Title: 2004 Biological Wastewater Treatment Operators School
12004 Biological Wastewater Treatment Operators
School
- Advanced Treatment Systems
- May 13, 2004
- Dean Pond, Black Veatch
2Advanced Treatment Systems
- What are the forms of nitrogen found in
wastewater?
3What are the forms of nitrogen found in
wastewater?
- TKN 40 Organic 60 Free Ammonia
- Typical concentrations
- Ammonia-N 10-50 mg/L
- Organic N 10 35 mg/L
- No nitrites or nitrates
- Forms of nitrogen
- Organic N
- Ammonia
- Nitrite
- Nitrate
TKN
Total N
4Advanced Treatment Systems
- Why is it necessary to treat the forms of
nitrogen?
5Why is it necessary to treat
the forms of nitrogen?
- Improve receiving stream quality
- Increase chlorination efficiency
- Minimize pH changes in plant
- Increase suitability for reuse
- Prevent NH4 toxicity
- Protect groundwater from nitrate contamination
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6Advanced Treatment Systems
- What are the effects of N and P in receiving
waters?
7What are the effects of N and P in
receiving waters?
- Increases aquatic growth (algae)
- Increases DO depletion
- Causes NH4 toxicity
- Causes pH changes
8Advanced Treatment Systems
- Why is it sometimes necessary to remove P from
municipal wastewater treatment plants?
9Why is it sometimes necessary to remove P from
municipal WWTPs?
- Reduce phosphorus, which is a key limiting
nutrient in the environment - Improve receiving water quality by
- Reducing aquatic plant growth and DO
depletion - Preventing aquatic organism kill
- Reduce taste and odor problems in downstream
drinking water supplies
10Advanced Treatment Systems
- How is P removed by conventional secondary
(biological) wastewater treatment plants?
11How is P removed by conventional secondary
(biological) WWTPs?
- Biological assimilation
- BUG C60H86O23N12P
- 0.03 lb P/lb of bug mass
- GROW BUGS, WASTE BUGS REMOVE P
12Advanced Treatment Systems
- Where in the treatment plant process flow could
chemical precipitants be added?
13Where in the treatment plant flow could chemical
precipitants be added?
- At pretreatment
- Before primary clarifiers
- After aeration basins
- At final clarifiers
- Ahead of effluent filters
- Considerations
- Effective mixing
- Flexibility
- Sludge production
14Advanced Treatment Systems
- How is N removed or altered by conventional
secondary (biological) treatment?
15How is N removed or altered by secondary
(biological) treatment?
- Biological assimilation
- BUG C60H86O23N12P
- 0.13 lb N/lb of bug mass
- Biological conversion by nitrification and
denitrification
16Nitrification
- NH4 ? Nitrosomonas ? NO2-
- NO2- ? Nitrobacter ? NO3-
- Notes
- Aerobic process
- Control by SRT (4 days)
- Uses oxygen ? 1 mg of NH4 uses 4.6 mg O2
- Depletes alkalinity ?
1 mg NH4 consumes 7.14 mg
alkalinity - Low oxygen and temperature
difficult to operate
17Denitrification
- NO3- ? denitrifiers (facultative bacteria) ?
N2 gas CO2 gas - Notes
- Anoxic process
- Control by volume and oxic MLSS recycle to anoxic
zone - N used as O2 source 1 mg NO3- yields 2.85 mg O2
equivalent - Adds alkalinity ? 1 mg NO3- restores 3.57 mg
alkalinity - High BOD and NO3- load and low temperature
difficult to operate
18Advanced Treatment Systems
- What are typical flow application rates in
tertiary filters?
19What are typical flow application rates in
tertiary filters?
- Automatic backwash filters
(1-2 ft media depth) 2 to 4 gpm/sf - Deep bed filters
(4-6 ft media depth) 4 to 8 gpm/sf
20Advanced Treatment Systems
- What are typical backwash rates for a tertiary
filter (in gpm/sf)?
21What are typical backwash rates for a tertiary
filter (in gpm/sf)?
- Automatic backwash filters
- 20 to 25 gpm/sf
- 5 to 10 of throughput
- Deep bed filters
- 15 to 20 gpm/sf
- 3 to 5 of throughput
22Advanced Treatment Systems
- Define advanced treatment
23Define advanced treatment
- Treatment that improves or enhances secondary
treatment processes - Further removal of organics, nutrients and
dissolved solids
24Advanced Treatment Systems
- Explain circumstances under which advanced
treatment may be necessary
25Explain circumstances under which advanced
treatment may be necessary
- Limited assimilative capacity of stream
- Toxicity reduction / elimination
- Nutrient control
- Closed systems
- Water reuse
26Advanced Treatment Systems
- Identify and explain the objectives of the
following advanced treatment systems - Further removal of organics
- Further removal of suspended solids
- Nutrient removal (N and P)
- Removal of dissolved solids
-
27Identify and explain the objectives of the
following advanced treatment systems
- Further removal of organics
- Reduce effluent BOD to reduce receiving stream DO
depletion - Improve disinfection
- Reduce effluent N to improve water quality
- Further removal of suspended solids
- Removing TSS removes BOD
- Removing TSS removes N and P
(BUG C60H86O23N12P) - Protects stream ? sediment oxygen demand
- Improves efficiency of disinfection
28Identify and explain the objectives of the
following advanced treatment systems
- Removal of nutrients (N and P)
- Reduce oxygen demand of receiving stream
- Control nutrients and algae
- Control taste and odor in downstream drinking
water - Suitability for reuse (examples boiler water
recycle, irrigation NP control of runoff,
groundwater recharge)
29Identify and explain the objectives of the
following advanced treatment systems
- Removal of dissolved solids
- Removal of specific pollutant
zinc, chromium, lead - Pretreatment of industrial waste
- Control effluent toxicity
- Make suitable for reuse
30Advanced wastewater treatmentDescribe the
purpose or procedure and mechanism by which it is
done for each of the following
- Activated carbon adsorption
- Chemical coagulation
- Flocculation
- Phosphorus removal
- Nitrogen removal
- Effluent Filtration
- Polishing lagoons
- Nitrification
- Denitrification
- Ammonia striping
- Alum or ion precipitation
- Lime precipitation
- Reverse osmosis (RO)
- Electrodialysis
31Activated Carbon Adsorption
- Purpose
- Tertiary treatment
- Removal of low concentration organic compounds
- Application
- Influent ?Primary Trt ?Biological Trt ?
Filtration ?Carbon ?Disinfection - Many variations
32Activated Carbon Adsorption
Continued
- Carbon Regeneration
- 5 to 10 loss
- Less capacity than new carbon
- Hot air _at_ 350oF
- Chemicals (sodium hydroxide)
- Fire / Explosion
- Carbon usually replaced after 5 regenerations
- Mechanism
- Active sites Activated Carbon
- Molecular bonding
- Particles adhere to surface
33Chemical Coagulation
- Purpose
- Enhanced removal of organics and fine particles
- Addition of lime, alum, iron, polymer to change
ionic charge - Application
- Chemical feed with rapid mix
- Ahead of final clarifiers
- Ahead of filtration
34Chemical Coagulation
Continued
- Lime Heavy metals Alum SS removal
- SS removal P removal
- P removal
- Polymer - SS control Iron SS removal
- P removal
- Mechanism
- Destabilization by ionic charge neutralization
- Reduce charge that keeps small particles apart
Aluminum sulfate
Ferric chloride Ferric sulfate Ferrous sulfate
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35Flocculation
- Purpose
- Produce larger, more dense floc particles that
will settle or filter easily - Application
- Gentle mixing after rapid mix (coagulation)
- Mixing Mechanical or Aeration
Q
Infl Q
Gentle Mix / Flocculation
Rapid Mix / Coagulation
Sludge
36Flocculation
Continued
- Mechanism
- Coagulated particles strung together into larger
floc particles (snow flake floc)
37Phosphorus Removal
- Purpose
- Reduce effluent P
- Biological or chemical method
- Reduce nutrient load on stream
- Reduce algae growth
- Reduce oxygen depletion
- Application / Mechanism
- Biological
- Chemical
38Phosphorus Removal
Continued
39Phosphorus Removal
Continued
Effl
Aerobic Zone
Primary Clarifier
Final Clarifier
Q
Chemical Coagulant
Chemical Coagulant
RAS
WAS
P Removal
40Nitrogen Removal
- Purpose
- Reduce effluent N (ammonia and nitrates)
- Biological or chemical
- Reduce nutrient load on stream
- Reduce algae growth
- Reduce oxygen depletion
- Application / Mechanism
- Advanced Activated Sludge Processes
- Nitrification (remove ammonia)
- NH4 ? NO2 ? NO3
41Nitrogen Removal
Continued
- Denitrification (remove nitrate)
- NO3 ? NO2 ? NO, N2O or N2 gas
- Deep Bed Filtration
- Anaerobic fixed film bacteria (denitrify)
- Air Stripping
- Removes ammonia
- Elevated pH 10.8 to 11.5 NH4 as gas
Q
Media
6-8
Methanol (carbon)
Q
42Effluent Filtration
- Purpose
- Remove SS (usually after FC)
- Reduce BOD and insoluble P
- Application
- Deep Bed
- 4-6 sand and gravel
- Large cells 10 x 30
- Similar to WTP
- (batch backwash)
- hL 4 - 6 ft
- 2. Traveling Bridge
- 1-2 sand and anthracite
- Small cells 1 x 14
- Contiuous backwash
- hL 2 - 3 ft
43Effluent Filtration
Continued
- Loading Rate
- Backwash
- 2 4 gpm/sf
- Frequency depends on loading
- 20 25 gpm/sf
- 5 15 of throughput
- Must clean beds
- Air scour
- Mechanism
- Filtration by granular media
44Polishing Lagoons
- Purpose
- To further treat or polish the effluent
- After final clarifier
- Facultative pond (aerobic and anaerobic)
- Application
- Typical volume 1 day average flow
- i.e., 1 mgd plant 1 mgd lagoon
- 24 hour detention time
- Surface aerators
45Polishing Lagoons
Continued
Sunlight
Surface Aerator
Algae
M
Settling
Aerobic
Anaerobic
- Sunlight ? Photosynthesis ? Algae Organics
Nutrients - Organic Matter ? Anaerobic Decomposition
- Mechanism
- Algae and bacteria grow in pond consuming
organics and nutrients in FC effluent. Algae
settles and degrades by anaerobic process.
methane gas
46Nitrification
- Purpose
- Reduce ammonia on plant effluent
- High ammonia concentrations are toxic to streams
- Quickest impact on DO versus nitrates
- Application
- SRT gt 3 days in activated sludge process
- Grow Nitrosomonas and Nitrobacter
- NH4 ? NO2 ?NO3
- Mechanism
- Biological conversion of ammonia to nitrate
47Denitrification
- Purpose
- Reduce nitrate on plant effluent
- Usually in combination with nitrification to
reduce Total N to the stream - Application
- Activated Sludge Process
- Deep Bed
- Filters
- Mechanism
- Biological conversion of nitrate to N2 gas
Q
Anx
Oxic
FC
Oxic Recycle
RAS
WAS
48Ammonia Stripping
- Purpose
- Reduce ammonia either before or after biological
treatment - Not commonly used in the US
- Application / Mechanism
- Raise pH ? 10.8 to 11.5, usually by adding lime
- Move equilibrium point to ammonia gas _at_ 250C and
pH 11 - NH4 gas 98
49Ammonia Stripping
Continued
- Break wastewater into droplets and strip off
ammonia gas with air - Freefall through tower that circulates a lot of
air to remove ammonia to atmosphere
NH4 Air
Lime
Q
NH4 Stripper
Floc
Precip.
Lime Sludge
Air
Q
50Alum or Iron Precipitation
- Purpose
- To remove orthophosphate
- Application
- As a backup to Bio-P process
- As chemical P removal
- As chemical process
- Mechanism
- Al or Fe PO4 ? Aluminum or Iron Phosphate
Al or Fe
Filtration Optional
Q
Q
Precipitate
Rapid Mix
RAS
WAS Precipitate
51Lime Precipitation
- Purpose
- P removal before primary clarifier or following
biological treatment - Application
- As a backup to Bio-P process
- As chemical P removal
- As chemical process
- High pH can be a problem in effluent or in
biological treatment - Mechanism
- Chemical conversion of phosphorus to calcium
phosphate is in pH range of 9.5 to 11.0
52Reverse Osmosis (RO)
- Purpose
- High quality removal of various salts calcium,
sodium, magnesium - Application
- Water reuse
- AWT
- Mechanism
- Chemical separation / filtration across a
semi-permeable membrane - High pressure
- Tertiary process
- Used in Gulf War to treat sea water sodium removal
53Electrodialysis
- Purpose
- Removal of ionic inorganic compounds
- Application
- AWT
- Medical
- WTP
- Clinical
- Mechanism
- Apply electrical current between two electrodes
- Water passes through semi-permeable membranes
(ion-selective) - Alternate spacing of cation and anion permeable
membranes - Cells of concentrated and diluted salts are formed
54Electrodialysis
- Purpose
- Removal of ionic inorganic compounds
- Application
- AWT
- Medical
- WTP
- Clinical
- Mechanism
- Apply electrical current between two electrodes
- Water passes through semi-permeable membranes
(ion-selective) - Alternate spacing of cation and anion permeable
membranes - Cells of concentrated and diluted salts are
formed - Sludge concentrated salt waste stream as
process reject water - Problems plugging, fowling of membranes, MUST
pretreat activated carbon, multi-media filtration
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H20
Cl-
H
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OH-
Na
Bipolar Membranes
55Advanced wastewater treatmentWhat would be the
effect on sludge production for each of the
following advanced treatment processes?
- Activated carbon adsorption
- Chemical coagulation
- Flocculation
- Phosphorus removal
- Nitrogen removal
- Effluent Filtration
- Polishing lagoons
- Nitrification
- Denitrification
- Ammonia striping
- Alum or ion precipitation
- Lime precipitation
- Reverse osmosis (RO)
- Electrodialysis
56What would be the effect on sludge production for
each of the advanced treatment processes?
- TANSTAAFL (tanstaffull)
- There aint no such thing as a free lunch.
- REMOVE MORE STUFF GET MORE SLUDGE
- More BOD TSS Removal ? MORE SLUDGE
- Add chemicals ? MORE SLUDGE
- N P Removal ? MORE SLUDGE
- Some processes produce more sludge than others
- Electro/mechanical some sludge
- Biological more sludge
- Chemical MOST sludge