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General Purposes of Biological Treatment
Coagulate and remove non-settleable colloidal solids
stabilize organic matter
Objectives of Biological Treatment in Domestic Wastewater
To reduce organic content and inorganic nutrients
To remove toxic organic compounds
Objectives of Biological Treatment in Industrial Wastewater
To remove or reduce concentration of organic and inorganic compounds
Mechanism of biological treatment
Uses microorganisms, especially bacteria
convert organic matter into various gases and cell tissue
O2, NH3, and PO43- are nutrients needed for conversion of organic matter
cell tissues are then removed thru gravity settling
time required for organisms to acclimate to new environment
Lag phase
cells divide at a rate determined by their generation time & ability to process food
Log-growth Phase
no more substrate or nutrients for growth; growth of new cells offset by death of old cells
Stationary Phase
death rate exceeds production of new cells
Log-death Phase
True or False. Most biological treatment processes are comprised of only one biological population
False. They are are comprised of complex, interrelated and mixed biological populations
Factors of growth curve in each biological population
Food and nutrients
Temperature
pH
Aerobic or anaerobic
Types of biological treatment processes
Attached-growth
suspended-growth
combined
lagoon
Type of biological treatment process where microorganisms are attached to some inert medium
Attached-growth processes
examples of Attached-growth processes
trickling filter
rotating
biological contactors
Type of biological process where microorganisms are maintained in liquid suspension by appropriate mixing methods
Suspended-growth processes
Example of Suspended-growth processes
activated sludge
aerobic and anaerobic digestion
Type of biological treatment process that is hybrid of attached and suspended-growth processes
Combined processes
Example of combined process
integrated Fixed Film Activated Sludge (IFAS)
Type of biological treatment process where lagoons and constructed wetlands are classified
Nature-based processes
Type of nature based process of biological treatment where treatment take place in ponds or lagoons
Lagoons
Type of nature based process of biological treatment characterized as manmade engineered wetland for treating wastewater effluent
Constructed wetlands
nonsubmerged fixed-film biological reactor using rock or plastic packing over which wastewater is distributed continuously
treatment occurs as the wastewater flows over attached biofilm
Trickling filter
provides a surface for the biological slime layer or biofilm to attach and grow
Filter media
collects treated wastewater and solids (sloughs)
discharged from the filter media, and transports them to a clarifier
must be designed to support packing, slime growth and wastewater
allows air ventilation through the filter media
Underdrain System
flow of wastewater including recirculation applied on unit area of the filter in a day
Hydraulic Loading Rate
amount of 5-day (20°C) BOD, excluding the BOD of the recirculant, applied per unit volume of filter media in a day
Organic Loading Rate
Biological treatment unit arrangement
Single-stage arrangement
Two-stage arrangement
Basic operation of the trickling filter treatment process
wastewater is distributed over the top area through rotating distributor
Air circulation in the void space, by either natural draft or blowers, provides oxygen for the microorganisms growing as an attached biofilm.
The organic material present in the wastewater is metabolized by the biomass attached to the medium.
the inner microbes lose their ability to cling to the surface of the media.
The wastewater then washes the slime off the media and a new slime layer will start to grow.
The sloughed off film and treated wastewater are collected by an underdrainage which also allows circulation of air through filter.
A portion of (supernatant) settling tank the treated effluent from the secondary is recirculated or returned to the TF.
suspended growth secondary treatment process which involves production of an activated mass of microbes capable of stabilizing a waste aerobically
these microorganisms are cultivated in aeration tanks, where they are provided with dissolved oxygen and food from the wastewater.
Activated Sludge Process
Basic components of Activated Sludge Process
Reactor
Liquid-solids separation
Activated Sludge
Recycle system
phases of bacterial growth curve
lag phase
log-growth phase
stationary phase
log-death phase
where microorganisms responsible for treatment are kept in suspension (agitated/mixed) and aerated
reactor
usually a sedimentation tank/ clarifier
Liquid-solids separation
for maintaining high population of microbes (efficient treatment)
Return activated sludge (RAS)
effect of too much waste activated sludge (WAS)
low number of microbes (less efficient treatment) - Food > Microbes
effect of too little WAS (Waste activated sludge)
large concentration of microbes (effluent overflow); food < microbes; imbalance in microbial population; decrease in the dissolved oxygen levels.
Basic Operation of Activated Sludge Process
As the influent enters the reactor or aeration tank, the activated sludge microbes consume the solids and organic matter present in the wastewater.
MIXED LIQUOR, is agitated and aerated in the aeration tank.
Microorganisms are mixed thoroughly with the organics under conditions
that stimulate their growth
The individual microorganisms will then floc together (due to mixing) to form an active mass of microbes or biological floc called activated sludge.
The mixed liquor (WW + AS) flows from the aeration tank to the secondary clarifier to separate the solids and microorganism from water by gravity.
Most of the activated sludge that settled at the bottom of the clarifier are returned to the aeration tank.
importance of RAS
to maintain high population of microbes in the aeration tank for rapid breakdown of the organic matter.
importance of waste activated sludge
to create a balance between the available food and the mass of microorganism (F/M ratio) allowed to accumulate in the aeration tank
→ for efficient degradation of BOD or organics
concentration of suspended solids present in the mixed liquor of the aeration tank
Mixed Liquor Suspended Solids (MLSS)
the concentration of the organic or volatile suspended solids in the mixed liquor of the aeration tank. It is used as a measure or indication of the microorganisms (biomass) present.
Mixed Liquor Volatile Suspended Solids (MLVSS)
Process of determining MLVSS concentration
A well-mixed sample (w/ volume V) is filtered through a weighed standard glass-fiber filter (Wfilter)
Filter residue is composed of the MLSS + capillary water
The filter residue is oven-dried at 103 to 105°C. The mass of the dried filter residue is the mass of the MLSS; MLSS = (Woven – Wfilter) / V
The oven-dried filter residue is placed in a furnace and ignited at 550°C for 15 to 30 minutes. The mass lost in the ignition is the mass of the MLVSS while the remaining residue is composed of the inert matter or solids. MLVSS = (Woven – Wfurnace) / V
Effect of High rate of wasting, high F/M Ratio
organisms are saturated with food; thus, poor treatment efficiency
Effect of low rate of wasting, low F/M Ratio
organisms are starved; thus, more complete degradation of food or BOD5 → longer sludge age Ɵc required
index of how well a sludge will settle at a given MLSS concentration.
SLUDGE VOLUME INDEX (SVI)
Result of high SVI
poor settleability
Sludge problems
bulking sludge
rising sludge
sludge problem characterized by poor settling and poor compactibility
bulking sludge
types of bulking sludge with respect to cause
Growth of filamentous organisms:
Low conc = provide structure for floc
High conc = bulking problems
Water trapped in the bacterial flow
cause of growth of filamentous organisms
Low dissolved oxygen
Low food to microorganism (F/M) ratio
Low pH
High sulfides
Nutrient deficiency
Excessive grease
A sludge that floats to the surface after apparently good settling (sludge settles to the bottom of the clarifier, is compacted, and then starts to rise to the surface)
Rising sludge
Solution for rising sludge
Increase rate of return sludge flow (Qr)
Decrease mean cell residence time (avoid denitrification)
types of oxidation ponds
Aerobic ponds
Aerated lagoons
Facultative ponds
Anaerobic ponds
Maturation or tertiary ponds
type of oxidation pond characterized as:
• Shallow ponds; < 1 m deep
• DO maintained throughout depth (O2 supplied by algal photosynthesis)
aerobic ponds
type of oxidation pond characterized as:
• Ponds oxygenated by surface or diffused air aeration
Aerated lagoons
type of oxidation pond characterized as:
• 1-2.5 m deep
• Aerobic upper zone (photosynthesis, surface re-aeration), facultative middle zone, anaerobic lower zone
Facultative ponds
type of oxidation pond characterized as:
•Deep ponds that receive high organic loadings (to deplete all O2); anaerobic conditions throughout
Anaerobic ponds
type of oxidation pond characterized as:
• Used for polishing effluents from biological processes (tertiary treatment)
• DO is furnished through photosynthesis & surface re-aeration
Maturation & tertiary ponds (polishing pond)
minimum requirements in the design of oxidation ponds
a berm or embankment
impermeable soil
a fence surrounding the pond
area around pond mowed and tree growth restricted
a windbreak
two to five feet deep
sensitivity to nearby
streams and rivers