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CLARIFICATION
Removal of
Settleable and Floatable Solids
•Increase Removal Amount
(More Solids Out)
•Increase Removal Rates
(Solids Settle Faster)
CHEMICAL
CLARIFICATION
•Less Solids
•More Sludge
CHEMICAL
CLARIFICATION
(in effluent)
(for disposal)
Stoke’s Law
2(p - po)g
9n
(d/2)2
VF =
VF = Fall Velocity
(p - po) = Density difference between
particle and water
n = viscosity of water
g = gravitational acceleration constant
d = diameter of the particle
2(p - po)g
9n
(d/2)2
VF =
VF = Fall Velocity
(p - po) = Density difference between
particle and water
n = viscosity of water
g = gravitational acceleration constant
d = diameter of the particle
Stoke’s Law
2(p - po)g
9n
(d/2)2
VF =
VF = Fall Velocity
(p - po) = Density difference between
particle and water
n = viscosity of water
g = gravitational acceleration constant
d = diameter of the particle
Stoke’s Law
2(p - po)g
9n
(d/2)2
VF =
VF = Fall Velocity
(p - po) = Density difference between
particle and water
n = viscosity of water
g = gravitational acceleration constant
d = diameter of the particle
Stoke’s Law
•Increase Particle Size
(Average Diameter)
CHEMICAL
CLARIFICATION
Particle Size versus Settling Time
Particle Size
mm
Order of Size Time to Settle
1.0 Coarse Sand 3 Seconds
0.1 Fine Sand 38 Seconds
0.01 Silt 33 Minutes
0.001 Bacteria 55 Hours
0.0001 Colloidal 230 Days
0.00001 Colloidal 6.3 Years
•Increase Particle Size
•Encourage Contact
CHEMICAL
CLARIFICATION
CHEMICAL
CLARIFICATION
1. Coagulation
2. Flocculation
3. Separation
Coagulation
•Rapid Mixing
•“Pin-point” Floc
Formation
•Chemical Addition
Flocculation
• Slow Mixing
• Floc Growth
• Increased
Diameter
* Fine Suspended Particles Have
an Electrostatic Charge (Usually +)
* Encourage Contact
* Destabilize Charges
Natural Stabilizing Force
Keeps Solids Apart
Like Charges Repel
Purpose of
Chemical Clarification
Mechanisms
•Electrostatic Charge Reduction
•Interparticle Bridging
•Physical Enmeshment
Electrostatic Charge
Reduction
• Solid Particles have an Electrostatic Charge
usually negative
solids repel one another
• Add Chemical to Neutralize Charge
positive charge (cationic)
• Must Not Overdose
excess positive charge
Negative
Colloidal
Particles
Cationic Polymer Unit
Interparticle Bridging
Interparticle Bridging
• Polyelectrolytes (polymers)
long chains
electrostatic charges
• Adsorb on the Charged Particles
bridges particles together
•Must Not Overdose
Physical Enmeshment
• Ions Combine with Hydroxyl Ions
OH -
• Gelatinous Precipitate Forms
flakes
void spaces
• Collects Particles as it Forms
co-precipitate
enlarges the floc
COAGULATION
FLOCCULATION
Rapid Mix
Adequate Contact
Slow Mixing
Increase Floc Size
PROCESS CONTROL
1. Provide complete mixing.
2. Control mixing for floc.
3. Control chemical dose.
Chemical Treatment
Addition of
Positive Ions
(Cations)
or
Polymers
CHEMICAL TREATMENT
Aluminum Sulfate (Al+3)
Calcium Hydroxide (Ca+2)
Ferric (Iron) Chloride (Fe+3)
Positive Ions Added by Adding
Metal Salts
Such As
Metal Salts Used
Most Common
Alum (Aluminum Sulfate)
Ferric Chloride
Lime ( Calcium Hydroxide)
Others
Sodium Aluminate
Ferric Sulfate
Ferrous Sulfate
Ferrous Chloride
Aluminum Sulfate (Dry)
Al2(SO4)3
. 14 H2O
“Alum” or “Filter Alum”
Available in Various Grades
Lump (rarely used)
Ground (granulated)
Rice
Powdered
Feeds Easily
doesn’t “bulk”
Aluminum Sulfate (Dry)
Al2(SO4)3
. 14 H2O
Irritant
skin
mucus membranes
eyes
Must be kept dry
cake to solid lump
corrosive
equipment must be cleaned
Dosage Approximately 75 - 250 mg/L
Aluminum Sulfate (Liquid)
Al2(SO4)3
Approximately 11 pounds / gallon
Approximately 5.4 pounds of “dry”/gal
Ease of Handling vs. Transportation Costs
Corrosive
equipment must be protected
Supports Bacterial Growth / Deposits
Reduces Alkalinity
Ferric Chloride (FeCl3)
Anhydrous
Absorbs Moisture from the Air
Corrosive with Water
Releases Heat as it is Dissolved
Crystal
Absorbs Moisture
Releases Less Heat
Liquid
Lined Containers
Shipped at 30 - 40 %
Approximately 12 pounds per gallon
Ferric Chloride (FeCl3)
Corrosive
equipment must be protected
Stains
Safety Concerns
Dosage Approximately 45 - 90 mg/L
LIME
Hydrated Lime
Ca(OH)2
Coagulant
pH Adjustment
Absorbs Moisture
Quicklime (anhydrous)
CaO
Absorbs Moisture
Must be “Slaked”
Heat Generated
Costs vs. Handling
LIME
Erode or Wear Equipment
Scale Build-up
LIME
Erode or Wear Equipment
Scale Build-up
Dosage Approximately 200 - 400 mg/L
Irritant
skin
eyes
mucus membranes
lungs
Equipment
CHEMICAL
CLARIFICATION
Dry Chemical Feeders
VOLUMETRIC
Measures chemical
amount by VOLUME
GRAVIMETRIC
Measures chemical
amount by WEIGHT
VOLUMETRIC FEEDERS
Less Expensive
Low Delivery Rate
Less Accurate
Screw Feed Mechanism
Volumetric Screw Feeder
Chemical
Hopper
Drive
Mechanism
Rotating
Feed Screw
Mixing
Tank
Gravimetric Feeders
Loss-in-Weight Gravimetric Feeders
Belt Gravimetric Feeders
Highly Accurate
Close Dosage Control
Chemical Cost Savings
Intermediate Cost
Accurate & Reliable
Gravimetric Feeder
HopperScale Beam
Control Wedge
Endless Belt
Slide Gate
GRAVIMETRIC BELT FEEDER
WEIGH BELT
CHEMICAL
HOPPER
WEIGH
DECK
VERTICAL
GATE
WEIGH
BEAM
CHEMICAL
HOPPER
MIXER
WATER
SUPPLY
TO
APPLICATION
FEEDER
Liquid Feeders
Rotary Dippers
Rotometers
Metering Pumps
METERING PUMPS
POSITIVE DISPLACEMENT
Gear
Diaphragm
Plunger
GEAR PUMP
Gear
Gear
Suction Discharge
GEAR PUMP
Suction Discharge
PLUNGER PUMP
PLUNGER
SUCTION
VALVE
DISCHARGE
VALVE
DIAPHRAGM METERING PUMP
SUCTION STROKE
INTAKE
OPEN
CLOSED
ECCENTRIC DRIVE
DIAPHRAGM
PLUNGER
PUMPING
CHAMBER
CHECK VALVE
ASSEMBLY
DIAPHRAGM METERING PUMP
DISCHARGE STROKE
OPEN
CLOSED
ECCENTRIC DRIVE
DIAPHRAGM
PLUNGER
PUMPING
CHAMBER
CHECK VALVE
ASSEMBLY
HYDRAULIC
FLUID
OUTLET
DIAPHRAGM PUMP
Treatment Process
Coagulation
Flocculation
Separation
MIXING
Initial Rapid Mixing
Uniform Dispersion
Efficient Application
Feed
Impeller
Overflow
FLASH MIX TANK
FLASH MIX TANK
FLOCCULATION
Gentle Mixing
Particle Contact
In Biological Process
Feed
Impeller
Overflow
FLOCCULATION TANK
Typical Mechanically Mixed Flocculating Clarifier
Influent
Effluent
Slow
Mixers
Circular
Baffle
Chemical clarification-coagulation

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