This document discusses two types of sedimentation processes: plain sedimentation and sedimentation with coagulation. Plain sedimentation involves separating impurities from water through natural gravitational forces alone, without chemical additives. This process lightens the load on subsequent treatment steps and reduces costs. Sedimentation occurs as particles heavier than water settle out due to gravity. Sedimentation tanks come in various shapes and sizes, and different zones exist within the tanks. Aeration is discussed as well, including its purposes and different aerator types like cascade, spray, and air diffusers. Design criteria and an example calculation for sedimentation tank sizing is also provided.
Intro to sedimentation; Plain sedimentation separates impurities by natural forces with advantages like reduced chemical use.
Sedimentation theory; heavier particles settle by gravity. Discrete particles have a constant settling velocity.
Design types include fill and draw & continuous flow tanks. Key metrics: detention times of 4-8 hrs, S.O.R estimates.Aeration increases oxygen, decreases CO2 and odors, and oxidizes metals. Various aerators serve different treatment needs.
Examples of aerators: Cascade, Inclined apron, and Spray aerators enhance gas exchange and reduce CO2.
Air diffusion techniques with details on perf pipe networks in aeration basins and closure of presentation.
• Two typesof sedimentation :
1. Plain sedimentation
2. Sedimentation with coagulation
Plain sedimentation :
When impurities are seperated from suspending fluid
by action of natural force alone, without aid of any coagulant,
is called plain sedimentation.
4.
Advantage of plainsedimentation
• It lightens load on subsequent processes.
• The operation of subsequent process can be controlled in a
better way.
• The cost of cleaning the chemical coagulation basin is reduced.
• Less quantity of chemicals are required.
12.
Theory of sedimentation
•The particle heavier than water are naturally likely to settle
down due to force of gravity.
1. Inorganic suspended solids sp. Gravity 2.65
2. Organic suspended solids sp. Gravity 1.04
• The phenomena of settling of particles at bottom of
sedimentation tank is called hydraulic subsidence.
13.
Settling of discreteparticle
• A particle that does not alter its shape, size and weight while
settling or rising in water is called discrete particle
• The discrete particle will accelerate until drag force becomes
equal to gravitational force.
• At this stage particle attains uniform velocity called settling
velocity.
14.
Types of sedimentationtanks
• Based on method of operation :
1. Fill and draw type tanks
2. Continuous flow type tank
• Depending upon shape :
1. Rectangular tanks
2. Circular tanks
3. Hopper bottom tanks
• vf =flow velocity
• vs= terminal settling velocity of a particle that is just removed
when it enters at the water surface (H).
• Note:
1) All particles with terminal settling velocity ≥ vs are removed.
2) Only part of particles with settling velocity < vs are removed.
24.
Design criteria
• Detentionperiod
for plain sedimentation = 4 to 8 hour
for sedimentation with coagulant = 3 to 4 hour
• Depth of settling tank vary from 3 to 4 hour.
• S.O.R
for plain sedimentation = 500 – 750 lit/hr/m2
for sedimentation with coagulant = 1000 – 1250 lit/hr/m2
25.
Example
• Purification planthas estimated 11 MLD. Design the dimension
of suitable sedimentation tank.
Solution :
Quantity of water to be treated = 11 * 106 litres
= 11 *106 /( 1000 * 24 )
= 458.33 m3 / hour
Assume detention period T = 6 hour
velocity of flow V = 20 cm / minute = 0.2 m/minute
26.
• T =C / Q C = T * Q
= 6 * 458.33
= 2750 m3
Length of tank , L = Velocity × detention time
= 0.20 × ( 6 × 60 )
= 72 m
T = C/Q = L × B × D / Q
6 = 72 × B × D / 458.33
B × D = 39.18
Assume depth of water 4 m and free board 0.5 m
B × 4 = 38.19 B = 9.54 m
Provide rectangular tank of 72 m × 9.60 m × 4.5 m
27.
• Check forsurface overflow rate :
S.O.R = Q / L × V
= 458333.33 / ( 72 × 9.60 )
= 663 lit/hr/m2
for plain sedimentation tank S.O.R should between
500 to 700 lit/hr/m2
Purpose of Aerationin water
Treatment
1. Increase the dissolved oxygen concentration in water.
2. Decrease CO2 concentration thereby reduce its
corrosiveness.
3. Reduce taste and odour caused by dissolved gases such as
Hydrogen sulphide (H2S) and methane (CH4) that are
removed during aeration.
4. Oxidize iron and manganese from their soluble to
insoluble states and cause them to precipitate so that they
removed by sedimentation and filtration processes.
5. Remove certain volatile organic compounds
30.
Types of aeratorsused in water Treatment
1. Gravity Aerators: In gravity aerators, water is allowed to fall
by gravity such that a large area of water is exposed to
atmosphere, sometimes aided by turbulence. Cascade
aerators and Multi‐tray aerators are two examples of this
type.
2. Fountain Aerators : These are also known as spray aerators
with special nozzles to produce a fine spray.
3. Injection or Diffused Aerators : It consists of a tank with
perforated pipes, tubes or diffuser plates, fixed at the
bottom to release fine air bubbles from compressor unit.
4. Mechanical Aerators : Mixing paddles as in flocculation are
used. Paddles may be either submerged or at the surface.
• These arethe simplest of the free fall aerator.
• Weirs and waterfall of any kind are cascade aerators.
• It consist of series of steps usually 3 to 4 steps of concrete or
metal.
• The reduction of CO2 is about 50 to 60%.
33.
Inclined apron aerator
•In this water is allowed to fall along an inclined plane which is
usually studded with riffle plates in herring bone fashion.
• The breaking up to the sheet of water will cause agitation of
water and consequent aeration.
• It consistof a closed round or square containing a series of
closely stacked superimposed wood slat trays.
• Water enters the top of aerator and is evenly distributed of top
most tray.
• Air is supplied to bottom of aerator which discharges air and
gases to the atm.
36.
SPRAY AERATOR
• Inthis method water is sprinkled in air through
special nozzle which breaks the water into droplets
thus permitting the escape of dissolved gases.
37.
AIR DIFFUSION
• Inthis perforated pipe network is installed at
bottom of aeration tank, and compressed air is
blown through the pipe.
• Air diffuser basin have a detention period of about
15 minutes and a depth of 2 to 5 meter.