AIR REAL SDSDS HFT FOR NFJ SEDFEFXSAL.ppt

RIAL

1. 5.7 Flocculation
 
Flocculation is the process of gentle and continuous stirring
of coagulated water for the purpose of forming flocs
through the aggregation of the minute particles present in
the water. It is thus the conditioning of water to form flocs
that can be readily removed by settling, dissolved air
flotation or filtration, Fig (5.8). The efficiency of the
flocculation process is largely determined by the number of
collisions between the minute coagulated particles per unit
of time.
 
 

2. Fig (5.8) Schematic representation of flocculation
process

3. There are mechanical and hydraulic flocculators. In
mechanical flocculators the stirring of the water is
achieved with devices such as paddles, paddle reels or
rakes, as shown in Fig. (5.9).

4. There are mechanical and hydraulic flocculators. In mechanical
flocculators the stirring of the water is achieved with devices such as
paddles, paddle reels or rakes, as shown in fig (5.9).
Fig. (5.9) Mechanical flocculators

5. These devices can be fitted to a vertical or horizontal shaft.
Vertical shaft flocculators are usually placed in a square tank with
several chambers (four or more). With horizontal shaft flocculators
having a traverse flow, one should provide at least four rows of shafts,
with partitions of baffles, so as to avoid short-circuiting.
The hydraulic flocculators utilize horizontal or vertical hydraulic
baffled channel as shown in Fig. (5.10). They are rarely used in large
size of water treatment plant, because of their sensitivity to flow
changes.

6. Fig (5.10) Hydraulic flocculators

12. 5.7.1 Agitation requirement:
The detention time in the flocculation tank is higher than that in
rapid mixing tank. Detention time from 20 to 30 min. Typical
velocity gradient G for flocculators range from 25 to 65 s-1. The
velocity gradient can be obtained by using eq. (5.1). In the case of
paddle wheel mixers (horizontal), the water power is given by:
2
v
3
AC
p
d


13. Where
p: power imparted to water, watt
Cd: drag coefficient, which varies with the length to width ratio of
the paddle blades. (L/W = 5)……..Cd = 1.2
(L/W = 20)………Cd = 1.5
A: area of the paddles, m2
v: velocity of the paddle relative to the water, m/s
The velocity of the paddle relative to the water is 75% of the
absolute peripheral velocity of the paddle.
v = Πnd
Where
n: rotational speed of the blades, rps
d: diameter from center to center of each paddle blade, m
The key design factor in flocculation tank is the value of GT (G*D.T) because
the number of particles collisions within the tank is directly proportional to the
value of GT. Typical value between 10000 and 150000.

14. Design of rapid mix and flocculation tanks
Flow rate = 113500 m3/day
1. Rapid mix: Number of tanks = 4
Number of stage = 1
D.T = 30 sec
G = 950 s-1
2. Flocculation tank: Number of tanks = 4
Number of stage = 3
D.T = 30 min total, 10 min for each stage
G = 60 s-1 (for first stage)
G = 30 s-1 (for second stage) G = 10 s-1 (for third stage)

19. Design flocculation tank
 
Volume = Q*D.T= 0.328 m3/s* (30*60)sec = 590 m3
 
Volume of each stage of the tank = 590 / 3 = 197 m3
 
Width of flocculation tank equal to the width of sedimentation tank,
then in this example use w = 18.4 m, length of each stage = depth
Vol = 18.4*d*d Þ 197 = 18.4*d2 Þ d = 3.27 m use 3.3 m
Vol = 18.4* 3.32 =199 m3
The water flows from one stage to the other through a baffle wall.
Total length of three stage = 3.3*3 = 10 m, fig (2)
Volume of each tank = 18.4 *10*3.3 m3
 

21. Flocculator power requirement
G1 stage = 60 s-1, volume of each stage = 199 m3
P1 stage = 602*199*(1.03*10-3) = 0.737kw
Pm=P/(Em*Ebearings)= 0.737/(0.9*0.7) = 1.16kw
P2 stage= 302*199*(1.03*10-3) = 0.184kw
Pm=0.184 /(0.9*0.7) = 0.29 kw
P3 stage= 152*199*(1.03*10-3) = 0.046 kw
 
Pm=0.046 /(0.9*0.7) = 0.073 kw
 
Size and number of paddle
 
- Each segment =3.2 m long
 
- Paddle wheel diameter = 85% of water depth
paddle diameter = 0.85*3.3 = 2.9, see fig (2)

22. Each stage of flocculation tank is provided with 5
segments and each segment has a 12 paddle blades. Each
paddle blade is 20 cm wide and 3.2 m long. The space
between two blades is 15 cm, as shown in fig (3).
Fig (3) Paddle blades for one segment

23. Calculate flocculator speed requirement
For paddles are placed at each location (see fig 4), 2.7 m (2.9 –
0.2), 2 m (2.7- (0.1*2 - 0.15*2)), 1.3 m center to center. Therefore,
the rotational speed is calculated by:

24. A1, A2 and A3: area of paddles at each location.
 
v1, v2 and v3: velocity of each paddle blade relative to the
water.
A1 = A2 = A3 = 5 segments per stage * 4 paddle blades at
each location per segment * 3.2 m * 0.2 m = 12.8 m2
v1 = pnreq d1= 0.75pnabs d1
 
v2 = pnreq d 2= 0.75pnabs d 2
 
v3 = pnreq d3= 0.75pnabs d3

26. Effluent structure (diffusion wall)
 
The diffusion wall separating flocculation and
sedimentation tanks is of concrete, with circular ports.
Diffusion wall is used to distribute the flow into the
sedimentation tank and consequently to prevent floc
breakup.
Let velocity through the port = 0.15 m/sec (to prevent
floc breakup)
A= Q/v= 0.328/0.15=2.187 m2
 
If diameter of port= 12.5 cm