From Stokes’s law, the velocity of settling of small discrete particles is given by:
v=418(s-s_1 ) d^2 (3T+70)/100 ………….6.2
Where v = velocity of settling in mm/sec
s = specific gravity of particle
s1= specific gravity of water
d = diameter of particle in mm
T = temperature in degree Celsius.
Assuming each settleable particle in water is discrete with an average diameter of 0.09 mm and specific gravity 1.75 in water at 25oC;
v=418(1.75-1.00)〖(0.09)〗^2 ((3x25+70))/100
v = 3.6821 mm/s
Thus, the velocity of each settling particle is 3.6821 mm/s.
Number of tanks required = 2
Geometry of tank: Cylindrical, of uniform cross section
Height of tank = 5.6 m
Radius of tank = 14.2 m
Point of entry of raw water = 3.5 m above the tank floor.
In quiescent water, the time for a particle to move to the bottom of the tank is given by
time =(velocity of particle )/(height of entry of water)
=(3500 mm )/(3.6821mm/s)
= 950.5445 s
= 15.84 min.
Capacity (volume) of each tank = 〖πD〗^2/4 H
=〖22 x 28.4〗^2/(7 x 4) x 5.6
= 3,548.864 m3.
To know the point where the discharge of raw water on the tank to the treatment plant will be, the accumulated height of sludge after a month is calculated.
To calculate the volume of sludge produced per tank:
From material balance, 998.1214394 m3 of raw water produces 418 kg of sludge
Therefore, 3,548.864 m3 of raw water will produce 3,548.864 x 418 kg of sludge
998.1214394
= 1,486.2171 kg of sludge
Volume of sludge/day =(mass of sludge )/(density of sludge)
=(1,486.2171 )/(1,750)
= 0.8493 m3 of sludge.
Height of sludge/day =(Volume of sludge )/(Area of tank)
Where area of tank = πr^2
=(0.8493 x 7)/(22 x14.2 x 14.2)
= 1.3402 x 10-3 m
= 1.3402 mm/day
The height of sludge after 31 days = 31 x 1.3402
= 41.5462 mm
= 0.0415 m
The water outlet from the tank will be placed at a height of 0.3 m above the floor of the tank.
An emergency overflow weir will be placed at a distance of 0.1 m from the top of the open tank.
Thus, the effective water holding capacity of the tank = 〖22 x 28.4〗^2/(7 x 4) x 5.2
= 3,295.3737 m3.
v=418(s-s_1 ) d^2 (3T+70)/100 ………….6.2
Where v = velocity of settling in mm/sec
s = specific gravity of particle
s1= specific gravity of water
d = diameter of particle in mm
T = temperature in degree Celsius.
Assuming each settleable particle in water is discrete with an average diameter of 0.09 mm and specific gravity 1.75 in water at 25oC;
v=418(1.75-1.00)〖(0.09)〗^2 ((3x25+70))/100
v = 3.6821 mm/s
Thus, the velocity of each settling particle is 3.6821 mm/s.
Number of tanks required = 2
Geometry of tank: Cylindrical, of uniform cross section
Height of tank = 5.6 m
Radius of tank = 14.2 m
Point of entry of raw water = 3.5 m above the tank floor.
In quiescent water, the time for a particle to move to the bottom of the tank is given by
time =(velocity of particle )/(height of entry of water)
=(3500 mm )/(3.6821mm/s)
= 950.5445 s
= 15.84 min.
Capacity (volume) of each tank = 〖πD〗^2/4 H
=〖22 x 28.4〗^2/(7 x 4) x 5.6
= 3,548.864 m3.
To know the point where the discharge of raw water on the tank to the treatment plant will be, the accumulated height of sludge after a month is calculated.
To calculate the volume of sludge produced per tank:
From material balance, 998.1214394 m3 of raw water produces 418 kg of sludge
Therefore, 3,548.864 m3 of raw water will produce 3,548.864 x 418 kg of sludge
998.1214394
= 1,486.2171 kg of sludge
Volume of sludge/day =(mass of sludge )/(density of sludge)
=(1,486.2171 )/(1,750)
= 0.8493 m3 of sludge.
Height of sludge/day =(Volume of sludge )/(Area of tank)
Where area of tank = πr^2
=(0.8493 x 7)/(22 x14.2 x 14.2)
= 1.3402 x 10-3 m
= 1.3402 mm/day
The height of sludge after 31 days = 31 x 1.3402
= 41.5462 mm
= 0.0415 m
The water outlet from the tank will be placed at a height of 0.3 m above the floor of the tank.
An emergency overflow weir will be placed at a distance of 0.1 m from the top of the open tank.
Thus, the effective water holding capacity of the tank = 〖22 x 28.4〗^2/(7 x 4) x 5.2
= 3,295.3737 m3.
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