CN1279214A - Process for treating sewage - Google Patents
Process for treating sewage Download PDFInfo
- Publication number
- CN1279214A CN1279214A CN99113073A CN99113073A CN1279214A CN 1279214 A CN1279214 A CN 1279214A CN 99113073 A CN99113073 A CN 99113073A CN 99113073 A CN99113073 A CN 99113073A CN 1279214 A CN1279214 A CN 1279214A
- Authority
- CN
- China
- Prior art keywords
- activated
- water
- activated sludge
- tank
- biofiler
- 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.)
- Granted
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Abstract
A process integrating active sludge with flowing-up active biological filter pool for treating sewage includes such steps as pretreating sewage in primary deposition pool, pumping it into active sludge pool (aerating pool) for adsorption, biological membrane treating in active biological filter pool, separating liquid from solid in deposition pool, discharging the treated water, and backflushing the active biological filter pool by starting back-flushing pump via electromagnetic valve with part of discharged water in collecting pool. Its advantages include less possessed ground, low energy consumption and high water quality.
Description
The present invention relates to the biochemical treatment of waste water, specifically a kind of active sludge and the incorporate sewage treatment process of upflowing biological filter process.
In the prior art, the biological treatment of traditional sewage aerobic comprises two big class basic skills, i.e. activated sludge process and biological filter process, and wherein activated sludge process is the technology of commonplace employing.Since first activated sludge process sewage work operation in 1914, developed out the kinds of processes form at present.Aspect technical process, develop into continuous operation from intermittent operation, develop into complete hybrid mode from the plug-flow mode; Aspect operating parameter, embody selection to sludge loading, and the expansion of sewage quality and concentration of wastewater scope.According to the different requirements of clearance, can select underload, often load and different load range such as high loading for use.There is high-efficiency bio-filter pool the biological filter, quickens various ways such as biological filter, tower biological filter with development at present behind nozzle-type water distribution biological filter in 1893.No matter be activated sludge process, or biological filter process, it is big all to exist floor space, the problem that operation energy consumption is high.The two-part treatment process of using has absorption-biological degradation technology (AB method) at present, biological filter-activated sludge process (ABF method), though the processing efficiency of above-mentioned two kinds of technologies is than higher, but effluent quality is difficult to reach higher standard, therefore it is higher only to be suitable for concentration of treatment, the less demanding sewage of water outlet.
In order to overcome above-mentioned deficiency, it is little to the invention provides a kind of floor space, and energy consumption is low, and water quality is good, active sludge and the incorporate sewage treatment process of upflowing activated biofiler method.
To achieve these goals, technical scheme of the present invention is: active sludge and upflowing activated biofiler method are integrated, and concrete steps are:
After sewage carried out pre-treatment by preliminary sedimentation tank, entering activated sludge tank through sump pump was that the activated sludge absorption processing is carried out in the aeration tank, is the technology fs; Water after activated sludge absorption is handled enters activated biofiler and carries out the microbial film processing, is the technology subordinate phase; Enter settling tank then and carry out the solid-liquid separation processing, mud is separated; Will be through the discharging of the water after the mud separating treatment, wherein portion water enters water collecting basin, starts backwashing pump by magnetic valve activated biofiler is carried out back flushing;
Described activated biofiler is a upward flow, the disposable aeration of described activated sludge tank and activated biofiler; Adopt some water distributions or 2 water distribution manners, more described water distribution manner is provided with at the activated sludge tank place, and described 2 water distribution manners are to be provided with respectively at activated sludge tank and activated biofiler place.
The present invention has following advantage:
1. global design of the present invention is reasonable.Upward flow is adopted in the biological filter, and activated sludge tank and biological filter are integrated, two disposable aerations of reactor, and the activated sludge tank water outlet directly enters the biological filter, and making this filter tank is activated biofiler; This processing efficiency demonstrates the synergistic effect of combination, is higher than the processing power of single technology, and indexs such as effluent quality and working cost all are better than present various biochemical processing methods, but primary treatment reaches the reuse water water quality standard.
2. the present invention takes upward flow filtration, has: (1) gas, horizontal line stream make and bring about the desired sensation, water distributes equably, prevent that bubble from condensing, and improve oxygen utilization coefficient; (2) with opposite to flowing through filter down, upward flow filtration continues to provide positive pressure on the height of whole filter tank, can avoid forming air pocket, provides moving half favourable boost conditions; (3) gas, horizontal line stream can be utilized spatial filtering better, and can reduce the back flushing water yield and back washing strength.
3. the present invention is of many uses.It can be used for the processing of sanitary sewage, municipal wastewater, middle and high concentration organic industrial sewage.
Description of drawings:
Fig. 1 is a schema of the present invention.
Fig. 2 is apparatus of the present invention synoptic diagram.
Below in conjunction with accompanying drawing the present invention is described in further detail.
As shown in Figure 1, 2, activated sludge and up flow type activated biofiler method are integrated, and concrete steps are:
After sewage carried out preliminary treatment by preliminary sedimentation tank 1, entering activated sludge tank through sewage pump 2 and air pump 3 was aeration tank 4 Carry out activated sludge absorption and process, be the technology phase I; Water after activated sludge absorption is processed enters activity The biomembrane processing is carried out in biofilter 5, is the technology second stage; Enter then sedimentation basin 6 and carry out the Separation of Solid and Liquid processing, Mud is separated; With the discharging of the water after the mud separating treatment, wherein part water enters collecting-tank 7, passes through magnetic valve 8 start 9 pairs of activated biofilers of backwashing pump 4 carries out backwash;
Described activated biofiler 5 is upward flow, described activated sludge tank 4 and activated biofiler 5 disposable aerations; Adopt some water distributions or 2 water distribution manners, more described water distribution manner arranges at activated sludge tank 4 places, and described two The point water distribution manner is She Zhi not in addition at activated sludge tank 4 and activated biofiler 5 punishment.
After sewage carries out pre-treatment by preliminary sedimentation tank 1, enter activated sludge tank 4 through sump pump 2 and carry out the activated sludge absorption processing, be the technology fs, take some water distributions in activated sludge tank 4 places, the hydraulic detention time of activated sludge tank (AS) 41 hour, water after activated sludge absorption is handled enters 5 li of activated biofilers (UABF) and carries out microbial film and handle then, be the technology subordinate phase, hydraulic detention time at activated biofiler 5 is 3 hours, and it is 1.44 kgCOD/m that described AS/UABF on average removes the COD load
aD; Removing organic load is 0.93 kgBOD
5/ m
3D, the total clearance of the average COD of system is 94%, BOD
5Be 97%, SS clearance 96%, AS/UABF is to NH
3The clearance of-N is 95%.
Embodiment 2
After sewage carries out pre-treatment by preliminary sedimentation tank 1, enter activated sludge tank 4 through sump pump 2 and carry out the activated sludge absorption processing, be the technology fs, adopt 2 water distributions respectively at activated sludge tank 4 and activated biofiler 5 places, the hydraulic detention time of activated sludge tank (AS) 41 hour, water after activated sludge absorption is handled enters 5 li of activated biofilers (UABF) and carries out microbial film and handle then, be the technology subordinate phase, hydraulic detention time at activated biofiler 5 is 2.5 hours, and the COD of AS/UABF removes load and reaches by 2.04 kgCOD/m
3D, COD clearance are 92%, and the removal organic load is 1.40kgBOD
5/ m
3D, BOD clearance are 91%, SS clearance 94%, and AS/UABF is to NH
3The clearance of-N is 97%.
Claims (3)
1. sewage treatment process, it is characterized in that: active sludge and upflowing activated biofiler method are integrated, and concrete steps are:
After sewage carried out pre-treatment by preliminary sedimentation tank (1), entering activated sludge tank through sump pump (2) was that the activated sludge absorption processing is carried out in aeration tank (4), is the technology fs; Water after activated sludge absorption is handled enters activated biofiler (5) and carries out the microbial film processing, is the technology subordinate phase; Enter settling tank (6) then and carry out the solid-liquid separation processing, mud is separated; Will be through the discharging of the water after the mud separating treatment, wherein portion water enters water collecting basin (7), starts backwashing pump (9) by magnetic valve (8) activated biofiler (4) is carried out back flushing.
2. according to the described sewage treatment process of claim 1, it is characterized in that: described activated biofiler (5) is a upward flow, described activated sludge tank (4) and the disposable aeration of activated biofiler (5).
3. according to the described sewage treatment process of claim 1, it is characterized in that: adopt some water distributions or 2 water distribution manners, more described water distribution manner is located to be provided with at activated sludge tank (4), and described 2 water distribution manners are to locate to be provided with respectively at activated sludge tank (4) and activated biofiler (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99113073A CN1103324C (en) | 1999-07-02 | 1999-07-02 | Process for treating sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99113073A CN1103324C (en) | 1999-07-02 | 1999-07-02 | Process for treating sewage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1279214A true CN1279214A (en) | 2001-01-10 |
| CN1103324C CN1103324C (en) | 2003-03-19 |
Family
ID=5276308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99113073A Expired - Fee Related CN1103324C (en) | 1999-07-02 | 1999-07-02 | Process for treating sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1103324C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100337947C (en) * | 2003-06-11 | 2007-09-19 | 金贤 | Process for printing and dyeing waste water treating tower |
| CN100364651C (en) * | 2003-11-27 | 2008-01-30 | 同济大学 | Catalytic oxidation reaction apparatus of trickle bed |
| CN101389572B (en) * | 2006-02-23 | 2011-04-13 | 旭化成化学株式会社 | Method of treating wastewater |
| CN101462816B (en) * | 2009-01-12 | 2011-09-14 | 浙江大学 | Apparatus for integrated treatment and comprehensive utilization of wastewater and use thereof |
| CN111011287A (en) * | 2019-12-13 | 2020-04-17 | 蓝淼科技(广州)有限公司 | Penaeus vannamei farming systems |
-
1999
- 1999-07-02 CN CN99113073A patent/CN1103324C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100337947C (en) * | 2003-06-11 | 2007-09-19 | 金贤 | Process for printing and dyeing waste water treating tower |
| CN100364651C (en) * | 2003-11-27 | 2008-01-30 | 同济大学 | Catalytic oxidation reaction apparatus of trickle bed |
| CN101389572B (en) * | 2006-02-23 | 2011-04-13 | 旭化成化学株式会社 | Method of treating wastewater |
| CN101462816B (en) * | 2009-01-12 | 2011-09-14 | 浙江大学 | Apparatus for integrated treatment and comprehensive utilization of wastewater and use thereof |
| CN111011287A (en) * | 2019-12-13 | 2020-04-17 | 蓝淼科技(广州)有限公司 | Penaeus vannamei farming systems |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1103324C (en) | 2003-03-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102372401B (en) | Iron-carbon micro-electrolysis-dynamic membrane wastewater deep treatment process | |
| CN101219842A (en) | Technique and equipment for recycling leachate of garbage | |
| CN101746931B (en) | Denitrification dephosphorization biological treatment and filtration integral sewage treatment system and method thereof | |
| CN106977042A (en) | A kind of modularization integrated approach handled suitable for soy sauce brewing wastewater | |
| CN209619125U (en) | Magnetic-coagulation clarification and denitrification filter pool combined type sewage treatment equipment | |
| CN201598224U (en) | Biological nitrogen and phosphorus removal treatment and filter integrated sewage treatment system | |
| CN101333055B (en) | Complete plant for treating and recovering printing light polluted waste liquid | |
| CN102351366B (en) | Device and method for treating pharmaceutical waste water through synchronous biological denitrification and devulcanization and autotrophic biological denitrification | |
| CN1286741C (en) | Aeration biological filtering tank with synchronizing removing nitrogen and organics function | |
| CN1400174A (en) | Anaerobic aerobic flocculation precipitation sewage treatment process | |
| CN209098459U (en) | A kind of high gravity fermentation class antibiotic waste water processing system | |
| CN201065361Y (en) | Integrated aerobic particles sludge film bioreactor | |
| CN100500593C (en) | Combined type wastewater treatment method and equipment | |
| CN1413916A (en) | Air-floated biological treatment process and equipment | |
| CN1103324C (en) | Process for treating sewage | |
| CN200988816Y (en) | Garbage percolating liquid treating system based on film biological reactor-filter film technology | |
| CN1693229A (en) | Jet-flow aeration biological filtering tank | |
| CN101391833A (en) | Filter tank type membrane bioreactor | |
| CN101786724A (en) | Technology for processing domestic sewage into normal water | |
| CN106186322A (en) | A kind of low energy consumption tubular membrane processes garbage filter liquid device | |
| CN102311206A (en) | SBR (Sequencing Batch Reactor)-ultrafiltration membrane sewage reusing device | |
| CN202139145U (en) | SBR (Sequencing Batch Reactor Activated Sludge Process)-ultrafiltration membrane sludge recycling device | |
| CN201250159Y (en) | Complete equipment used for treating dyeing light pollution waste water for reuse | |
| CN1332897C (en) | Combined alternative flow integrated biological reactor and method for treating waste water therewith | |
| CN2848842Y (en) | Aeration biological filtering chamber |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |