CN105461176A - Integrated system for treating domestic sewage - Google Patents
Integrated system for treating domestic sewage Download PDFInfo
- Publication number
- CN105461176A CN105461176A CN201511034488.0A CN201511034488A CN105461176A CN 105461176 A CN105461176 A CN 105461176A CN 201511034488 A CN201511034488 A CN 201511034488A CN 105461176 A CN105461176 A CN 105461176A
- Authority
- CN
- China
- Prior art keywords
- contact oxidation
- biological contact
- pond
- oxidation pond
- water
- 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
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
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 Using Semi-Permeable Membranes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention provides an integrated system for treating domestic sewage. The integrated system comprises a biochemical treatment device and a deep water treatment room; the biochemical treatment device comprises an air blower, a primary settling pond, an anaerobic pond, a first biological contact oxidation pond, a second biological contact oxidation pond, a third biological contact oxidation pond, a settling pond, a clear water disinfection pond, a disinfection system and a sludge well; the deep water treatment room comprises a multi-medium filter, a full-automatic filter value, a belt filter, an ultrafiltration system, a water producing box, an efflux pump, an air pump, a backwashing pump and a bactericide adding system; the primary settling pond, the anaerobic pond, the first biological contact oxidation pond, the second biological contact oxidation pond, the third biological contact oxidation pond, the settling pond, the clear water disinfection pond and the deep water treatment room are sequentially adjacent and are formed in the mode that a box is partitioned by partition plates. According to the integrated system for treating the domestic sewage, the mode that biochemical treatment and microfiltration deep treatment are combined is adopted, it is guaranteed that the treated sewage can meet the requirement of the reuse water quality through the system, and the system is also suitable for sewage treatment of cities and towns.
Description
Technical field
The present invention relates to sanitary sewage disposal technical field, particularly relate to a kind of integral system processing sanitary sewage.
Background technology
In recent years, along with the constantly in short supply of water resources and the continuous reinforcement of environmental pollution control, the control of people to the sewage that community in urban areas produces has dropped into increasing concern.Now, the administering method of the sewage that community produces roughly has activated sludge process, biological filter process, biomembrance process etc., these methods are mostly existing technology directly applied in community's sewage disposal, and the cost that result in Sewage treatment systems is high, floor space large and the low standard that can not reach reuse of effluent quality.Thus make these Sewage treatment systemss be difficult to popularize in the work for the treatment of of town sewage.
Summary of the invention
Main purpose of the present invention is to solve problems of the prior art, provides a kind of low cost of manufacture, technical process is simple, floor space is little, effluent quality can reach reuse standard, compact construction, flexible for installation and be easy to manage the integral system of process sanitary sewage used.
For solving the problems of the technologies described above, the technical solution used in the present invention is: a kind of integral system processing sanitary sewage, the integral system of described process sanitary sewage comprises biochemical treatment apparatus and deep water treatment chamber, described biochemical treatment apparatus comprises gas blower, preliminary sedimentation tank, anaerobic pond, biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three, settling tank, clear water sterilization pool, sterilizing unit and sewer catch basin, described advanced treatment room comprises more medium filter, Full-automatic filter valve, deep bed filter, ultrafiltration system, produce water tank, efflux pump, air pump, backwashing pump and sterilant medicine system, wherein,
Described preliminary sedimentation tank, anaerobic pond, biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three, settling tank, clear water sterilization pool and deep water treatment chamber are cut off by partition panel that casing is adjacent is successively formed;
After described gas blower, a sub-cylinder is set, and the aerating system that this gas blower is arranged with the bottom in described biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three is respectively connected; The casing of the upside of described preliminary sedimentation tank is arranged a water-in, and this preliminary sedimentation tank top arranges an overflow groove near the side of described anaerobic pond; The bottom of described anaerobic pond arranges a perforate, and the bottom of this anaerobic pond also arranges a mud discharging mouth; The top of described biological contact oxidation pond one arranges a perforate; The bottom of described biological contact oxidation pond two arranges a perforate; The top of described biological contact oxidation pond three arranges an overflow groove near the side of described settling tank; Biside plate on the downside of described settling tank inner chamber is provided with taper storage basin, casing bottom described taper storage basin arranges a mud discharging mouth, and the two side of this settling tank is provided with locating support, described locating support is arranged at the upside of described taper storage basin, and this locating support is provided with several swash plates, described swash plate is used for settled sludge, simultaneously, the sidewall of this settling tank also arranges a water outlet, described water outlet is arranged at the upside of described swash plate, and this water outlet is connected with described clear water sterilization pool; In described clear water sterilization pool, a sterilizing unit is set, and between this clear water sterilization pool and described advanced treatment room, a lift pump is set; Described sewer catch basin is connected with described preliminary sedimentation tank, biological contact oxidation pond one, biological contact oxidation pond three, settling tank, clear water sterilization pool respectively;
Described more medium filter is arranged at after described lift pump, and this more medium filter is arranged a Full-automatic filter valve, after described Full-automatic filter valve, a deep bed filter is set, after described deep bed filter, a ultrafiltration system is set, described ultrafiltration system is arranged an air pump, and this ultrafiltration system below a backwashing pump is set, described backwashing pump is connected with described product water tank, simultaneously, described product water tank and described deep bed filter, described ultrafiltration system is connected respectively, and this product water tank below an efflux pump is set, described sterilization medicine system is connected with described ultrafiltration system.
Further, described aerating system is set to micro-hole aerator.
Further, described preliminary sedimentation tank is set to perpendicular stream preliminary sedimentation tank.
Further, arrange a water pump before described water-in, this pump is communicated with source of sewage.
Further, arrange a pipe core bottom described preliminary sedimentation tank, described pipe core is connected with described water-in.
Further, the bottom of described pipe core arranges an echo area, described echo area water distribution uniformity.
Further, described overflow groove is communicated with adjacent described anaerobic pond, described settling tank respectively each via pipeline.
Further, the casing of described anaerobic pond is provided with locating support, described locating support hangs several combined stuffing strings, form combined stuffing district.
Further, the casing of described biological contact oxidation pond one, biological contact oxidation pond two and biological contact oxidation pond three is respectively arranged with locating support, described locating support hangs several combined stuffing strings, form Ball-type packing district.
Further, described combined stuffing string is set to several fillers of serial connection rope serial connection, and described filler is set to umbrella-shaped structure, and this filler is soft plastic material.
The advantage that the present invention has and positively effect are: the integral system of process sanitary sewage provided by the invention, by the mode that biochemical treatment and micro-filtration advanced treatment combine, ensure that the Nitrogen/Phosphorus Removal of sanitary sewage disposal, stable water outlet, water quality can reach reuse standard, simultaneously, the low cost of manufacture of this system, technical process is simple, floor space is little, compact construction, flexible for installation, be easy to management and can civil engineering cost be saved, equipment cost and running cost, and the integral system of this cover process sanitary sewage, be of value to popularizing of the treatment unit of the sanitary sewage of community in urban areas.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of biochemical treatment apparatus part of the present invention;
Fig. 2 is the schematic diagram of advanced treatment room of the present invention part;
In figure: 10-biochemical treatment apparatus, 101-water-in, 102-gas blower, 103-sub-cylinder, 104-preliminary sedimentation tank, 105-anaerobic pond, 106-biological contact oxidation pond one, 107-biological contact oxidation pond two, 108-biological contact oxidation pond three, 109-settling tank, 110-clear water sterilization pool, 111-sterilizing unit, 112-sewer catch basin, 20-advanced treatment room, 201-lift pump, 202-more medium filter, 203-Full-automatic filter valve, 204-deep bed filter, 205-ultrafiltration system, 206-produces water tank, 207-efflux pump, 208-air pump, 209-backwashing pump, 210-sterilant medicine system.
Embodiment
For a better understanding of the present invention, below in conjunction with specific embodiments and the drawings, the present invention is conducted further description.
As depicted in figs. 1 and 2, a kind of integral system processing sanitary sewage, comprise biochemical treatment apparatus 10 and deep water treatment chamber 20, described biochemical treatment apparatus 10 comprises gas blower 102, preliminary sedimentation tank 104, anaerobic pond 105, biological contact oxidation pond 1, biological contact oxidation pond 2 107, biological contact oxidation pond 3 108, settling tank 109, clear water sterilization pool 110, sterilizing unit 111 and sewer catch basin 112, described advanced treatment room 20 comprises more medium filter 202, Full-automatic filter valve 203, deep bed filter 204, ultrafiltration system 205, produce water tank 206, efflux pump 207, air pump 208, backwashing pump 209 and sterilant medicine system 210, wherein,
Preliminary sedimentation tank 104, anaerobic pond 105, biological contact oxidation pond 1, biological contact oxidation pond 2 107, biological contact oxidation pond 3 108, settling tank 109, clear water sterilization pool 110 and deep water treatment chamber 20 are cut off by partition panel that casing is adjacent is successively formed;
After gas blower 102, a sub-cylinder 103 is set, and the aerating system that this gas blower 102 is arranged with the bottom in biological contact oxidation pond 1, biological contact oxidation pond 2 107, biological contact oxidation pond 3 108 is respectively connected; The casing of the upside of preliminary sedimentation tank 104 is arranged a water-in 101, and this preliminary sedimentation tank 104 top arranges an overflow groove near the side of anaerobic pond 105; The bottom of anaerobic pond 105 arranges a perforate, and the bottom of this anaerobic pond 105 also arranges a mud discharging mouth; The top of biological contact oxidation pond 1 arranges a perforate; The bottom of biological contact oxidation pond 2 107 arranges a perforate; The top of biological contact oxidation pond 3 108 arranges an overflow groove near the side of settling tank 104; Biside plate on the downside of settling tank 109 inner chamber is provided with taper storage basin, casing bottom taper storage basin is arranged a mud discharging mouth, and the two side of this settling tank 109 is provided with locating support, locating support is arranged at the upside of taper storage basin, and this locating support is provided with several swash plates, and swash plate is used for settled sludge, simultaneously, the sidewall of this settling tank 109 also arranges a water outlet, and water outlet is arranged at the upside of swash plate, and this water outlet is connected with clear water sterilization pool 110; One sterilizing unit 111 is set in clear water sterilization pool 110, and between this clear water sterilization pool 110 and advanced treatment room 20, a lift pump 201 is set; Sewer catch basin 112 is connected with preliminary sedimentation tank 104, biological contact oxidation pond 1, biological contact oxidation pond 3 108, settling tank 109, clear water sterilization pool 110 respectively;
More medium filter 202 is arranged at after lift pump 201, and this more medium filter 202 arranges a Full-automatic filter valve 203, after Full-automatic filter valve 203, a deep bed filter 204 is set, after deep bed filter 204, a ultrafiltration system 205 is set, ultrafiltration system 205 is arranged an air pump 208, and this ultrafiltration system 205 below a backwashing pump 209 is set, backwashing pump 209 is connected with product water tank 206, simultaneously, produce water tank 206 and deep bed filter 204, ultrafiltration system 205 is connected respectively, and this product water tank 206 below an efflux pump 207 is set, sterilization medicine system 210 is connected with ultrafiltration system 205.
Aerating system is set to micro-hole aerator.
Preliminary sedimentation tank 104 is set to perpendicular stream preliminary sedimentation tank.
Arrange a water pump before water-in 101, this pump is communicated with source of sewage.
Arrange a pipe core bottom preliminary sedimentation tank 104, this pipe core is connected with water-in 101.
The bottom of pipe core arranges an echo area, this echo area water distribution uniformity.
Overflow groove is communicated with adjacent anaerobic pond 105, settling tank 109 respectively each via pipeline.
The casing of anaerobic pond 105 is provided with locating support, locating support hangs several combined stuffing strings, form combined stuffing district.
The casing of biological contact oxidation pond 1, biological contact oxidation pond 2 107 and biological contact oxidation pond 3 108 is respectively arranged with locating support, locating support hangs several combined stuffing strings, form Ball-type packing district.
Locating support hangs several combined stuffing strings, combined stuffing string is set to several fillers of serial connection rope serial connection, and filler is set to umbrella-shaped structure, and this filler is soft plastic material.
Use the integral system of process sanitary sewage provided by the invention, effluent quality can be made to reach reuse standard.During this system works, sewage passes through the lifting of water pump by water-in 101, and the water distribution uniformity through the echo area of pipe core is pumped in preliminary sedimentation tank 104, then under the agitaion of the intake pressure of anaerobic pond 105, form the sludge blanket suspended, sewage is flowed downward by this Chi Chiding and enters combined stuffing district, the sludge blanket formed on filler through bacterium adsorbs suspended substance, net is caught, biofloculation, biological degradation, solid matter is made to be degraded to dissolved matter, macromolecular substance is degraded to small-molecule substance, in the process of degraded COD, sewage is clarified, the mud that anaerobic pond produces then is discharged by the mud discharging mouth be arranged on bottom this pond, process water after anaerobic pond is from entering biological contact oxidation pond bottom it, simultaneously, air is divided into three tunnels by sub-cylinder 103 by gas blower 102, and every air-supply duct all has a gas meter, biological contact oxidation pond 1 is entered after cloth band of gas aeration, the Ball-type packing district of biological contact oxidation pond 2 107 and biological contact oxidation pond 3 108, the microorganism on Ball-type packing is helped to process sewage under the effect of dissolved oxygen, then, process water flows through settling tank 109 again, mud in this pond is discharged into sewer catch basin, processing water then flows in clear water sterilization pool 110, sterilizing agent drops in clear water sterilization pool 110 by sterilizing unit 111 simultaneously, be promoted in advanced treatment room 20 by lift pump 201 again after clear water sterilization pool 110 processes, process water is successively by the Full-automatic filter valve 203 on more medium filter 202, deep bed filter 204, ultrafiltration system 205, produce the deep purifying of water tank 206, by efflux pump 207 by the water pump that finally obtains to water, thus complete the treating processes of sewage.Wherein, the mud produced in preliminary sedimentation tank 104, biological contact oxidation pond 1 and biological contact oxidation pond 3 108 is directed to sewer catch basin, and sewage is also introduced sewer catch basin when keeping in repair emptying by clear water sterilization pool 110.In addition, the waste water of Full-automatic filter valve 203 regularly backwash can be discharged into water drain, and ultrafiltration system 205 also regularly will carry out air water backwash, and need air pump 208, backwashing pump 209 and sterilization medicine system 210 to cooperate during backwash, the waste water of backwash also enters water drain simultaneously.
Above embodiments of the invention have been described in detail, but described content being only preferred embodiment of the present invention, can not being considered to for limiting practical range of the present invention.All equalizations done according to the scope of the invention change and improve, and all should still belong within this patent covering scope.
Claims (10)
1. one kind processes the integral system of sanitary sewage, it is characterized in that: the integral system of described process sanitary sewage comprises biochemical treatment apparatus and deep water treatment chamber, described biochemical treatment apparatus comprises gas blower, preliminary sedimentation tank, anaerobic pond, biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three, settling tank, clear water sterilization pool, sterilizing unit and sewer catch basin, described advanced treatment room comprises more medium filter, Full-automatic filter valve, belt filter, ultrafiltration system, produce water tank, efflux pump, air pump, backwashing pump and sterilant medicine system, wherein,
Described preliminary sedimentation tank, anaerobic pond, biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three, settling tank, clear water sterilization pool and deep water treatment chamber are cut off by partition panel that casing is adjacent is successively formed;
After described gas blower, a sub-cylinder is set, and the aerating system that this gas blower is arranged with the bottom in described biological contact oxidation pond one, biological contact oxidation pond two, biological contact oxidation pond three is respectively connected; The casing of the upside of described preliminary sedimentation tank is arranged a water-in, and this preliminary sedimentation tank top arranges an overflow groove near the side of described anaerobic pond; The bottom of described anaerobic pond arranges a perforate, and the bottom of this anaerobic pond also arranges a mud discharging mouth; The top of described biological contact oxidation pond one arranges a perforate; The bottom of described biological contact oxidation pond two arranges a perforate; The top of described biological contact oxidation pond three arranges an overflow groove near the side of described settling tank; Biside plate on the downside of described settling tank inner chamber is provided with taper storage basin, the casing of the bottom of described taper storage basin arranges a mud discharging mouth, and the two side of this settling tank is provided with locating support, described locating support is arranged at the upside of described taper storage basin, and this locating support is provided with several swash plates, meanwhile, the sidewall of this settling tank also arranges a water outlet, described water outlet is arranged at the upside of described swash plate, and this water outlet is connected with described clear water sterilization pool; In described clear water sterilization pool, a sterilizing unit is set, and between this clear water sterilization pool and described advanced treatment room, a lift pump is set; Described sewer catch basin is connected with described preliminary sedimentation tank, biological contact oxidation pond one, biological contact oxidation pond three, settling tank, clear water sterilization pool respectively;
Described more medium filter is arranged at after described lift pump, and this more medium filter is arranged a Full-automatic filter valve, after described Full-automatic filter valve, a deep bed filter is set, after described deep bed filter, a ultrafiltration system is set, described ultrafiltration system is arranged an air pump, and this ultrafiltration system below a backwashing pump is set, described backwashing pump is connected with described product water tank, simultaneously, described product water tank and described deep bed filter, described ultrafiltration system is connected respectively, and this product water tank below an efflux pump is set, described sterilization medicine system is connected with described ultrafiltration system.
2. the integral system of process sanitary sewage according to claim 1, is characterized in that: described aerating system is set to micro-hole aerator.
3. the integral system of process sanitary sewage according to claim 1, is characterized in that: described preliminary sedimentation tank is set to perpendicular stream preliminary sedimentation tank.
4. the integral system of process sanitary sewage according to claim 1, is characterized in that: also comprise, and arranges a water pump before described water-in, and this pump is communicated with source of sewage.
5. the integral system of process sanitary sewage according to claim 1, is characterized in that: also comprise, and arranges a pipe core bottom described preliminary sedimentation tank, and described pipe core is connected with described water-in.
6. the integral system of process sanitary sewage according to claim 5, is characterized in that: also comprise, and the bottom of described pipe core arranges an echo area, described echo area water distribution uniformity.
7. the integral system of process sanitary sewage according to claim 1, is characterized in that: also comprise, and described overflow groove is communicated with adjacent described anaerobic pond, described settling tank respectively each via pipeline.
8. the integral system of process sanitary sewage according to claim 1, is characterized in that: also comprise, and the casing of described anaerobic pond is provided with locating support, described locating support hangs several combined stuffing strings, forms combined stuffing district.
9. the integral system of process sanitary sewage according to claim 1, it is characterized in that: also comprise, the casing of biological contact oxidation pond one, biological contact oxidation pond two and biological contact oxidation pond three is respectively arranged with locating support, described locating support hangs several combined stuffing strings, form Ball-type packing district.
10. according to Claim 8 or the integral system of process sanitary sewage according to claim 9, it is characterized in that: described combined stuffing string is set to several fillers of serial connection rope serial connection, and described filler is set to umbrella-shaped structure, and this filler is soft plastic material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511034488.0A CN105461176A (en) | 2015-12-31 | 2015-12-31 | Integrated system for treating domestic sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511034488.0A CN105461176A (en) | 2015-12-31 | 2015-12-31 | Integrated system for treating domestic sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105461176A true CN105461176A (en) | 2016-04-06 |
Family
ID=55599403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201511034488.0A Pending CN105461176A (en) | 2015-12-31 | 2015-12-31 | Integrated system for treating domestic sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105461176A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105800855A (en) * | 2016-05-25 | 2016-07-27 | 王杨 | Community domestic wastewater treatment device |
| CN105819631A (en) * | 2016-05-25 | 2016-08-03 | 王杨 | Municipal wastewater treatment system |
| CN106673303A (en) * | 2016-12-20 | 2017-05-17 | 天津膜天膜科技股份有限公司 | Multi-effect and energy-saving bio-contact oxidation process |
| CN108203179A (en) * | 2017-11-01 | 2018-06-26 | 北京贝特斯联合科技有限公司 | A kind of intelligence fast sewage treatment device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2078057C1 (en) * | 1994-03-02 | 1997-04-27 | Научно-производственное объединение по сельскохозяйственному использованию сточных вод "Прогресс" | Biological oxidational contact stabilizing pond |
| CN102874984A (en) * | 2012-10-15 | 2013-01-16 | 天津工业大学 | Short-distance regenerated water treatment and reuse device |
| CN104230092A (en) * | 2013-06-07 | 2014-12-24 | 湖南永清环保研究院有限责任公司 | Technological system for urban domestic sewage treatment and synchronous sludge reduction near-zero emission |
| CN205473179U (en) * | 2015-12-31 | 2016-08-17 | 天津汉晴环保科技有限公司 | Integrate sewage treatment system |
-
2015
- 2015-12-31 CN CN201511034488.0A patent/CN105461176A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2078057C1 (en) * | 1994-03-02 | 1997-04-27 | Научно-производственное объединение по сельскохозяйственному использованию сточных вод "Прогресс" | Biological oxidational contact stabilizing pond |
| CN102874984A (en) * | 2012-10-15 | 2013-01-16 | 天津工业大学 | Short-distance regenerated water treatment and reuse device |
| CN104230092A (en) * | 2013-06-07 | 2014-12-24 | 湖南永清环保研究院有限责任公司 | Technological system for urban domestic sewage treatment and synchronous sludge reduction near-zero emission |
| CN205473179U (en) * | 2015-12-31 | 2016-08-17 | 天津汉晴环保科技有限公司 | Integrate sewage treatment system |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105800855A (en) * | 2016-05-25 | 2016-07-27 | 王杨 | Community domestic wastewater treatment device |
| CN105819631A (en) * | 2016-05-25 | 2016-08-03 | 王杨 | Municipal wastewater treatment system |
| CN106673303A (en) * | 2016-12-20 | 2017-05-17 | 天津膜天膜科技股份有限公司 | Multi-effect and energy-saving bio-contact oxidation process |
| CN108203179A (en) * | 2017-11-01 | 2018-06-26 | 北京贝特斯联合科技有限公司 | A kind of intelligence fast sewage treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104528932B (en) | A kind of advanced treatment of wastewater denitrification bio-filter apparatus system and process technique | |
| CN102249491B (en) | Deep treatment device and process for secondary treatment effluent of urban sewage plant | |
| CN106277558A (en) | A kind of integrate process for removing nitrogen and phosphor from sewage and the device that physical biochemistry filters | |
| CN101219847A (en) | Integrated water purification processing method and device of ultrafiltration membrane coagulation/bioreactor | |
| CN104829056A (en) | Integrated sewage treatment apparatus, and sewage treatment process flow using apparatus | |
| CN107151053A (en) | A kind of aerobic membrane module processing unit of anoxic anaerobic/anoxic | |
| CN206127067U (en) | Container formula sludge -biofilm intergrowth integrative sewage treatment device | |
| CN105461176A (en) | Integrated system for treating domestic sewage | |
| CN107473378A (en) | The aerobic membrane module processing method of anoxic anaerobic/anoxic | |
| CN104045205A (en) | Low-power-consumption integrated water purifying apparatus and water purifying method | |
| CN205473179U (en) | Integrate sewage treatment system | |
| CN201834830U (en) | Integrated sewage treatment device | |
| CN205773629U (en) | A kind of high ammonia nitrogen sewage treatment unit | |
| CN108996827B (en) | Sewage plant tail water deep denitrification device based on methane oxidation | |
| CN103193360B (en) | Nitrogen and phosphorus removal integrated biological aerated filter water purification system and water purification method thereof | |
| CN204588956U (en) | A kind of low turbidity micro-polluted surface water advanced treatment apparatus | |
| CN207405026U (en) | Sewage treating and recovering device | |
| CN103819048A (en) | Complete field camp domestic sewage treatment device and method | |
| CN206562380U (en) | A kind of unpowered sewage complex biological processing integrated apparatus | |
| CN105417870A (en) | Downward-flow zero-valent-iron-fenton-like and biological-filter integrating wastewater treatment technology and device | |
| CN202099169U (en) | Device for advanced treatment of secondary effluent in municipal sewage plant | |
| CN206940544U (en) | A30+MBR processing units | |
| CN106430846A (en) | Efficient treatment integrated process for recalcitrant wastewater with low organic matter content | |
| CN105693036A (en) | Intelligent sewage treatment system | |
| CN205953787U (en) | Printing and dyeing wastewater advanced treatment unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160406 |
|
| RJ01 | Rejection of invention patent application after publication |