CN205061784U - Treatment of domestic sewage recycling system - Google Patents
Treatment of domestic sewage recycling system Download PDFInfo
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- CN205061784U CN205061784U CN201520059257.4U CN201520059257U CN205061784U CN 205061784 U CN205061784 U CN 205061784U CN 201520059257 U CN201520059257 U CN 201520059257U CN 205061784 U CN205061784 U CN 205061784U
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- contact oxidation
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model relates to a treatment of domestic sewage recycling system. Including the equalizing basin, the anaerobism pond, the oxygen deficiency pond, the elevator pump, biological catalytic oxidation system, MBR film reaction system, the self priming pump, the clean water basin, the retrieval and utilization pump, wherein the equalizing basin is equipped with the domestic sewage entry, the delivery port of equalizing basin communicates with each other with the water inlet in anaerobism pond, the delivery port in anaerobism pond communicates with each other with the water inlet in oxygen deficiency pond, water in the oxygen deficiency pond passes through the elevator pump and promotes to biological catalytic oxidation system, the delivery port of biological catalytic oxidation system communicates with each other with the water inlet of MBR film reaction system, water in the MBR film reaction system is taken out to the clean water basin through the self priming pump, water in the clean water basin passes through retrieval and utilization pump exhausting to water department. The utility model discloses throughput is strong, solid -liquid separation is efficient, go out that water quality of water is good, to take up an area of the space little, and compact structure, the working property is reliable and stable, operation maintenance is convenient.
Description
Technical field
The utility model is one way of life waste water treating and reutilizing system, belongs to the innovative technology of life sewage treatment and reuse system.
Background technology
Along with urban construction and industrial expansion, on the one hand, the demand of people to water strengthens day by day, and on the other hand, to the destructiveness of water resources more and more seriously, the situation causing shortage of water resources thus is constantly aggravated for the life of the mankind and activity in production.Urban water consumption and water displacement constantly increase, and cause city water resource worsening shortages.
Based on the principle to water resources available protecting and Appropriate application, the reuse dynamics of various dirt (giving up) water should be strengthened, to alleviate the shortage of city water resource, protection water surrounding.
Summary of the invention
The purpose of this utility model is consider the problems referred to above and provide the life sewage treatment and reuse system that a kind of processing power is strong, solid-liquid separation efficiency is high, effluent quality is good, occupation of land space is little.The utility model compact construction, stable and reliable working performance, convenient operating maintenance.
The technical solution of the utility model is: life sewage treatment and reuse system of the present utility model, include equalizing tank, anaerobic pond, anoxic pond, lift pump, bio-contact oxidation system, MBR film reaction system, vacuum primingpump, clean water basin, reuse pump, wherein equalizing tank is provided with sanitary sewage entrance, the water outlet of equalizing tank communicates with the water inlet of anaerobic pond, the water outlet of anaerobic pond communicates with the water inlet of anoxic pond, water in anoxic pond is promoted to bio-contact oxidation system by lift pump, the water outlet of bio-contact oxidation system communicates with the water inlet of MBR film reaction system, the intrasystem water of MBR film reaction is evacuated to clean water basin by vacuum primingpump, water in clean water basin is evacuated to by reuse pump and uses water place.
The utility model includes the structure of equalizing tank, anaerobic pond, anoxic pond, lift pump, bio-contact oxidation system, MBR film reaction system owing to adopting, sewage water outlet after treatment reaches zero-emission sea, all can be used as greening, sweep ground, landscape water moisturizings etc., effluent quality reaches urban sewage reutilization urban reclaimed water water quality and urban sewage reutilization water for scenic environment use water quality.The utility model processing power is strong, solid-liquid separation efficiency is high, effluent quality is good, occupation of land space is little, and compact construction, aesthetic in appearance, stable and reliable working performance, convenient operating maintenance, the utility model is that a kind of design is ingenious, excellent property, convenient and practical life sewage treatment and reuse system.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Embodiment
Embodiment:
Schematic diagram of the present utility model as shown in Figure 1, life sewage treatment and reuse system of the present utility model, include equalizing tank, anaerobic pond, anoxic pond, lift pump, bio-contact oxidation system, MBR film reaction system, vacuum primingpump, clean water basin, reuse pump, wherein equalizing tank is provided with sanitary sewage entrance, the water outlet of equalizing tank communicates with the water inlet of anaerobic pond, the water outlet of anaerobic pond communicates with the water inlet of anoxic pond, water in anoxic pond is promoted to bio-contact oxidation system by lift pump, the water outlet of bio-contact oxidation system communicates with the water inlet of MBR film reaction system, the intrasystem water of MBR film reaction is evacuated to clean water basin by vacuum primingpump, water in clean water basin is evacuated to by reuse pump and uses water place.
In the present embodiment, above-mentioned bio-contact oxidation system is provided with biological contact oxidation equipment.
In the present embodiment, above-mentioned biological contact oxidation equipment is polyfunctional reactant unit, and polyfunctional reactant unit comprises removes BOD, nitration reaction and absorption phosphorus reaction unit.
In the present embodiment, above-mentioned MBR film reaction system is provided with membrane reactor.
In the present embodiment, above-mentioned bio-contact oxidation system and MBR film reaction system are provided with Aeration fan.
In the present embodiment, the pipeline that above-mentioned vacuum primingpump draws water to clean water basin is provided with sterilisation system.The pipeline that vacuum primingpump draws water to clean water basin is provided with sterilisation system.
Sanitary sewage enters equalizing tank regulating pondage, balanced water quality, more successively through anaerobic pond and anoxic pond, utilizes that anerobe makes organism be hydrolyzed, acidifying in anaerobic pond, removes dirty Organic substance in water and discharges phosphorus; Anoxic pond carries out denitrification denitrogenation, rise to bio-contact oxidation system by lift pump afterwards and carry out aeration, the intrasystem biological contact oxidation equipment of bio-contact oxidation is polyfunctional reactant unit, removes BOD, nitration reaction and absorption phosphorus etc. and occurs all herein.Reuse standard is reached for making effluent quality, water after biological contact oxidization treatment enters MBR film reaction system again, and the intrasystem membrane reactor of MBR film reaction, because of its effective crown_interception, can retain the microorganism that life cycle is longer, further denitrogenation dephosphorizing, realizes the deep purifying of sewage.Water after purification is sterilized through sterilisation system, and is evacuated to clean water basin by vacuum primingpump, and the water in clean water basin is evacuated to by reuse pump and uses water place.Sanitary sewage can all afforest as this district, sweep ground, landscape water moisturizing etc. after treatment.
Living quarters sanitary sewage every day total amount is about 100m3, every day, system operation time was 20h, the Project design water yield is 5m3/h, the utility model adopts bio-contact oxidation+film process MBR technique+sterilization, after process, water outlet reaches zero-emission sea, all afforest as this district, sweep ground, landscape water moisturizings etc., effluent quality reaches " urban sewage reutilization urban reclaimed water water quality " (GB/T18920-2002) and " urban sewage reutilization water for scenic environment use water quality " (GB/T18921-2002).
Above-mentioned bio-contact oxidation is a kind of biological sewage treatment method derived from from biomembrance process, namely in biological contact oxidation pond, load the filler of some amount, utilizing dwells is attached to the oxygen of microbial film on filler and ample supply, pass through biological oxidation, oxidation operation in waste water is decomposed, reaches purification object.
Biological contact oxidation process is the microbial film be attached on carrier (being commonly called as filler) is main, a kind of High-efficient Water treatment process of purification of organic waste water.There is the biomembrance process of activated sludge process feature, have the advantage of activated sludge process and biomembrance process concurrently.Can under biochemical condition, no matter be applied to the process of trade effluent or aquaculture wastewater, sanitary sewage, all achieve good economic benefit.This technique is because having the features such as energy-efficient, floor space is little, anti impulsion load, operational management are convenient.
Biological treatment is through the link after materializing strategy, also be the important step in whole circulation process, here the objectionable impurities such as ammonia/nitrogen, nitrous acid, nitrate, thiocyanogen all will be removed, and will play a key effect to the further process of water quality in later flow process.
Membrane Bio-reactor Technology is a kind of high-efficiency sewage treatment process combined with membrane separation technique of carrying out a biological disposal upon.Due to the application of film, substantially increase the water quality standard of process water outlet, comparatively meet the development trend that Treated sewage reusing purposes requires.In view of this trend, in nearly 2 years of membrane Bio-reactor Technology water in small-scale sewage process and urban architecture (bath wastewater is former water), application is more and more, has greatly the trend of the Biological Contact Oxidation Process replacing dominate nearly ten years.
Membrane bioreactor (MembranceBioreacter, MBR) is the biochemical reaction system be integrated in one by the biological degradation of membrane separation technique and bio-reactor.Membrane separation technique is physical processing techniques conventional in sewage treatment area, and its mechanism mainly sieve effect, according to different film surface apertures sizes, can be divided into filtration, micro-filtration (MF), ultrafiltration (UF) and nanofiltration (NF) etc.What usually adopt in membrane bioreactor is micro-filtration and ultra-filtration membrane, its separating mechanism mainly sieve effect, and because of the difference of membrane structure, crown_interception can be divided into mechanical retention substantially, absorption retains and bridging action etc.This technique has the features such as processing power is strong, solid-liquid separation efficiency is high, effluent quality is good, occupation of land space is little, operational management is simple.
At present, MBR Technology process sanitary sewage and trade effluent highlight effect.Membrane module is the core of MBR, what adopt is immersed flat plate membrane biologic reaction equipment, the unique aeration tube of plate film assembly configuration through optimizing, aeration is enable to act on flat sheet membrane surface equably, farthest increase oxygen transfer efficiency, reduce the impact of concentration difference polarization, except having compact construction, aesthetic in appearance, reliable and stable, outside the advantages such as convenient operating maintenance, also there is better antifouling property, good mechanical stability, without fracture of wire phenomenon, purging method is more convenient, cleaning interval is longer, life-span is long, working cost is low, the advantages such as film Renewal process is simple.
Claims (6)
1. one way of life waste water treating and reutilizing system, it is characterized in that including equalizing tank, anaerobic pond, anoxic pond, lift pump, bio-contact oxidation system, MBR film reaction system, vacuum primingpump, clean water basin, reuse pump, wherein equalizing tank is provided with sanitary sewage entrance, the water outlet of equalizing tank communicates with the water inlet of anaerobic pond, the water outlet of anaerobic pond communicates with the water inlet of anoxic pond, water in anoxic pond is promoted to bio-contact oxidation system by lift pump, the water outlet of bio-contact oxidation system communicates with the water inlet of MBR film reaction system, the intrasystem water of MBR film reaction is evacuated to clean water basin by vacuum primingpump, water in clean water basin is evacuated to by reuse pump and uses water place.
2. life sewage treatment and reuse system according to claim 1, is characterized in that above-mentioned bio-contact oxidation system is provided with biological contact oxidation equipment.
3. life sewage treatment and reuse system according to claim 2, is characterized in that above-mentioned biological contact oxidation equipment is polyfunctional reactant unit, and polyfunctional reactant unit comprises removes BOD, nitration reaction and absorption phosphorus reaction unit.
4. life sewage treatment and reuse system according to claim 1, is characterized in that above-mentioned MBR film reaction system is provided with membrane reactor.
5. the life sewage treatment and reuse system according to any one of Claims 1-4, is characterized in that above-mentioned bio-contact oxidation system and MBR film reaction system are provided with Aeration fan.
6. life sewage treatment and reuse system according to claim 5, is characterized in that the pipeline that above-mentioned vacuum primingpump draws water to clean water basin is provided with sterilisation system.
Priority Applications (1)
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CN201520059257.4U CN205061784U (en) | 2015-01-28 | 2015-01-28 | Treatment of domestic sewage recycling system |
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CN201520059257.4U CN205061784U (en) | 2015-01-28 | 2015-01-28 | Treatment of domestic sewage recycling system |
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CN201520059257.4U Expired - Fee Related CN205061784U (en) | 2015-01-28 | 2015-01-28 | Treatment of domestic sewage recycling system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105800882A (en) * | 2016-05-09 | 2016-07-27 | 宁波淳源环保科技有限公司 | Recycled water reuse system |
CN106630411A (en) * | 2016-12-14 | 2017-05-10 | 嘉工集团有限公司 | Domestic sewage treatment system and control method |
CN107176749A (en) * | 2016-03-11 | 2017-09-19 | 浙江国清环保科技有限公司 | Integral continuous Fenton oxidation-reduction sewage disposal device |
CN110117139A (en) * | 2019-06-19 | 2019-08-13 | 云南中贸环境节能科技投资股份有限公司 | A kind of bis- film Two-way Cycle sewage treatmentmethods of IBO |
-
2015
- 2015-01-28 CN CN201520059257.4U patent/CN205061784U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107176749A (en) * | 2016-03-11 | 2017-09-19 | 浙江国清环保科技有限公司 | Integral continuous Fenton oxidation-reduction sewage disposal device |
CN105800882A (en) * | 2016-05-09 | 2016-07-27 | 宁波淳源环保科技有限公司 | Recycled water reuse system |
CN106630411A (en) * | 2016-12-14 | 2017-05-10 | 嘉工集团有限公司 | Domestic sewage treatment system and control method |
CN110117139A (en) * | 2019-06-19 | 2019-08-13 | 云南中贸环境节能科技投资股份有限公司 | A kind of bis- film Two-way Cycle sewage treatmentmethods of IBO |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160302 Termination date: 20170128 |