Wastewater Treatment
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Transcript Wastewater Treatment
Wastewater
Treatment
Municipal WW Management Systems
Sources of
Wastewater
Transmission
and Pumping
Processing at
the Source
Treatment
Wastewater
Collection
Reuse/Disposal
Sources & Types of WW
Domestic Wastewater
– from residences, commercial & institutional
– flows ~70-90% of water supplied
Industrial Wastewater
– highly dependent on industry
Infliltration/Inflow
– enters through leaks, foundation drains, etc.
Stormwater
– for combined sewers - largely in older cities
Typical WW Characteristics
Parameter
Conc.
BOD
TSS
COD
Ammonia
TOC
Chloride
250 mg/L
250 mg/L
500 mg/L
30 mg/L
100 mg/L
+ 50 mg/L
1972: Federal Water Pollution Control Act
PL 92-500
subsequently amended and now
called the Clean Water Act
– established water quality goals “fishable &
swimmable” and timetable
– established National Pollution Discharge
Elimination System (NPDES)
– construction grants for WW treatment
required
secondary treatment (30/30)
– 30 mg/L BOD5
– 30 mg/L TSS
Conventional WW Treatment
Preliminary
Treatment
Secondary
Sedimentation
Primary
Sedimentation
Biological Process
Sludge
Disinfection
Sludge
Preliminary Treatment
To
remove materials that will interfere with
subsequent treatment
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Coarse Screening (bar racks)
Medium Screening
Comminution
Flow measuring
Pumping
Grit removal
Pre-aeration
Bar Racks
Metal
bars spaced a few cm apart across
water flow
mechanical or manually cleaned
size of unit set by approach velocity
– 0.6-1.0 m/s for mechanically cleaned
– 0.3-0.7 m/s for manually cleaned
see
Fig 10.4 and example 10.2 on pg. 311
Grit Removal
Grit
chambers intended to remove sand,
cinders, gravel that may enter system by
cracks in pipes, inflow etc.
Grit can cause excess wear in pipes and
pumps
small sedimentation tanks; designed with
the help of Stoke’s Law
no organics removal
Grit Chamber
Primary Sedimentation
Purpose:
to remove suspended solids
(smaller than grit, and less harmful)
Typical efficiency
– 67% TSS removal
– 33% BOD removal
Design
parameters
– overflow rate
– weir loading rate
– detention time
Primary effluent is
largely composed of
soluble and colloidal
organics which can be
converted to settleable
microbial solids and
CO2 by biological
treatment
Primary Sedimentation
– Primary Treatment
– Removes ~50% of suspended solids
Parameter Design Range
Typical
Value
Overflow
Rate
35-45 m/d
800-1200 gal/ft2/d
40 m/d
1000 gal/ft2/d
Detention
Time
1.5-2.5 h
2h
2
275 m2/d
Weir loading 125-500 m /d
10,000-40,000 gal/ft/d 20,000 gal/ft/d
rate
Primary Sed. Tank
Primary Clarifier: Center Feed
Secondary Treatment
Generally
includes some biological process
plus secondary clarification
Required under PL92-500
Converts soluble and colloidal organic
materials to biomass and CO2
Biological Treatment
Suspended
Growth
– Activated Sludge
» Conventional, Extended Aeration, Contact
Stabilization
– Aerated lagoons
– Aerobic digestion
Attached
Growth
– Trickling Filters
– Rotating Biological Contactors
Suspended Growth Systems
Air
Aeration Tank
Return Activated Sludge
Secondary
Sedimentation
Sludge
Waste
Activated Sludge
Attached Growth: Trickling Filters
Rotary Distributor
Rocks or
Plastic
Media
Air
Underdrain
With rocks, depth is limited to 2-3 m because of oxygen needs
Rotating Biological Contactors
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Drum diameters are typically 10-12 ft.
Rotation speed: ~1.5 rpm
May be in several stages
No flow recycle
Requires piloting
Secondary Clarifier
Sludge Disposal
Thickening
– gravity, flotation
Digestion
– aerobic, anaerobic
Mechanical
Dewatering
– Vacuum filtration, centrifugation, pressure filtr.
Disposal
– land application, burial, incineration
Anaerobic Digestion
• Sludge held without aeration for 10-90 days
• Process can be accelerated by heating to 35-40oC
• These are called High Rate Digestors (10-20 days)
• Advantages
•low solids production
•useable methane gas produced
• Disadvantages
•high capital costs
•susceptibility to shocks and overloads
Sludge Dewatering
Sludge
drying beds
– historically the most common
– sand bed, 15-30 days, evaporation & seepage
Vacuum
Filtration
– cylindrical rotating drum covered with fabric
– submerged with applied vacuum
Continuous
belt filter presses (follows)
Plate pressure filters
– vertical plates mounted on a frame
Belt Filter Press (Komline-Sanderson)