CN110282820A - A kind of high stability processing system for trade effluent - Google Patents
A kind of high stability processing system for trade effluent Download PDFInfo
- Publication number
- CN110282820A CN110282820A CN201910553600.3A CN201910553600A CN110282820A CN 110282820 A CN110282820 A CN 110282820A CN 201910553600 A CN201910553600 A CN 201910553600A CN 110282820 A CN110282820 A CN 110282820A
- Authority
- CN
- China
- Prior art keywords
- sewage
- trade effluent
- high stability
- processing system
- bbr
- 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 claims abstract description 31
- 238000005273 aeration Methods 0.000 claims abstract description 13
- 238000002156 mixing Methods 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 10
- 238000004062 sedimentation Methods 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 7
- 230000003750 conditioning effect Effects 0.000 claims abstract description 4
- 239000004744 fabric Substances 0.000 claims abstract description 4
- 238000009434 installation Methods 0.000 claims abstract description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000010802 sludge Substances 0.000 claims description 14
- 239000005416 organic matter Substances 0.000 claims description 6
- 238000011282 treatment Methods 0.000 claims description 6
- 241001037822 Bacillus bacterium Species 0.000 claims description 3
- 229910019142 PO4 Inorganic materials 0.000 claims description 3
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 3
- 235000015097 nutrients Nutrition 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 3
- 239000010452 phosphate Substances 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 239000004576 sand Substances 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 11
- 238000004065 wastewater treatment Methods 0.000 abstract description 4
- 239000010842 industrial wastewater Substances 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000004904 shortening Methods 0.000 abstract 1
- 238000003911 water pollution Methods 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- 208000005623 Carcinogenesis Diseases 0.000 description 2
- 208000035473 Communicable disease Diseases 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 230000036952 cancer formation Effects 0.000 description 2
- 231100000504 carcinogenesis Toxicity 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 208000015181 infectious disease Diseases 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- BBEAQIROQSPTKN-UHFFFAOYSA-N pyrene Chemical compound C1=CC=C2C=CC3=CC=CC4=CC=C1C2=C43 BBEAQIROQSPTKN-UHFFFAOYSA-N 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 206010008631 Cholera Diseases 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000709687 Coxsackievirus Species 0.000 description 1
- 208000004232 Enteritis Diseases 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 208000030527 Minamata disease Diseases 0.000 description 1
- 208000009507 Nervous System Mercury Poisoning Diseases 0.000 description 1
- 208000005374 Poisoning Diseases 0.000 description 1
- 208000037386 Typhoid Diseases 0.000 description 1
- 241000726445 Viroids Species 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 231100000570 acute poisoning Toxicity 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 125000005605 benzo group Chemical group 0.000 description 1
- 229910052790 beryllium Inorganic materials 0.000 description 1
- ATBAMAFKBVZNFJ-UHFFFAOYSA-N beryllium atom Chemical compound [Be] ATBAMAFKBVZNFJ-UHFFFAOYSA-N 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 231100000739 chronic poisoning Toxicity 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 208000001848 dysentery Diseases 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- GVEPBJHOBDJJJI-UHFFFAOYSA-N fluoranthrene Natural products C1=CC(C2=CC=CC=C22)=C3C2=CC=CC3=C1 GVEPBJHOBDJJJI-UHFFFAOYSA-N 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 208000006454 hepatitis Diseases 0.000 description 1
- 231100000283 hepatitis Toxicity 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 231100000405 induce cancer Toxicity 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 208000027753 pain disease Diseases 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 125000005575 polycyclic aromatic hydrocarbon group Chemical group 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 201000008297 typhoid fever Diseases 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- 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
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Activated Sludge Processes (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention belongs to Industrial Waste Water Treatments applied technical fields, specifically disclose a kind of high stability processing system for trade effluent, including sequentially connected conditioning tank, grille well, aerated grit chamber, hybrid reaction sedimentation basin, mixing distribution reservoir, BBR device, aeration tank, secondary settling tank, turntable filtering cloth filtering pool, ultraviolet disinfection canal, reuse or discharge；Sewage is evacuated to aerated grit chamber by installation sewage pump in the grille well；The sewage is successively carried out different procedures processing by above system component parts, and by final reuse or discharge.A kind of beneficial effect of the high stability processing system for trade effluent of the present invention is: it designs reasonable, stable working state and can efficiently remove harmful substance such as COD, NH3-N, T-N in sewage etc., improve sewage treating efficiency and processing quality, the processing time for shortening sewage, reduce cost.
Description
Technical field
The invention belongs to Industrial Waste Water Treatments applied technical fields, and in particular to a kind of high stability for trade effluent
Processing system.
Background technique
Sewage refers to the general name of the water discharged in production and life activity, loses the original water for using function and is referred to as
Sewage, sewage are to cause aqueous metamorphism cannot be after continuation of insurance due to being mixed with new substance in water or because of the variation of external condition
Hold original use function.
The harm of water pollution is various, wherein the influence to human health is to cause acute and chronic poisoning, water
After body is polluted by toxic and harmful substance, poisoning just may cause by drinking-water or food chain, such as famous minamata disease, pain pain
Disease is as caused by water pollution；Carcinogenesis, certain chemical substances for having carcinogenesis such as arsenic, chromium, nickel, beryllium, aniline, benzo
(a) after pyrene and other polycyclic aromatic hydrocarbons, contaminated with halogenated hydrocarbons water body, it can be suspended object, bed mud absorption, it can also be in aquatic organism inner product
Tired, long-term drinking contains the water of this substance, or edible accumulation in vivo has the biology (such as fish) of this substance that may induce
Cancer；Occur using water as the infectious disease of medium.The biological pollutants polluted-water such as human and animal excreta may cause bacillary enteron aisle and pass
It catches an illness such as typhoid fever, dysentery, enteritis, cholera；Common virus such as gray nucleus viroid, Coxsackie virus, infectiousness in enteron aisle
Hepatitis virus etc. can all cause corresponding infectious disease by water pollution；It influences indirectly, after water pollution, can often cause water
Sensory properties deteriorates, and such as certain pollutants are under a certain concentration, though water generation can be made different without directly endangering the health of people
It is smelly, heterochromatic, foam and oil film etc. is presented, interferes the normal utilization of water body.The substances such as copper, zinc, nickel can inhibit under a certain concentration
The growth and breeding of microorganism decline water body self-purification ability to influence the decomposition and biological oxidation of Organic substance in water, influence
The sanitary condition of water body.
Water pollution can both seriously endanger the ecosystem, can also cause serious economic loss, so current water pollution
Improvement has attracted people's attention, and before the sewage such as production, life are discharged, needs to carry out a series of processing, so that
Its standard for reaching discharge.
Currently, for producing the processing system of trade effluent, design it is unreasonable, cannot be in efficient, high-quality removal sewage
The mixed harmful substance of institute and solid sundries etc., i.e., production Industrial Waste Water Treatments quality is low, the sewage treatment time is long, at high cost
Deng.
Therefore, based on the above issues, the present invention provides a kind of high stability processing system for trade effluent.
Summary of the invention
Goal of the invention: the object of the present invention is to provide a kind of high stability processing system for trade effluent, designs
Rationally, stable working state and harmful substance such as COD, NH3-N, T-N in sewage can efficiently be removed etc., improves sewage treatment effect
Rate and processing quality, shorten the processing time of sewage, reduce cost.
Technical solution: the present invention provides a kind of high stability processing system for trade effluent, including sequentially connected
Conditioning tank, grille well, aerated grit chamber, hybrid reaction sedimentation basin, mixing distribution reservoir, BBR device, aeration tank, secondary settling tank, turntable
Filtering cloth filtering pool, ultraviolet disinfection canal, reuse or discharge；Sewage is evacuated to sediment by aeration by installation sewage pump in the grille well
Pond；The sewage is successively carried out different procedures processing by above system component parts, and by final reuse or discharge.
The technical program, the BBR device is biofilm processing, by being attached on BBR device medium surface
Organic matter, ammonia nitrogen and phosphate in the absorption of Bacillus bacterium and decomposition water inlet, reach 40-75% to the removal rate of organic matter.
The technical program, the grid slag in trade effluent is screened out outward transport by the grille well, and the aerated grit chamber will
Sand setting in trade effluent screens out outward transport, and flocculant, the mixing water distribution is added when handling operation in the hybrid reaction sedimentation basin
Nutrient solution is added in pond when handling operation, air is added when handling operation in the BBR device, aeration tank.
The technical program, the hybrid reaction sedimentation basin is connect with thickened sludge pond, thickened sludge pond and sludge dewatering
Machine connection, the mud cake outward transport handled through dense sludge dewatering equipment.
The technical program, the aeration tank, secondary settling tank are connect with mixing distribution reservoir respectively, and the interior reflux of aeration tank is dirty
Water, secondary settling tank returned sludge be back to respectively mixing distribution reservoir carry out circular treatment again.
Compared with prior art, a kind of beneficial effect of the high stability processing system for trade effluent of the present invention exists
In: it designs reasonable, stable working state and can efficiently remove harmful substance such as COD, NH3-N, T-N in sewage etc., improves
Sewage treating efficiency and processing quality, shorten the processing time of sewage, reduce cost.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of high stability processing system for trade effluent of the invention；
Fig. 2 is a kind of water outlet detection data of high stability processing system for trade effluent of the invention.
Specific embodiment
In the following with reference to the drawings and specific embodiments, the present invention is furture elucidated.
A kind of high stability processing system for trade effluent as shown in Figure 1, including sequentially connected conditioning tank, lattice
Grid well, aerated grit chamber, hybrid reaction sedimentation basin, mixing distribution reservoir, BBR device, aeration tank, secondary settling tank, turntable filtering cloth filtering pool,
Ultraviolet disinfection canal, reuse or discharge；Sewage is evacuated to aerated grit chamber by installation sewage pump in the grille well；The sewage
Successively carry out different procedures processing by above system component parts, and by final reuse or discharge.
It is further preferred that the BBR device is biofilm processing, by being attached on BBR device medium surface
Organic matter, ammonia nitrogen and phosphate in the absorption of Bacillus bacterium and decomposition water inlet, reach 40-75% to the removal rate of organic matter；And
Grid slag in trade effluent is screened out outward transport by the grille well, and the aerated grit chamber will screen out the sand setting in trade effluent outer
Flocculant is added in fortune, the hybrid reaction sedimentation basin when handling operation, nutrient solution is added when handling operation in the mixing distribution reservoir,
Air is added when the BBR device, aeration tank processing operation；And the hybrid reaction sedimentation basin is connect with thickened sludge pond, it is dense
Contracting sludge-tank is connect with sludge dewatering equipment, the mud cake outward transport handled through dense sludge dewatering equipment；And the aeration tank, secondary settling tank difference
It is connect with mixing distribution reservoir, the interior reflux sewage of aeration tank, the returned sludge of secondary settling tank are back to mixing distribution reservoir again respectively
Carry out circular treatment.
Through this system, treated that COD index is as shown in the table,
；
Through this system, treated that NH3-N index is as shown in the table,
；
Through this system, treated that T-N index is as shown in the table,
。
Efficient process system for municipal sewage of the invention, treatment scale are 3/d of 12000m.
It is illustrated in figure 2 the water outlet detection data of the efficient process system for municipal sewage of the invention, is accorded with
National " urban wastewater treatment firm pollutant emission standard " (GB18918-2002) secondary standard is closed to ask.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
It for member, without departing from the principle of the present invention, can also make several improvements, these improvement also should be regarded as of the invention
Protection scope.
Claims (5)
1. a kind of high stability processing system for trade effluent, it is characterised in that: including sequentially connected conditioning tank, grid
Well, aerated grit chamber, hybrid reaction sedimentation basin, mixing distribution reservoir, BBR device, aeration tank, secondary settling tank, turntable filtering cloth filtering pool, purple
Outer disinfection canal, reuse or discharge；Sewage is evacuated to aerated grit chamber by installation sewage pump in the grille well；The sewage by
Above system component parts successively carries out different procedures processing, and by final reuse or discharge.
2. a kind of high stability processing system for trade effluent according to claim 1, it is characterised in that: described
BBR device is biofilm processing, is adsorbed and is decomposed in water inlet by the Bacillus bacterium being attached on BBR device medium surface
Organic matter, ammonia nitrogen and phosphate, 40-75% is reached to the removal rate of organic matter.
3. a kind of high stability processing system for trade effluent according to claim 1, it is characterised in that: the lattice
Grid slag in trade effluent is screened out outward transport by grid well, and the sand setting in trade effluent will be screened out outward transport, institute by the aerated grit chamber
Flocculant is added when stating the processing operation of hybrid reaction sedimentation basin, nutrient solution is added when handling operation in the mixing distribution reservoir, described
Air is added when BBR device, aeration tank processing operation.
4. a kind of high stability processing system for trade effluent according to claim 1, it is characterised in that: described mixed
It closes reaction settling basin to connect with thickened sludge pond, thickened sludge pond is connect with sludge dewatering equipment, is handled through dense sludge dewatering equipment
Mud cake outward transport.
5. a kind of high stability processing system for trade effluent according to claim 1, it is characterised in that: the exposure
Gas pond, secondary settling tank are connect with mixing distribution reservoir respectively, and the interior reflux sewage of aeration tank, the returned sludge of secondary settling tank are back to respectively
Mixing distribution reservoir carries out circular treatment again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910553600.3A CN110282820A (en) | 2019-06-25 | 2019-06-25 | A kind of high stability processing system for trade effluent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910553600.3A CN110282820A (en) | 2019-06-25 | 2019-06-25 | A kind of high stability processing system for trade effluent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110282820A true CN110282820A (en) | 2019-09-27 |
Family
ID=68005624
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910553600.3A Pending CN110282820A (en) | 2019-06-25 | 2019-06-25 | A kind of high stability processing system for trade effluent |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110282820A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112321064A (en) * | 2020-09-30 | 2021-02-05 | 南京传业环保科技有限公司 | Biochemical advanced treatment unit of BBR sewage |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4649911B2 (en) * | 2004-08-19 | 2011-03-16 | 栗田工業株式会社 | Treatment of organic matter and nitrogen-containing wastewater |
| CN103910463A (en) * | 2013-11-21 | 2014-07-09 | 青海洁神环境能源产业有限公司 | Novel process for BC urban sewage treatment |
| CN105060635A (en) * | 2015-08-07 | 2015-11-18 | 柴建中 | BBR urban sewage low temperature nitrogen removal treatment method |
| CN105621801A (en) * | 2016-01-18 | 2016-06-01 | 江阴市弘诺机械设备制造有限公司 | Biological reaction sewage treatment method |
| CN205473207U (en) * | 2016-01-18 | 2016-08-17 | 江阴市弘诺机械设备制造有限公司 | Biological reaction sewage treatment system |
-
2019
- 2019-06-25 CN CN201910553600.3A patent/CN110282820A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4649911B2 (en) * | 2004-08-19 | 2011-03-16 | 栗田工業株式会社 | Treatment of organic matter and nitrogen-containing wastewater |
| CN103910463A (en) * | 2013-11-21 | 2014-07-09 | 青海洁神环境能源产业有限公司 | Novel process for BC urban sewage treatment |
| CN105060635A (en) * | 2015-08-07 | 2015-11-18 | 柴建中 | BBR urban sewage low temperature nitrogen removal treatment method |
| CN105621801A (en) * | 2016-01-18 | 2016-06-01 | 江阴市弘诺机械设备制造有限公司 | Biological reaction sewage treatment method |
| CN205473207U (en) * | 2016-01-18 | 2016-08-17 | 江阴市弘诺机械设备制造有限公司 | Biological reaction sewage treatment system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112321064A (en) * | 2020-09-30 | 2021-02-05 | 南京传业环保科技有限公司 | Biochemical advanced treatment unit of BBR sewage |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Majumder et al. | A review on hospital wastewater treatment: A special emphasis on occurrence and removal of pharmaceutically active compounds, resistant microorganisms, and SARS-CoV-2 | |
| Sathya et al. | A comprehensive review on comparison among effluent treatment methods and modern methods of treatment of industrial wastewater effluent from different sources | |
| Ahmed et al. | Recent developments in physical, biological, chemical, and hybrid treatment techniques for removing emerging contaminants from wastewater | |
| CN105585220B (en) | A kind of urban sewage treatment system and purification method | |
| Li et al. | Hazardous substances and their removal in recirculating aquaculture systems: A review | |
| CN109592840A (en) | A kind of School Wastewater processing unit | |
| Alfonso-Muniozguren et al. | A combined activated sludge-filtration-ozonation process for abattoir wastewater treatment | |
| Altowayti et al. | The role of conventional methods and artificial intelligence in the wastewater treatment: a comprehensive review | |
| CN205099548U (en) | A section + A2O sewage treatment system | |
| CN101781048B (en) | Low ammonia nitrogen waste water treatment and recycling method | |
| KR102170601B1 (en) | Advanced sewage and wastewater separation membrane device using low temperature plasma | |
| Chan et al. | Oxidation of ammonia using immobilised FeCu for water treatment | |
| CN105693028A (en) | Eliminating system and method for wastewater biological toxicity in industrial park | |
| CN108212181A (en) | A kind of hollow microsphere photochemical catalyst and preparation method for sewage disposal | |
| Ali et al. | Sources, classifications, constituents, and available treatment technologies for various types of wastewater: An overview | |
| CN208471811U (en) | A kind of sewage disposal system | |
| CN109879386A (en) | A kind of food industrial wastewater treatment process | |
| CN110282820A (en) | A kind of high stability processing system for trade effluent | |
| CN1931750B (en) | Petrochemical effluent treating and reusing process | |
| Masood et al. | Current situation of pharmaceutical wastewater around the globe | |
| CN110282821A (en) | A kind of efficient process system for municipal sewage | |
| CN108821521A (en) | Multistage settling gardens regeneration effluent system | |
| CN201284279Y (en) | Biochemical processor | |
| Hill et al. | Reduction of enteric microbes in flushed swine wastewater treated by a biological aerated filter and UV irradiation | |
| CN108862817A (en) | A kind of sewage water treatment method |
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 |
Application publication date: 20190927 |
|
| RJ01 | Rejection of invention patent application after publication |