
Activated Sludge Separation Problems
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Content
- Cover
- Copyright
- Contents
- Abbreviations
- List of contributors
- 1. Wastewater characterization
- 1.1 Introduction
- 1.2 Gross parameters
- 1.3 Physical properties
- 1.4 Organic matter
- 1.5 Inorganic matter
- 1.6 Biodegradability
- 1.6.1 COD, Nitrogen fractionation
- 1.6.2 Evaluation methods
- 1.6.2.1 Carbonaceous substrate (COD)
- 1.6.2.2 Nitrogen and phosphorus
- 1.7 References
- 2. The Microbiology of Activated Sludge Process
- 2.1 Introduction
- 2.2 Microorganisms in activated sludge
- 2.3 The identification of bacteria
- 2.4 Filamentous bacteria
- 2.5 Microthrix parvicella
- 2.6 Thiothrix
- 2.7 Nostocoida limicola
- 2.8 Polyphosphate Accumulating Organisms (PAO)
- 2.9 Glycogen Accumulating Organisms (GAO)
- 2.10 Nitrifiers
- 2.11 Denitrifiers
- 2.12 Quantitative estimation of filamentous bacteria in activated sludge
- 2.13 FISH Analysis
- 2.14 References
- 3. AS Separation problems
- 3.1 Introduction
- 3.2 "Well-settling" activated sludge
- 3.2.1 Requirements
- 3.2.2 Microscopic features of well settling activated sludge
- 3.3 Activated sludge separation problems
- 3.3.1 Poor floc microstructure
- 3.3.1.1 Dispersed growth
- 3.3.1.2 Unsettleable microflocs
- 3.3.1.3 Viscous bulking
- 3.3.2 Poor floc macrostructure
- 3.3.2.1 Filamentous bulking
- 3.3.2.2 Foaming caused by filamentous microorganisms
- 3.3.3 Other reasons
- 3.3.3.1 Rising sludge
- 3.4 Summary
- 3.5 References
- 4. Aeration tank and secondary clarifier as one system
- 4.1 Introduction
- 4.2 Aeration tank and secondary clarifier interactions
- 4.2.1 Activated sludge process
- 4.2.2 Secondary clarifier
- 4.2.2.1 General performance, thickening function
- 4.2.3 Separation function
- 4.2.4 BOD5
- 4.2.5 COD
- 4.2.6 Nitrogen and phosphorus
- 4.3 The impact of aeration basin equipment and operation on the performance of secondary clarifiers
- 4.3.1 Mechanical vs. diffused-air aeration
- 4.3.2 Mixed liquor mixing
- 4.3.3 Degasification and reflocculation in aeration tanks
- 4.4 Features of secondary clarifier construction
- 4.4.1 Inlet structure with a flocculation zone
- 4.4.1.1 Principles of a flocculation zone
- 4.4.1.2 Conventional flocculation zones with tangential flow regime
- 4.4.1.3 Novel flocculation zone with deflectors and a vertical flow regime
- 4.4.2 Outlet structure
- 4.4.2.1 Peripheral vs. internal effluent launders
- 4.4.3 Scum baffles
- 4.5 Efficient scum removal from the surface of secondary clarifiers
- 4.5.1 Conventional scum boxes
- 4.5.2 "Travelling" scum boxes
- 4.5.3 Pneumatic systems
- 4.6 Removal of settled and thickened sludge
- 4.6.1 Effect on the final effluent quality
- 4.6.2 Mechanical scrapers
- 4.6.3 Vacuum sludge removal
- 4.7 References
- 5. Bulking and Foaming Control Methods
- 5.1 Introduction
- 5.2 Specific control methods
- 5.2.1 Bulking due to low F/M
- 5.2.1.1 Continuous plug-flow reactors
- 5.2.1.2 Selectors
- 5.2.1.3 Sequencing batch reactors
- 5.2.1.4 Role of storage phenomena in microbial competition in substrate gradient processes
- 5.2.2 Bulking due to low nutrient concentration
- 5.2.3 Bulking due to low dissolved oxygen concentrations
- 5.2.4 Bulking due to fatty acids in the influent stream: control methods for Microthrix parvicella
- 5.2.5 Microbial and enzymatic preparations
- 5.3 Non specific control methods
- 5.3.1 Oxidising agents
- 5.3.2 Weighting or flocculating agents
- 5.3.3 New findings: use of alluminum salts to control Microthrix parvicella
- 5.4 Control of non-filamentous bulking ("viscous bulking")
- 5.5 Avoiding poor settling properties: alternative separations of activated sludge
- 5.6 References
- 6. Experiences in Various Countries
- 6.1 Introduction
- 6.2 Australia
- 6.2.1 General situation
- 6.2.2 Foaming filamentous bacteria in Australian Activated Sludge Plants
- 6.2.3 Foaming and Bulking Filamentous Bacteria in Activated Sludge Plants
- 6.2.4 Do the filamentous populations in activated sludge plants change with time?
- 6.2.5 Which operational factor affect filamentous populations and consequently determine incidents of bulking and foaming
- 6.2.6 Control Measures for Bulking and Foaming
- 6.2.7 An Australian Case Study
- 6.2.7.1 Plant Design Features
- 6.2.7.2 Microscopic Features of the Biomass
- 6.2.7.3 Bulking and Foaming Incidents
- 6.2.8 Conclusions
- 6.3 Czech Republik
- 6.3.1 Separation problems - situation up to 1980s
- 6.3.2 Separation problems - situation up to mid-1990s
- 6.3.3 WWTPs screening - 1995 - 2000
- 6.3.3.1 Methodology
- 6.3.3.2 Microscopic analysis and sedimentation properties evaluation
- 6.3.4 Results of separation problems and filamentous micro-organisms screening
- 6.3.4.1 Filamentous micro-organism abundance
- 6.3.4.2 Dominant filamentous microorganisms in sludge and foam
- 6.3.5 Development of filamentous population in Czech activated sludge plants between 1997 - 1998
- 6.3.5.1 SVI and total abundance of filaments
- 6.3.5.2 Dominant filamentous microorganisms in activated sludge mixed liquor and foams
- 6.3.6 Screening of eight nutrient removal plants in 2000
- 6.3.6.1 Characterization of monitored WWTPs
- 6.3.6.2 Activated sludges and settling properties
- 6.3.6.3 Dominant filamentous microorganisms in activated sludge mixed liquor
- 6.3.6.4 Biological foams
- 6.3.7 Foam control strategies
- 6.3.7.1 Water sprays
- 6.3.7.2 Skimming (mechanical removal) of foam
- 6.3.7.3 Return activated sludge manipulation
- 6.3.7.4 Manipulation of SRT
- 6.3.7.5 Additional installation of baffles
- 6.3.7.6 Initial contact zones ("selectors")
- 6.3.7.7 Chlorination of foam
- 6.4 Denmark, Greece and Netherlands
- 6.4.1 General situation
- 6.4.2 Wastewater composition
- 6.4.3 Process configurations
- 6.4.4 Magnitude of bulking and foaming problems in Denmark, Greece and The Netherlands
- 6.4.5 Settling properties in nutrient removal plants
- 6.4.6 Effect of different process conditions on SVI and the size of the filamentous population
- 6.4.7 Composition of the filamentous population
- 6.4.8 Influence of wastewater composition, process configuration and operating parameters on filamentous microorganisms growth
- 6.4.9 Effects of wastewater composition
- 6.4.10 Effects of process configuration
- 6.4.11 Experience with control measures applied
- 6.4.12 Non specific control measures
- 6.4.13 Specific control measures
- 6.4.14 Conclusions
- 6.5 France
- 6.5.1 General situation
- 6.5.2 Bulking and foaming characterization
- 6.5.3 Bulking and foaming situation
- 6.5.4 Dominant filamentous microorganisms in bulking and foaming sludges
- 6.5.5 Filamentous microorganisms and relationship with plant operation
- 6.5.6 Successful solutions for bulking and foaming control
- 6.5.7 Contact zone as preventive solution
- 6.5.7.1 Key points of contact zone design
- 6.5.8 Control of bulking by Cl2 addition
- 6.6 Germany/Austria
- 6.6.1 General situation
- 6.6.2 Bulking and scum in municipal and industrial wastewater treatment plants
- 6.6.3 Biology and specific troubleshooting measures of filamentous bacteria
- 6.6.4 Sulfur bacteria
- 6.6.5 Gram-negative filamentous bacteria in highly load plants
- 6.6.6 Experience with selectors for industrial wastes in Austria
- 6.6.6.1 Dimensioning and construction of an aerobic selector
- 6.6.6.2 Storage capacity and substrate removal after shock loads, maximum storage capacity
- 6.6.6.3 Influence of SRT and F/M ratio on the substrate elimination in the selector
- 6.6.6.4 Nutrient supply and substrate elimination
- 6.6.6.5 Adaptation of mixed liquor to a selector
- 6.6.6.6 Microbial growth and storage of substrate in the selector
- 6.6.7 Gram-positive filamentous bacteria in low load WWTP
- 6.6.7.1 M. parvicella
- 6.6.7.2 Nocardioform actinomycetes
- 6.6.8 Eikelboom morphotypes Nostocoida limicola, Types 0041/0675, 1851, and 0092
- 6.6.9 Non-specific control measures for sludge bulking and scum
- 6.6.9.1 Addition of aluminum salts for phosphate precipitation
- 6.6.9.2 Addition of layered silicates
- 6.6.9.3 Addition of lime
- 6.6.10 Decreasing the biomass of filamentous bacteria
- 6.7 Italy
- 6.7.1 General situation
- 6.7.2 Filament surveys
- 6.7.2.1 Puglia Region, Southern Italy
- 6.7.2.2 Lazio Region, Central Italy
- 6.7.2.3 Industrial wastes, Northern Italy
- 6.7.2.4 Survey on 167 Domestic plants
- 6.7.3 Control methods
- 6.7.3.1 Non specific methods
- 6.7.3.2 Specific methods
- 6.7.4 Case studies at full-scale plants
- 6.7.4.1 Reduction of Type 021N by chlorination at the Bagnuolo (Reggio Emilia) Municipal Plant
- 6.7.4.2 Controlling growth of Nocardia and M. parvicella by selectors at the Moncasale (Reggio Emilia) Treatment Plant
- 6.7.4.3 Experiences at Varese - Olona Plant (northern Italy) for controlling Nocardia and M. parvicella growth by reducing sludge age
- 6.7.4.4 Type 021N and Thiothrix reduction by an anoxic selector at Area Nolana Treatment Plant
- 6.7.4.5 Selector investigations on four large WWTP in Central Italy
- 6.7.4.6 M. parvicella elimination by poly aluminium chloride at Fusina Treatment Plant
- 6.8 Japan
- 6.8.1 General situation
- 6.8.2 Major Filaments Responsible for problems
- 6.8.3 Research on Fundamental Aspects of Filamentous Bulking in Japan/Thailand
- 6.8.4 Control Measures Applied
- 6.8.5 Case Studies
- 6.9 South Africa
- 6.9.1 General situations
- 6.9.1.1 Extended aeration plants
- 6.9.1.2 Conventional activated sludge
- 6.9.1.3 Plants treating industrial wastes
- 6.9.2 Plants specifically designed for biological nutrient removal (BNR)
- 6.9.2.1 First generation plants
- 6.9.3 Filamentous organisms in South African activated sludge plants
- 6.9.4 Reasons for the growth of filamentous organisms in SA plants
- 6.9.5 Methods used for the control of bulking and foaming in South Africa
- 6.9.5.1 Physical removal
- 6.9.5.2 Use of toxicants
- 6.9.5.3 Reduction of sludge age
- 6.9.5.4 Elimination and prevention of surface trapping
- 6.9.5.5 Increase in clarification capacity
- 6.9.5.6 Adjustments of dissolved oxygen levels
- 6.9.5.7 Improvements of reactor configuration
- 6.9.6 A case study
- 6.10 United Kingdom
- 6.10.1 General situation
- 6.10.2 Current situation
- 6.10.3 Control measures
- 6.10.4 Case history
- 6.10.4.1 Background
- 6.10.4.2 Solution Process
- 6.10.5 Conclusion
- 6.11 USA
- 6.11.1 General situations
- 6.11.2 Control of filaments in activated sludge systems
- 6.11.3 Other solids separation problems
- 6.11.4 Foaming
- 6.11.5 Viscous bulking and dispersed growth
- 6.11.6 Conclusions
- 6.12 References
- 7. Modelling of bulking phenomena
- 7.1 Introduction
- 7.2 Chudoba's theory
- 7.3 Chiesa and Irvine model
- 7.4 AEROFIL model
- 7.4.1 Hypotheses and fundamentals
- 7.4.2 Processes in model
- 7.5 Conclusions
- 7.6 References
- Index
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