CN1911834A - Prewarning and control method of active sludge expansion and biological foam in sewage treatment - Google Patents
Prewarning and control method of active sludge expansion and biological foam in sewage treatment Download PDFInfo
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- CN1911834A CN1911834A CNA2006100252722A CN200610025272A CN1911834A CN 1911834 A CN1911834 A CN 1911834A CN A2006100252722 A CNA2006100252722 A CN A2006100252722A CN 200610025272 A CN200610025272 A CN 200610025272A CN 1911834 A CN1911834 A CN 1911834A
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- 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
Abstract
The present invention belongs to the field of environment controlling technology, and is especially active sludge bulking and foaming controlling method for sewage treating yard. By means of analysis and calculation on the active sludge data in sewage treating yard, the sludge bulking and foaming conditions are divided into three grades, so as to take corresponding measures to control active sludge bulking and foaming effectively and prevent and reduce relevant hazard and loss.
Description
Technical field
The invention belongs to the environmental improvement technical field, be specifically related to a kind of Sewage treatment systems activated sludge bulking and bio foam early warning and control method.
Background technology
Activated sludge sewage processing system is easier to take place sludge bulking and bio foam phenomenon.These phenomenons not only have influence on the water quality of water outlet when taking place, and bring the view problem.But because the complicacy of genesis mechanism, analyzing its occurrence cause needs the long time, brings inconvenience for operation control.Present many sludge bulkings and foamy control method have tangible lag-effect all in sludge bulking with foam is a large amount of takes after taking place, the expense height of Tou Ruing not only, and also effect is undesirable.
Summary of the invention
The objective of the invention is to propose a kind of method that can carry out early warning and in time be controlled the sludge bulking and the bio foam phenomenon of mud and sewage treatment system,, improve treatment effect to reduce running cost.
Because activated sludge bulking and foamy produce a process is arranged, when people observe tangible sludge bulking and a large amount of foam, qualitative change has taken place in Sludge System in fact, control for the quantitative change process that causes qualitative change, can eliminate in bud producing expansion and foamy trend, be major technique thinking of the present invention.
The present invention observes according to long-term experiment, has selected to influence 3 significant parameters that sludge bulking and frothing take place in the activated sludge sewage processing system, tests and assesses, and determines its occurrence degree, judges its corresponding rank, sends different alarms simultaneously.These 3 parameters are to be easy to the representative parameter index measuring and observe in production practice, are respectively sludge volume index SVI, and subjective graded index of filamentous bacterium and aeration tank foam coverage degree are established the grade of early warning system with this.The early warning system rank is divided into three grades, is 150~200ml/gMLSS at SVI, and filamentous bacterium quantity is 4 grades, and aeration tank foam coverage degree (visual inspection) is to be first-degree alert below 30%, and this rank is sludge bulking and foamy early period of origination; When SVI is 200~300mL/gMLSS, filamentous bacterium quantity is 5 grades, aeration tank foam coverage degree be 30~50% o'clock be the secondary warning, this rank is sludge bulking and foamy evolution period, take appropriate measures and control; When SVI is greater than 300mL/gMLSS, filamentous bacterium quantity is more than 5 grades or 5 grades, and the foam coverage degree is 50% to be three grades of warnings or serious warning when above, is sludge bulking and foamy peak period here.
According to the different stage of alarm, take different control reclamation activitiess respectively, specific as follows:
When first-degree alert, need arouse attention this moment, can take 1. suitably to shorten mud age, promptly controls sludge retention time at 6-8 days; 2. reduce the time 10-20% of the oxygen section of holding concurrently, improve aerobic section aeration time 10-20%,, keep dissolved oxygen under the condition of 2~4mg/L to improve dissolved oxygen content; 3. increase the sludge volume (increasing 50-100%) of aeration tank, reduce sludge concentration, control to improve sludge loading more than 0.3kgBOD/kgMLSSd;
When secondary is guarded against, can take 1. to shorten mud age, promptly control sludge retention time 5-7 days; 2. increase aeration time 10-20%; 3. improve load, the 4. braking measure of dosing coagulant (flocculation agent) or sterilant, adds the sterilant clorox at i, and dosage press available chlorine content 8~10mg/L calculating in the mixed solution, is equivalent to 0.3%MLSS; Ii, add coagulant aids polyacrylamide PAM, dosage is 1~2mg/L;
When being three grades of whens warning, can take 1. to shorten mud age, control residence time 6-8 days; 2. add the sterilant clorox of capacity, dosage is pressed available chlorine content 10-12mg/L calculating in the mixed solution; Interception guipure (highly dense nylon wire) 3. is set in the aeration tank, the foam that swims in the surface, aeration tank and scum silica frost is carried out net catch and tackle, regularly gather foreign material and the residual body of foam on labor cleaning's filter.
Initial stage in sludge bulking and foam generation is carried out early warning, take different countermeasures respectively, it is eliminated in original state, can reduce sludge bulking and foam probability that takes place and the loss that causes significantly, be the effective ways of practicable cost-effective active sludge sewage work's sludge bulking and foam control.
The following table of filamentous bacterium quantity rank:
Rank | Richness | Explain |
0 | Do not have | Do not observe mycelia |
1 | Few | There is mycelia to exist, but only in some flco, finds accidentally |
2 | Some | The mycelia ubiquity, but all exist in the not all flco |
3 | Common | All flcos all have mycelia to exist, but density very low (1~5 mycelia/flco) |
4 | More | All flcos all have mycelia to have density medium (5~20 mycelia/flcos) |
5 | Abundant | All there be (a 20-100 mycelia/flco) in a large number in mycelia in all flcos |
6 | A lot | Thread fungus is far away more than flco, (greater than 100 a mycelia/flco) |
Description of drawings
Photo when Fig. 1 reaches 3 grades of warnings for certain activated sludge sewage processing system sludge bulking and foam, visible reaction tank surface have the floating foam of large number of biological to exist.
Fig. 2 is abundant for filamentous bacterium, reaches the photo of a 20-100 mycelia/flco.
Fig. 3 is for reaching 3 grades of whens warning, the photo that the reaction tank surface has oil slick to exist.
Fig. 4 is for being provided with the photo of interception guipure in the aeration tank.
Fig. 5 is through aeration tank face photo after the repair process, and wherein biological floating foam disappears.
Fig. 6 is that certain sludge of sewage treatment plant is between the phase of expansion and adopt SVI change curve after the measure of control.
Embodiment
The present invention is further described below in conjunction with example
Certain sewage work's designing treatment amount is 150,000 m
3/ d sets up three group reaction ponds separately, and 50,000 m are born in every group reaction pond
3The treatment capacity of/d.
Owing to do not set up early warning mechanism, break out sludge bulking in November, 2004, has large number of biological to float the foam (see figure 1) in the activated sludge reaction pond.This time sludge age in service be 11~14 days, MLSS concentration~3000mg/L, SVI surpasses 300mL/g after testing, filamentous bacterium is abundant, reaches 5 grades of (see figure 2)s, on the face of reaction tank pond the oil slick (see figure 3) is arranged.Be in three grades of warnings.
The measure of taking be at first reduce mud age to 6~8 days, the interception guipure is set in the pond foam that swims in the surface, aeration tank and scum silica frost are carried out net catches and tackle (see figure 4), SVI drops to 100~130mL/g, the filamentous bacterium richness is common, reaches 2~3 grades.SVI slowly rises to 175~220mL/g then, and every group reaction pond adds the 150kg clorox, presses available chlorine content 9mg/L calculating in the mixed solution, is equivalent to 0.3%MLSS (weight ratio w/w).SVI drops to below the 120mL/g after the dosing, and the filamentous bacterium richness is few, reach 1 grade and below, the reaction tank pond floating foam disappearance (see figure 5) of thing of looking unfamiliar.Fig. 6 is seen in the SVI variation during this section.
Claims (2)
1, the early warning system of sludge bulking and frothing takes place in a kind of Sewage treatment systems, it is characterized in that the early warning system rank is divided into three grades, at SVI is 150 ~ 200ml/gMLSS, filamentous bacterium quantity is 4 grades, aeration tank foam coverage degree is to be first-degree alert below 30%, and this rank is sludge bulking and foamy early period of origination; When SVI is 200 ~ 300mL/gMLSS, filamentous bacterium quantity is 5 grades, aeration tank foam coverage degree be 30 ~ 50% o'clock be the secondary warning, this rank is sludge bulking and foamy evolution period, take appropriate measures and control; When SVI is greater than 300mL/gMLSS, filamentous bacterium quantity is more than 5 grades or 5 grades, and the foam coverage degree is 50% to be three grades of warnings or serious warning when above, is sludge bulking and foamy peak period here;
Here, SV1 is a sludge volume index, and the rank of filamentous bacterium amount is: 4 grades of 5-20 mycelia/flcos, 5 grades: a 20-100 mycelia/flco, 6 grades: greater than 100 a mycelia/flco.
2, the control method of sludge bulking and frothing taking place in a kind of Sewage treatment systems, it is characterized in that when first-degree alert, take 1. to shorten mud age, promptly controls sludge retention time at 6-8 days; 2. reduce the time 10-20% of the oxygen section of holding concurrently, improve aerobic section aeration time 10-20%,, keep dissolved oxygen under the condition of 2~4mg/L to improve dissolved oxygen content; 3. increase the sludge volume of aeration tank, reduce sludge concentration with the load that improves mud more than 0.3kgBOD/kgMLSSd, control;
When secondary is guarded against, take 1. to shorten mud age, promptly control sludge retention time 5-7 days; 2. increase aeration time 10-20%; 3. improve load, the 4. braking measure of dosing coagulant or sterilant, adds the sterilant clorox at i, and dosage press available chlorine content 8~10mg/L calculating in the mixed solution, is equivalent to 0.3%MLSS; Ii, add coagulant aids polyacrylamide PAM, dosage is 1~2mg/L;
When being three grades of whens warning, take 1. to shorten mud age, control residence time 6-8 days; 2. add the sterilant clorox of capacity, dosage is pressed available chlorine content 10-12mg/L calculating in the mixed solution; 3. the interception guipure is set in the aeration tank, the foam that swims in the surface, aeration tank and scum silica frost is carried out net catch and tackle, regularly gather foreign material and the residual body of foam on labor cleaning's filter.
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102616933A (en) * | 2012-04-11 | 2012-08-01 | 北京工业大学 | Filamentous sludge bulking recovery method based on non-nitrification A/O (anaerobic/aerobic) biological phosphorus removal process |
CN103011419A (en) * | 2012-12-03 | 2013-04-03 | 北京工业大学 | Method for rapidly solving problem of filamentous bacteria sludge bulking through hunger treatment |
CN104710004A (en) * | 2015-03-27 | 2015-06-17 | 中蓝连海设计研究院 | Secondary sedimentation tank sludge floatation alarming and controlling method for sewage treatment system |
CN104914213A (en) * | 2015-05-13 | 2015-09-16 | 西安建筑科技大学 | Method for early warning of activated sludge filamentous bacterium expansion |
CN106709603A (en) * | 2016-12-21 | 2017-05-24 | 中国科学院海洋研究所 | Implementation method of optimizing method of using improved clay method to eliminate red tide |
CN111144221A (en) * | 2019-11-29 | 2020-05-12 | 光大环境科技(中国)有限公司 | Method and device for evaluating operation condition of aeration tank through image recognition technology |
CN114314818A (en) * | 2022-03-15 | 2022-04-12 | 兰州建投环保节能产业有限公司 | Sludge bulking treatment device based on intermediary principle |
CN114573096A (en) * | 2022-03-25 | 2022-06-03 | 南京大学 | Sewage treatment aeration system control method based on microbial community |
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2006
- 2006-03-30 CN CNB2006100252722A patent/CN100528769C/en active Active
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102616933A (en) * | 2012-04-11 | 2012-08-01 | 北京工业大学 | Filamentous sludge bulking recovery method based on non-nitrification A/O (anaerobic/aerobic) biological phosphorus removal process |
CN103011419A (en) * | 2012-12-03 | 2013-04-03 | 北京工业大学 | Method for rapidly solving problem of filamentous bacteria sludge bulking through hunger treatment |
CN104710004A (en) * | 2015-03-27 | 2015-06-17 | 中蓝连海设计研究院 | Secondary sedimentation tank sludge floatation alarming and controlling method for sewage treatment system |
CN104914213A (en) * | 2015-05-13 | 2015-09-16 | 西安建筑科技大学 | Method for early warning of activated sludge filamentous bacterium expansion |
CN106709603A (en) * | 2016-12-21 | 2017-05-24 | 中国科学院海洋研究所 | Implementation method of optimizing method of using improved clay method to eliminate red tide |
CN106709603B (en) * | 2016-12-21 | 2020-10-16 | 中国科学院海洋研究所 | Implementation method for eliminating red tide by optimizing and utilizing modified clay method |
CN111144221A (en) * | 2019-11-29 | 2020-05-12 | 光大环境科技(中国)有限公司 | Method and device for evaluating operation condition of aeration tank through image recognition technology |
CN114314818A (en) * | 2022-03-15 | 2022-04-12 | 兰州建投环保节能产业有限公司 | Sludge bulking treatment device based on intermediary principle |
CN114573096A (en) * | 2022-03-25 | 2022-06-03 | 南京大学 | Sewage treatment aeration system control method based on microbial community |
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