Design of Well Type Fall
Design of Well Type Fall
Design of Well Type Fall
OF 3 M HEIGHT
DATA
1 Height of fall 3m
2 General ground level 287.250 m
3 Full supply depth 0.5 m
4 Upstream CBL 287.711
5 Discharge 14.23 cusec
Q 0.40 cumec
Bed width upstream
6 1.2 m
and downstream
DESIGN
0.20 = 2.22*(0.33)^(3/2)*(l+0.4*n*0.33)
0.48 = l+0.132*n ……… ii)
= 1.60 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.4/(3.14/4*0.4^2)^2)/(2*9.81)] + [(0.4/
HL1 = (3.14/4*0.4^2)-0.42)^2/ (2*9.81)] +
[(0.012*10*(0.42)^2)/(2*9.81*1)] + [(0.42)^2/
(2*9.81)]
= 0.66
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.53 m
Scour Depth
q= 0.33 m
f= 1
Scour Depth R = 1.35*(q2/f)1/3 0.65 m
Depth Below bed 0.15 m
DESIGN OF WELL TYPE FALL AT 6110M OF LEFT CANAL
OF 3 M HEIGHT
DATA
1 Height of fall 3m
2 General ground level 283.815 m
3 Full supply depth 0.5 m
4 Upstream CBL 284.535
5 Discharge 14.23 cusec
Q 0.40 cumec
Bed width upstream
6 ssss m
and downstream
DESIGN
0.20 = 2.22*(0.33)^(3/2)*(l+0.4*n*0.33)
0.48 = l+0.132*n ……… ii)
= 1.60 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.4/(3.14/4*0.4^2)^2)/(2*9.81)] + [(0.4/
HL1 = (3.14/4*0.4^2)-0.42)^2/ (2*9.81)] +
[(0.012*10*(0.42)^2)/(2*9.81*1)] + [(0.42)^2/
(2*9.81)]
= 0.66
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.53 m
Scour Depth
q= #VALUE! m
f= 1
Scour Depth R = 1.35*(q2/f)1/3 #VALUE! m
Depth Below bed #VALUE! m
DESIGN OF WELL TYPE FALL AT 6925 M OF LEFT CANAL
OF 3 M HEIGHT
DATA
1 Height of fall 3m
2 General ground level 281.810 m
3 Full supply depth 0.5 m
4 Upstream CBL 281.507
5 Discharge 14.23 cusec
Q 0.40 cumec
Bed width upstream
6 1.2 m
and downstream
DESIGN
0.20 = 2.22*(0.33)^(3/2)*(l+0.4*n*0.33)
0.48 = l+0.132*n ……… ii)
= 1.60 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.4/(3.14/4*0.4^2)^2)/(2*9.81)] + [(0.4/
HL1 = (3.14/4*0.4^2)-0.42)^2/ (2*9.81)] +
[(0.012*10*(0.42)^2)/(2*9.81*1)] + [(0.42)^2/
(2*9.81)]
= 0.66
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.53 m
DATA
1 Height of fall 3m
2 General ground level 278.730 m
3 Full supply depth 0.5 m
4 Upstream CBL 278.483
5 Discharge 14.23 cusec
Q 0.40 cumec
Bed width upstream
6 1.2 m
and downstream
DESIGN
0.20 = 2.22*(0.33)^(3/2)*(l+0.4*n*0.33)
0.48 = l+0.132*n ……… ii)
= 1.60 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.4/(3.14/4*0.4^2)^2)/(2*9.81)] + [(0.4/
HL1 = (3.14/4*0.4^2)-0.42)^2/ (2*9.81)] +
[(0.012*10*(0.42)^2)/(2*9.81*1)] + [(0.42)^2/
(2*9.81)]
= 0.66
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.53 m
DATA
1 Height of fall 2m
2 General ground level 288.500 m
3 Full supply depth 0.49 m
4 Upstream CBL 288.534
5 Discharge 14.82 cusec
Q 0.42 cumec
Bed width upstream
6 1.25 m
and downstream
DESIGN
0.21 = 2.22*(0.32)^(3/2)*(l+0.4*n*0.32)
0.52 = l+0.128*n ……… ii)
= 1.58 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.42/(3.14/4*0.4^2)^2)/(2*9.81)] +
HL1 = [(0.42/(3.14/4*0.4^2)-0.44)^2/ (2*9.81)] +
[(0.012*10*(0.44)^2)/(2*9.81*1)] + [(0.44)^2/
(2*9.81)]
= 0.72
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.05 m
DATA
1 Height of fall 3m
2 General ground level 286.500 m
3 Full supply depth 0.49 m
4 Upstream CBL 286.466
5 Discharge 14.82 cusec
Q 0.42 cumec
Bed width upstream
6 1.25 m
and downstream
DESIGN
0.21 = 2.22*(0.32)^(3/2)*(l+0.4*n*0.32)
0.52 = l+0.128*n ……… ii)
= 1.58 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.42/(3.14/4*0.4^2)^2)/(2*9.81)] +
HL1 = [(0.42/(3.14/4*0.4^2)-0.44)^2/ (2*9.81)] +
[(0.012*10*(0.44)^2)/(2*9.81*1)] + [(0.44)^2/
(2*9.81)]
= 0.72
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.50 m
DATA
1 Height of fall 3m
2 General ground level 281.010 m
3 Full supply depth 0.49 m
4 Upstream CBL 283.023
5 Discharge 14.82 cusec
Q 0.42 cumec
Bed width upstream
6 1.25 m
and downstream
DESIGN
0.21 = 2.22*(0.32)^(3/2)*(l+0.4*n*0.32)
0.52 = l+0.128*n ……… ii)
= 1.58 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.42/(3.14/4*0.4^2)^2)/(2*9.81)] +
HL1 = [(0.42/(3.14/4*0.4^2)-0.44)^2/ (2*9.81)] +
[(0.012*10*(0.44)^2)/(2*9.81*1)] + [(0.44)^2/
(2*9.81)]
= 0.72
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.50 m
DATA
1 Height of fall 3m
2 General ground level 280.030 m
3 Full supply depth 0.49 m
4 Upstream CBL 279.683
5 Discharge 14.82 cusec
Q 0.42 cumec
Bed width upstream
6 1.25 m
and downstream
DESIGN
0.21 = 2.22*(0.32)^(3/2)*(l+0.4*n*0.32)
0.52 = l+0.128*n ……… ii)
= 1.58 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.42/(3.14/4*0.4^2)^2)/(2*9.81)] +
HL1 = [(0.42/(3.14/4*0.4^2)-0.44)^2/ (2*9.81)] +
[(0.012*10*(0.44)^2)/(2*9.81*1)] + [(0.44)^2/
(2*9.81)]
= 0.72
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.50 m
DATA
1 Height of fall 4.5 m
2 General ground level 278.625 m
3 Full supply depth 0.6 m
4 Upstream CBL 279.093
5 Discharge 20 cusec
Q 0.57 cumec
DESIGN
0.29 = 2.22*(0.4)^(3/2)*(l+0.4*n*0.4)
0.51 = l+0.16*n ……… ii)
= 1.69 m/s
Now
Loss of head between the inlet well and the d/s FSL is
= [0.5*(V2^2)/(2g)] + [(V2-V3)^2/(2g)] + [(f'L(V3)^2)/(2gd)] + [(V3)^2/ (2g)]
Let us assume
Length of pipe = 10 m
f' (Darcey's coeff of
friction) = 0.012 m
[0.5*(0.57/(3.14/4*0.4^2)^2)/(2*9.81)] +
HL1 = [(0.57/(3.14/4*0.4^2)-0.6)^2/ (2*9.81)] +
[(0.012*10*(0.6)^2)/(2*9.81*1)] + [(0.6)^2/
(2*9.81)]
= 1.34
Now the dia of the inlet well may be kept at about 1.5X
i.e., X = 1.90 m
Scour Depth
q= 0.29 m
f= 0.9
Scour Depth (R) = 1.35*(q2/f)1/3 0.61 m
Depth Below bed 1.5R-d 0.32 m