The document discusses sedimentation tanks, which use gravity to separate suspended solids from water. Sedimentation tanks work by slowing water flow so that particles heavier than water can settle to the bottom as sludge. There are four types of particle settling. Design considerations for sedimentation tanks include detention time, flow velocity, tank dimensions, depth, overflow rate, and slopes. An example is provided showing how to design a rectangular sedimentation tank based on flow rate and detention time.
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Solid liquid separation process in which a suspension is
separated into two phases –
Clarified supernatant leaving the top of the sedimentation
tank (overflow).
Concentrated sludge leaving the bottom of the
sedimentation tank (underflow).
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Laboratories Complex, Karachi
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Purpose of Settling
To remove coarse dispersed phase.
To remove coagulated and flocculated impurities.
To remove precipitated impurities after chemical
treatment.
To settle the sludge (biomass) after activated sludge
process / tricking filters.
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Laboratories Complex, Karachi
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Principle of Settling
Suspended solids present in water having specific
gravity greater than that of water tend to settle down
by gravity as soon as the turbulence is retarded by
offering storage.
Basin in which the flow is retarded is called settling
tank.
Theoretical average time for which the water is
detained in the settling tank is called the detention
period.
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Laboratories Complex, Karachi
Off: University Road, Karachi-75280.
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Laboratories Complex, Karachi
Off: University Road, Karachi-75280.
Types of Settling
Type I settling (free settling)
Type II settling (settling of flocculated
particles)
Type III settling (zone or hindered
settling)
Type IV settling (compression settling)
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Laboratories Complex, Karachi
Off: University Road, Karachi-75280.
Design parameters for settling tank
Types of settling
Overflow rate
m3m2/day
Solids loading
kg/m2/day
Depth
Detentio
n time
Average Peak Average Peak
Primary settling only 25-30 50-60 - - 2.5-3.5 2.0-2.5
Primary settling followed by
secondary treatment
35-50 60-120 - - 2.5-3.5
Primary settling with activated
sludge return
25-35 50-60 - - 3.5-4.5 -
Secondary settling for trickling
filters
15-25 40-50 70-120 190 2.5-3.5 1.5-2.0
Secondary settling for activated
sludge (excluding extended
aeration)
15-35 40-50 70-140 210 3.5-4.5 -
Secondary settling for extended
8-15 25-35 25-120 170 3.5-4.5 -
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Laboratories Complex, Karachi
Off: University Road, Karachi-75280.
Design Details
Detention period: for plain sedimentation: 3 to 4 h, and for
coagulated sedimentation: 2 to 2.5 h.
Velocity of flow: Not greater than 30 cm/min (horizontal
flow).
Tank dimensions: L:B = 3 to 5:1. Generally L= 30 m
(common) maximum 100 m. Breadth= 6 m to 10 m.
Circular: Diameter not greater than 60 m. generally 20 to
40 m.
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Depth 2.5 to 5.0 m (3 m).
Surface Overflow Rate: For plain sedimentation 12000 to
18000 L/d/m2 tank area; for thoroughly flocculated water
24000 to 30000 L/d/m2 tank area.
Slopes: Rectangular 1% towards inlet and circular 8%.
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Laboratories Complex, Karachi
Off: University Road, Karachi-75280.
Problem:
Design a rectangular sedimentation tank to treat 2.4
million litres of raw water per day. The detention period
may be assumed to be 3 hours.
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Laboratories Complex, Karachi
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Solution: Raw water flow per day is 2.4 x 106 L . Detention
period is 3h.
Volume of tank = Flow x Detention period = 2.4 x 106 x 3/24 =
300 m3
Assume depth of tank = 3.0 m.
Surface area = 300/3 = 100 m2
L/B = 3 (assumed). L = 3B.
3B2 = 100 m2 i.e. B = 5.8 m
L = 3B = 5.8 X 3 = 17.4 m
Hence surface loading (Overflow rate) = 2.4 x 106 =
100
24,000 L/d/m2
13. Pakistan Council of Scientific & Industrial Research
Laboratories Complex, Karachi
Off: University Road, Karachi-75280.