
| CN107082536A (en) | A kind of cultivating wastewater purification technique | |
| CN105271610A (en) | Comprehensive processing process of culturing farm cow dung waste water | |
| CN104944710A (en) | Medical wastewater three-stage treatment technique | |
| CN103304093B (en) | Device and method for advanced denitrification and phosphorous removal of municipal wastewater | |
| CN101468859A (en) | Advanced purification treatment system for high concentrated organic wastewater | |
| CN105859033A (en) | Domestic sewage treatment process | |
| CN106830542A (en) | UASB two-stage A/O coagulating treatments pig farm biogas slurry system | |
| CN103663871A (en) | Method used for processing and recycling of aquacultural waste water | |
| CN104761102A (en) | Comprehensive reaction purification treatment method for recycling culture tail water | |
| CN109761455A (en) | A kind of processing method of synthesis and the class pharmaceuticals industry sewage that ferments | |
| Ashadullah et al. | Wastewater treatment by microalgal membrane bioreactor: evaluating the effect of organic loading rate and hydraulic residence time | |
| CN106946403A (en) | UASB two-stage A/O coagulating treatments pig farm biogas slurry technique | |
| CN102531277A (en) | Purification method and device of cold-water fish cultivation water body in mountain gully watershed | |
| CN204918299U (en) | Biological laboratory effluent disposal system | |
| CN108069570B (en) | Method for removing carbon, nitrogen and phosphorus in aquaculture wastewater | |
| CN204737860U (en) | Effluent disposal system is bred to beasts and birds | |
| CN102502972B (en) | Method using downflow biological aerated filter to treat algal slurry press filtrate | |
| CN108164002A (en) | A kind of microorganism and the method for nanoscale PAC built-up flocculants processing cultivation water | |
| CN210261453U (en) | Recirculating aquaculture and tail water treatment integrated water treatment system | |
| CN104926014A (en) | Traditional wastewater processing system and technology |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20120125 |