CN104478158A - Sewage treatment method - Google Patents
Sewage treatment method Download PDFInfo
- Publication number
- CN104478158A CN104478158A CN201410648456.9A CN201410648456A CN104478158A CN 104478158 A CN104478158 A CN 104478158A CN 201410648456 A CN201410648456 A CN 201410648456A CN 104478158 A CN104478158 A CN 104478158A
- Authority
- CN
- China
- Prior art keywords
- sewage
- water
- treatment
- anaerobic
- sludge
- 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
- 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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/123—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
-
- 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
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
- C02F3/02—Aerobic processes
-
- 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
- C02F3/28—Anaerobic digestion processes
-
- 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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/341—Consortia of bacteria
Abstract
The invention discloses a sewage treatment method, large floating objects in sewage are removed by a coarse grille in a plant, then the sewage flows into a water collecting pool; the sewage is lifted to a combined rotating fine grille with smaller mesh than that of the coarse grille by a vertical sewage pump, debris and sand are separated from the sewage by the combined rotating fine grille; effluent treated by the rotating fine grille enters into an anaerobic tank, flowing-in water is mixed with anaerobic sludge for anaerobic treatment; the anaerobically treated sewage flows into a biochemical pool, a compound bacteria agent is first added when the anaerobically treated sewage flows into the biochemical pool, a catenary aerator is used for oxygenation by aeration for aerobic treatment, the treated sewage is precipitated and then aerated for oxygenation for stabilization, the sewage flows automatically into a disinfection pool, and after the disinfection, the sewage is discharged. The sewage treatment method has the advantages of low investment, high efficiency, large sludge recycle flow rate and simple process, in order to improve sewage treatment capacity, an effective microbial iinoculum is added in the running process, all kinds of pollutants can be effectively degraded, odor can be removed, and pollution load can be reduced.
Description
Technical field
The present invention relates to water harnessing field, particularly relate to a kind of sewage water treatment method.
Background technology
Along with the fast development of national economy, city size constantly expands the fast development with urbanization, and the total emission volumn of urban industry waste water and sanitary sewage also strengthens year by year.If undressed waste water, sewage directly enter natural water, not only can severe contamination river, river, lake, storehouse and underground water water quality, and can spread disease germs in a large number, virus, objectionable impurities and obnoxious flavour, affect the quality of life of the people and healthy.
In the face of the water crisis of pressing hard step by step, the environmental protection industry that municipal sewage treatment and water reuse have utilized technology, Industrial Wastewater Treatment and recycle industrial technology, water-saving technology and equipment to first develop as current national by the Chinese government and major fields.
In recent years, the construction of National urban sewage work progressively comes into one's own, and sewage work has included municipal capital construction in.But construction speed is unable to catch up with the needs of prevention and cure of pollution far away.
Current wastewater treatment in China mainly adopts aerobe to add membrane technology, i.e. AAOM technique.Because its construction investment is high, preparation of construction require high, run processing cost and management and maintenance costly, the problem that sludge yield is large, processing efficiency is low (being commonly called as " three high and one low " technique), cause wastewater treatment in China cause to be walked with difficulty, even occur the difficult situation that sewage work " afford to build, can not afford ".Therefore in the urgent need to developing efficient, practical, the economic urban wastewater treatment new technology being applicable to China's national situation.
Summary of the invention
For above-mentioned shortcoming and defect of the prior art, the object of the present invention is to provide that a kind of input cost is low, sludge yield is little and the sewage water treatment method that processing efficiency is high.
The object of the invention is to be achieved through the following technical solutions:
A kind of sewage water treatment method, first removes large floating matter through coarse rack by sewage, then flows into water collecting basin in factory; Sewage is promoted to the Assembled rotary fine fack little compared with coarse rack mesh through vertical sump pump, and Assembled rotary fine fack is separated foreign material and sand grains from waste water; Water outlet after rotating fine fack process enters anaerobic pond, by thruster, anaerobic treatment is carried out in water inlet and anaerobic sludge mixing; Sewage after anaerobic treatment flows into biochemistry pool, add when flowing into first with the composite fungus agent of the thread fungus group of photosynthetic bacteria group, lactobacillus, yeast flora, Gram positive actinomycetes group and fermentation composition, form probiotic bacterium flora, utilize the oxygenation of suspensive chain type aerator aeration to carry out aerobic treatment; Sewage after process, carry out aeration aerating after precipitation again and stablize, sewage self-flowing enters sterilization pool, discharge after sterilization.
Preferably, sludge thickener sent into by the mud sludge pump produced after precipitation, and mud is sent into belt filter press by spiral pump again and dewatered after concentrated; The supernatant liquor that sludge thickener produces and the filtrate that pressure filter produces are from flowing into water collecting basin secondary treatment.
Preferably, the oxygen needed in aeration and clarifying process is supplied by blower fan.
Compared with prior art, the embodiment of the present invention at least has the following advantages:
In the embodiment of the present invention, the investment of this sewage water treatment method is low, efficiency height sludge reflux amount is large, technique is simple, for improving sewage treatment capacity, effective microbe microbial inoculum is added in operational process, can effectively degrade each pollutant, removing stink, lowers pollution load.Microorganism can run under normal temperature, normal pressure, and not only energy consumption is low, outlet effect is good, and does not have secondary pollution.Effluent quality reaches the secondary water quality standard of GB8979-96, and process can consider reuse further.
Embodiment
Below in conjunction with embodiment, the invention will be further described, and following examples are descriptive, is not determinate, can not limit protection scope of the present invention with this.
Sewage is first removed large floating matter through coarse rack in factory, then from flowing into water collecting basin.Sewage is promoted to Assembled rotary fine fack through vertical sump pump, and Assembled rotary fine fack can be separated foreign material and sand grains from waste water, can remove a part of organic loading simultaneously.Rotate fine fack process water outlet and be introduced into anaerobic pond, by thruster, anaerobic treatment is carried out in water inlet and anaerobic sludge mixing, then from flowing into biochemistry pool, adding our the effective microbe microbial inoculum of exploitation during first operation (is with photosynthetic bacteria group, lactobacillus, yeast flora, the 5 large classes 10 such as the thread flora of Gram positive actinomycetes group and fermentation belong to the composite fungus agent that more than 80 plant microorganism composition, thus powerful probiotic bacterium flora is formed, by oxidation, reduction, the approach such as fermentation, decompose oxidation of organic compounds, can degradation of organic substances effectively, suppress, kill various unwanted bacteria, suppress the propagation of prevailing disease pathogenic microorganism, the common peculiar smell such as removal of hydrogen sulfide and ammonia, play the effect of environmental protect), the oxygenation of suspensive chain type aerator aeration is utilized to carry out aerobic treatment, sewage after process, carry out aeration aerating after precipitation again to stablize, sewage self-flowing enters sterilization pool, discharge after sterilization.Sludge thickener sent into by the mud sludge pump that precipitation produces, and mud to be made a gift to someone belt filter press dehydration by spiral pump after concentrated again.The supernatant liquor that sludge thickener produces and the filtrate that pressure filter produces are from flowing into water collecting basin secondary treatment.The oxygen that aeration and clarifying process need is supplied by blower fan, the mechanical foreign material outward transport landfill stabilization that pre-treatment facility produces, and the excess sludge outward transport of generation is fertile as agriculture.
The process characteristic of this sewage water treatment method:
Invest low: owing to adopting Tu Chi to add seepage control measure, the construction cost of water per ton is greatly about about 800 ~ 1000 yuan, and the construction cost of AAOM technique water per ton is about 3000 ~ 3200 yuan.So expense is significantly less than the construction cost of other process spent water treatment plants needed for water treatment method in the present invention.Also there is floor space in addition little, arrange with suiting measures to local conditions, not by the influence of topography.
According to State Bureau of Environmental Protection 1992 " investigation and research of Industrial Wastewater Treatment facility ", China's Industrial Wastewater Treatment facility fund 54% for civil engineering facility, and only have 36% for equipment, cause the major cause of this Investment Allocation general layout to be that process pool mostly adopts expensive steel reinforced concrete pool.And imperial field Sewage Plant civil engineering cost, only account for 20% of gross investment.Large steel reinforced concrete pool is not only expensive, and difficulty of construction is large.In order to reduce investment, first the aeration tank adopted in the present invention is use HDPE anti seepage membrane to completely cut off sewage and underground water, is secondly that the micro porous aeration head be suspended in float tube avoids pool wall perforation installation at the bottom of pond.The Tu Chi of this HDPE of laying anti seepage membrane is not only easy to excavation, low investment, and treatment tank requirement functionally can be met completely, and can suit measures to local conditions, adapt to on-the-spot landform admirably, under depositing some special geologic condition, as earthquake prone areas, the soil is porous area, its advantage is embodied more fully.Lay native pond work-ing life of HDPE anti seepage membrane considerably beyond steel reinforced concrete pool.
Efficiency is high: utilize the floating aerating chain system of keeping afloat, micro porous aeration head is arranged at bottom, and aeration efficiency is high.Aerator is arranged on pool side, and energy consumption is little.Energy consumption is only about 1/2 ~ 1/3 of traditional wastewater process.
Traditional wastewater process seldom adopts underload Sludge System, this is because not efficient, and rational technique and aerator.The development of C-BIOLAK aerator (BIoLAK mono-FluoX), for we be familiar with already and the utilization obtaining this technique of certain effect opens more great scope of land.The power consumption in the system aeration tank of C-BIOLAK aerator needed for mixing effect is adopted to be only 1.5 watts/m
3, and in general traditional aeration method, the power consumption of mixing effect is 10 ~ 15 watts/m
3, this very valuable improvement beyond doubt.
Sludge reflux amount is large: in operational process, and the mud of 30 ~ 40%, by microbial consumption, separately has the sludge reflux process of 30 ~ 40%, excess sludge is 20 ~ 30% energy long storage time without putrefactions of traditional technology, do not produce stink, through storage pool mummification, can agricultural fertilizer be done.C-BIOLAK process sludge quantity of reflux is large, and sludge concentration is higher, and biomass is large, and relative aeration time is longer, so sludge loading is lower.
Technique is simple: this technique starts fast, operation, management, easy to maintenance, and after stable, the working cost of sewage per ton is lower, is about 1/3 ~ 1/4 of traditional method.Emptying or stopping production is not needed during maintenance.Due to the structure that C-BIOLAK micro-hole aerator (BloLAK mono-FluoX) is special, both aerator in very complex environment had been made also to be unlikely to block, this means that aerating apparatus can run several years and not keep in repair, decrease the workload of maintenance, so need maintenance cost little.C-BIOLAK technique is by a large amount of returned sluge, and its excess sludge reduces a lot than traditional technology.Before use mud, no longer need any process, therefore, the expense of flower on lignin-sludge is also very low.
C-BIOLAK system does not have fixing part under water, need not drain the water in pond, and mentioned by the aeration head under aerator chain to repair location with canoe during maintenance.Practice shows, aeration head runs several years and also need not anyly keep in repair, and this mainly because aeration tube is made by very thin fiber (diameter is about 0.003mm), and uses polymkeric substance filling, to reach the object of waterproof and anti-foul.Meanwhile, aeration head has the free space of about 80% and the surface of 20%, and traditional aeration head is just contrary.Therefore, the area that microorganism can grow is very little, and is easy to be removed.When aeration head must keep in repair, do not affect the operation in whole sewage farm yet.Moving-member and the easy ageing component of this technique are all little.When the equipment of selection and material, all have employed reliability and durability material.This technique is without the need to too many automatization.It is both without any need for the detector of rapid wear, also without any need for the Controlling System of complexity.
For improving sewage treatment capacity, add effective microbe microbial inoculum, each pollutant of can effectively degrading in operational process, removing stink, lowers pollution load.Microorganism can run under normal temperature, normal pressure, and not only energy consumption is low, outlet effect is good, and does not have secondary pollution.Effluent quality reaches the secondary water quality standard of GB8979-96, and process can consider reuse further.
The above; be only the present invention's preferably embodiment, but protection scope of the present invention is not limited thereto, is anyly familiar with those skilled in the art in the technical scope that the present invention discloses; the change that can expect easily or replacement, all should be encompassed within protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with the protection domain of claims.
Claims (3)
1. a sewage water treatment method, is characterized in that, comprises successively by step:
S1, first removes large floating matter through coarse rack by sewage, then flows into water collecting basin in factory;
S2, sewage is promoted to the Assembled rotary fine fack little compared with coarse rack mesh through vertical sump pump, and Assembled rotary fine fack is separated foreign material and sand grains from waste water;
S3, the water outlet after rotating fine fack process enters anaerobic pond, by thruster, anaerobic treatment is carried out in water inlet and anaerobic sludge mixing;
S4, sewage after anaerobic treatment flows into biochemistry pool, add when flowing into first with the composite fungus agent of the thread fungus group of photosynthetic bacteria group, lactobacillus, yeast flora, Gram positive actinomycetes group and fermentation composition, form probiotic bacterium flora, utilize the oxygenation of suspensive chain type aerator aeration to carry out aerobic treatment;
S5, the sewage after process, carry out aeration aerating after precipitation again and stablize, sewage self-flowing enters sterilization pool, discharge after sterilization.
2. sewage water treatment method according to claim 1, is characterized in that, the sewage in S5 produces mud after precipitation, and sludge thickener sent into by the mud sludge pump of generation, and mud is sent into belt filter press by spiral pump again and dewatered after concentrated; The supernatant liquor that sludge thickener produces and the filtrate that pressure filter produces are from flowing into water collecting basin secondary treatment.
3. sewage water treatment method according to claim 1 and 2, is characterized in that, the oxygen needed in aeration and clarifying process is supplied by blower fan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410648456.9A CN104478158A (en) | 2014-11-17 | 2014-11-17 | Sewage treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410648456.9A CN104478158A (en) | 2014-11-17 | 2014-11-17 | Sewage treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104478158A true CN104478158A (en) | 2015-04-01 |
Family
ID=52752799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410648456.9A Pending CN104478158A (en) | 2014-11-17 | 2014-11-17 | Sewage treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104478158A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293765A (en) * | 2015-10-26 | 2016-02-03 | 北京东方协和医药生物技术有限公司 | Domestic wastewater treatment fundamental technology |
| CN105601046A (en) * | 2016-03-10 | 2016-05-25 | 蒋安美 | Domestic sewage treatment method |
| CN106946389A (en) * | 2017-03-31 | 2017-07-14 | 陈来胜 | A kind of sewage-treatment plant |
| CN107777833A (en) * | 2016-08-29 | 2018-03-09 | 江苏众胜灭菌设备科技有限公司 | A kind of sewage water treatment method |
| CN108191190A (en) * | 2017-12-30 | 2018-06-22 | 山东中荣生物科技有限公司 | A kind of sewage treatment plant's biochemical system mud decrement method |
| CN108298681A (en) * | 2018-04-12 | 2018-07-20 | 南京林业大学 | Light intensity energy-saving sewage treating device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2144517C1 (en) * | 1999-05-05 | 2000-01-20 | Камайданов Евгений Николаевич | Method and plant for treatment of sewage |
| CN2737787Y (en) * | 2004-05-24 | 2005-11-02 | 北京科技大学 | Sewage treatment apparatus with swinging aeration head |
| US20110127214A1 (en) * | 2008-02-15 | 2011-06-02 | Rico Martinez Mauricio | Energy optimization in an anaerobic, facultative, anoxic aerobic plant, using fine bubbles, without sludge production |
| CN102173529A (en) * | 2010-11-30 | 2011-09-07 | 福建凤竹纺织科技股份有限公司 | Deodorization method in treatment of printing and dyeing wastewater |
| CN203440210U (en) * | 2013-09-12 | 2014-02-19 | 江苏和顺环保股份有限公司 | Wastewater treatment system for pharmaceutical factory |
-
2014
- 2014-11-17 CN CN201410648456.9A patent/CN104478158A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2144517C1 (en) * | 1999-05-05 | 2000-01-20 | Камайданов Евгений Николаевич | Method and plant for treatment of sewage |
| CN2737787Y (en) * | 2004-05-24 | 2005-11-02 | 北京科技大学 | Sewage treatment apparatus with swinging aeration head |
| US20110127214A1 (en) * | 2008-02-15 | 2011-06-02 | Rico Martinez Mauricio | Energy optimization in an anaerobic, facultative, anoxic aerobic plant, using fine bubbles, without sludge production |
| CN102173529A (en) * | 2010-11-30 | 2011-09-07 | 福建凤竹纺织科技股份有限公司 | Deodorization method in treatment of printing and dyeing wastewater |
| CN203440210U (en) * | 2013-09-12 | 2014-02-19 | 江苏和顺环保股份有限公司 | Wastewater treatment system for pharmaceutical factory |
Non-Patent Citations (3)
| Title |
|---|
| 何强等: "《细部小城镇污水处理设施建设技术指南》", 30 September 2011 * |
| 李桂平: "某工业园区污水处理厂设计", 《工业水处理》 * |
| 环境保护部污染物排放总量控制司组织编写: "《城镇分散型水污染物减排实用技术汇编》", 31 January 2009 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293765A (en) * | 2015-10-26 | 2016-02-03 | 北京东方协和医药生物技术有限公司 | Domestic wastewater treatment fundamental technology |
| CN105601046A (en) * | 2016-03-10 | 2016-05-25 | 蒋安美 | Domestic sewage treatment method |
| CN107777833A (en) * | 2016-08-29 | 2018-03-09 | 江苏众胜灭菌设备科技有限公司 | A kind of sewage water treatment method |
| CN106946389A (en) * | 2017-03-31 | 2017-07-14 | 陈来胜 | A kind of sewage-treatment plant |
| CN108191190A (en) * | 2017-12-30 | 2018-06-22 | 山东中荣生物科技有限公司 | A kind of sewage treatment plant's biochemical system mud decrement method |
| CN108298681A (en) * | 2018-04-12 | 2018-07-20 | 南京林业大学 | Light intensity energy-saving sewage treating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101928097B (en) | Domestic sewage treatment system for ecological residential quarter | |
| CN104478158A (en) | Sewage treatment method | |
| CN102249478B (en) | Deep nitrogen and phosphorus removal process for surface water body | |
| CN102276110B (en) | Method for remedying micro-polluted water body and subsurface flow artificial wetland system | |
| CN104528931A (en) | Biological aerated filter using barley straws as substrate and application thereof | |
| CN201485358U (en) | Ecological treatment system of domestic sewage | |
| CN201864641U (en) | Housing estate domestic sewage ecological treatment system | |
| CN103819052B (en) | A kind of animal farm wastewater Zero discharging system | |
| CN104787958A (en) | Culturing farm sewage treatment system, and sewage treatment method | |
| CN101164924A (en) | Countryside sewage treatment equipment and application | |
| CN101905925B (en) | Method for treating dispersed domestic sewage in rural areas by using sequencing batch mineralized waste wetland bed | |
| CN107827324B (en) | Urban sewage comprehensive treatment system | |
| CN110790451A (en) | Black odorous water treatment system and method for treating black odorous water by using same | |
| CN1789173A (en) | Method for treating leachate in domestic refuses landfill site by tower type aged-refuse bioreactor | |
| CN103723892B (en) | Livestock and poultry wastewater treatment system and treatment method using system | |
| CN105461167A (en) | Ecological landscape type integrated garbage and sewage treatment system for villages and small towns | |
| CN102515434A (en) | Method for sewage treatment in compound tower-type ecological filtering pool | |
| CN105084555A (en) | Water body pollution treatment method taking microbiological method as main body | |
| CN201473421U (en) | Buried non-sludge integrated sewage treatment device | |
| CN104016546B (en) | Environment-friendly artificial wetland system for purifying dredging remained water/tail water | |
| CN103304029A (en) | Artificial soil infiltration system for treating rural distributed sewage | |
| CN105236575B (en) | It is a kind of that stream process is made using circulation and repairs the device and method of polluted-water | |
| CN205133243U (en) | Adopt circulation to make class processing and repair device that pollutes water | |
| CN211644985U (en) | Brewing production wastewater purification ecological system | |
| CN2818472Y (en) | In situ composite reaction treater for domestic and fecal sewage |
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: 20150401 |
|
| RJ01 | Rejection of invention patent application after publication |