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Hydraulic Design
Headloss calculation Sheet...
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Vijay Tamrakar
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P hawa Khola HEP
Appendix Appendix D: Hydraulic Hydraulic Design Calculation Calculation
DED Vol: III Appendices
Project Name : Location :
Descriptions
Sym b o ls
Un it s
Qdesign_min
m /s
Qsettling_min
3
m /s
Design Discharge to Turbine
Qturbine
Diameter of Penstock
D Lpenstock
Discharge through intake Discharge to Settling Basin
Total Penstock Length Installed Capacity
Phawa Khola Hydropower Project
Taplejung Type : Detail Design Head Loss Calculation Calculation for full Design Flow (Ashar to Aswin) Title : Head
3
Valu es
Remarks
2.52
HW components L osses upto Siphon
1.23
m
2.31
Siphon Losses
2.01
m
m /s
2.10
HW components L osses from S iphon to Fore
8.01
m
m
1.10
Losses in Pressure Pipe
1.88
m
m MW
483.00 5.16
3
Total Losses
13.126
Gross Head
322.500 309.374
Net Head
m m
Intake Orifice Losses No. Of orifice
Width
Height
Area
Velocity
Coeffcient
Head loss
Description
-
B
H
V =Qdesign /A
C
HL=V^2/(2xg)/C
-
m
m
A=BxH m
m/s
-
m
Intake
2.00
1.50
1.20
3.60
0.70
0.66
0.0381
No. Of orifice
Width
Height
Area
Velocity
K - entrance loss coefficient
Head loss
-
B
H
V =Qdesign /A
a constant
HL=KxV^2/(2xg)
m/s
-
m
0.70
0.10
0.0025
Intake Entrance Losses Description Applicable
Intake
-
m
m
A=BxH m
2.00
1.50
1.20
3.60
Intake Trashrack Loss Description Applicable
Trashr Trashrack ack
No.
Width
Height
Area
Velocity
-
B
H
V =Qdesign /A
0.70
-
m
m
A=BxH m
2.00 2.00
1.50
1.20
3.6
m/s
k-bar shape coefficient
t-thickness of rack bars
1.83
b-clear spacing between bars
-Rack inclination to the horizontal
Head loss
-
-
-
mm
deg
mm
m
10
80
75
0.0062
HL=k(t/b)^(1/8)xsin xV^2/(2xg)
Gravel Trap Loss Length
Slope
L
S
m 7.70
0.002
fc-Contraction coefficient
Length
Slope
-
L
S
Description Applicable
GT
Head loss HL= L x S m
0.0154
Gravel Trap Transition Loss (Contraction) Description Applicable
GT
Before transition Height Area H1 A1 = B1 x H1 2 m m
Width B1 m
3.00
Velocity V1 =Qdesign /A1 m/s
W i dt h B2 m
1.20
3.60
0.70
1.50
Width
Height
Area
Velocity
After transition Height Area H2 A2 = B2 x H2 2 m m
0.98
1.47
Head loss
Velocity V2 =Qdesign /A2 m/s
-
m
-
HL=fc x (V2 - V1)^2/(2g) + L x S m
1.57
0.35
6.5
0.002
0.0265
Approach canal Trashrack Loss No.
Description
NA
Trashr Trashrack ack
B
H
k-bar shape
t-thickness
coefficient
of rack bars
-Rack inclination
b-clear spacing between bars Head loss
1.83
to the horizontal
-
-
-
mm
deg
mm
m
10
75
100
0.0000
m
m
A=BxH m
V =Qdesign /A
-
1.00 1.00
3.00
0.98
2.94
0.79
No. Of gate
Width
Height
Area
Velocity
K - entrance loss coefficient
Head loss
-
B m
H m
A=BxH m
V =Qdesign /A m/s
a constant -
HL=KxV^2/(2xg) m
1.00
1.50
0.98
1.47
1.57
0.10
0.0126
m/s
HL=k(t/b)^(1/8)xsin xV^2/(2xg)
Approach canal entrance loss Description Applicable
AC
Phawa Khola HEP
Appendix D: Hydraulic Design Calculation
DED Vol: III Appendices
Project Name : Location :
Descriptions
Symbols
Units
Qdesign_min
m /s
Qsettling_min
3
m /s
Design Discharge to Turbine
Qturbine
Diameter of Penstock
Phawa Khola Hydropower Project
Taplejung Type : Detail Design Title : Head Loss Calculation for full Design Flow (Ashar to Aswin)
3
Values
Remarks
2.52
HW components L osses upto Siphon
1.23
m
2.31
Siphon Losses
2.01
m
m /s
2.10
HW components L osses from S iphon to Fore
8.01
m
m
1.10
Losses in Pressure Pipe
1.88
m
Total Penstock Length
D Lpenstock
m
483.00
Approach Canal Bend loss Width Description B
Height H
Velocity V =Qdesign /A
Bend angle 1 1
m/s
deg
deg
deg
deg
deg
deg
-
-
-
-
-
m
1.57
0
0
0
0
0
0
0.000
0.000
0.000
0.000
0.000
0.0000
Discharge through intake Discharge to Settling Basin
NA
Approach canal
3
m
m
Area A=BxH m2
1.50
0.98
1.47
Total Losses Bend angle 2 Bend angle 3 2 3
Approach canal to Settling Basin Length Segment L m Applicable
1 20 AC
60
Bend angle 4 4
Bend angle 5 Bend angle 6 5 6
Factor1
13.126 Factor2
Factor3
Factor4
Factor6
Head loss HL=F x V^2/(2g)
Slope
Head loss
S -
HL=L*S m
0.0020 0.0000
0.1200
Desander Basin entrance loss Description
No. Of gate
Width
Height
Area
Velocity
K - entrance loss coefficient
Head loss
-
B m
H m
A=BxH 2 m
V =Qdesign /A m/s
a constant -
HL=KxV^2/(2xg) m
2.00
1.00
0.98
1.96
1.18
0.10
0.0071
Velocity V1 =Qdesign /A1
Width B2
Applicable
DB
Desander Basin Transition Loss (Expansion) Description Applicable
SB
Before transition Height Area H1 A1 = B1 x H1 m m
Width B1 m
1.00
0.98
0.98
m/s
m
2.36
4.00
After transition Height Area H2 A2 = B2 x H2 m m
2.20
8.80
Velocity V2 =Qdesign /A2
fc-Expansion coefficient
Length
Slope
-
L
S
Head loss HL=fc x (V2 - V1)^2/(2g) + L x S
m/s
-
m
-
m
0.26
0.4
32.00
0.001
0.1108
Length
Slope
L
S
m 32.00
0.001
Desander Basin Loss Description Applicable
GT Headrace Canal entrance loss No. Of gate Description Applicable -
HC
2.00
Head loss HL= L x S m
0.0213
Width
Height
Area
Velocity
K - entrance loss coefficient
Head loss
B m
H m
A=BxH m
V =Qdesign /A m/s
a constant -
HL=KxV^2/(2xg) m
1.50
1.50
4.50
0.47
0.10
0.0011
Velocity V1 =Qdesign /A1
Width B2
Headrace canal Transition Loss (Expansion) Description Applicable
HC
Width B1 m
4.00
Before transition Height Area H1 A1 = B1 x H1 m m
2.20
8.80
m/s
m
0.26
1.25
After transition Height Area H2 A2 = B2 x H2 m m
1.19
1.49
Velocity V2 =Qdesign /A2
fc-Expansion coefficient
Length
Slope
-
L
S
Head loss HL=fc x (V2 - V1)^2/(2g) + L x S
m/s
-
m
-
m
1.55
0.4
10.00
0.002
0.0504
Phawa Khola HEP
Project Name : Location :
Descriptions
Symbols
Units
Qdesign_min
m /s
Qsettling_min
3
m /s
Design Discharge to Turbine
Qturbine
Diameter of Penstock
D Lpenstock
Discharge through intake Discharge to Settling Basin
Total Penstock Length
Phawa Khola Hydropower Project
Taplejung Type : Detail Design Title : Head Loss Calculation for full Design Flow (Ashar to Aswin)
3
Values
Remarks
2.52
HW components L osses upto Siphon
1.23
m
2.31
Siphon Losses
2.01
m
m /s
2.10
HW components L osses from S iphon to Fore
8.01
m
m
1.10
Losses in Pressure Pipe
1.88
m
m
483.00
3
Total Losses
Headrace Canal from Desander to Syphon Length Segment L Applicable
1 Total
Slope S -
m
0.002
0.8167 0.8167
No. Of gate
SC
Height
Area
Velocity
K - entrance loss coefficient
Head loss
-
B
H
a constant
HL=KxV^2/(2xg)
m
m
A=BxH m2
V =Qdesign /A
-
m/s
-
Width
m
0.95
2.21
0.08
0.0199
1.00
Headloss in Syphon Barrel Length Segment L
Velocity
Head loss HL=L*S
0.026
1.9518
m
334.4
2.210
1.9518
No. Of gate
Width
Height
Area
Velocity
K - exit loss coefficient
Head loss
-
B
H
V =Qdesign /A
a constant
HL=KxV^2/(2xg)
-
m
m
A=BxH m2
Applicable
SC
m/s
-
m
2.21
0.15
0.0373
Headrace Canal from Syphon Barrel to Forebay Length Segment L
1 HC
F- friction loss coefficient
V
m
Syphon Barrel Exit loss Description
Applicable
Head loss HL=L*S
m
Applicable
1 SC
13.126
490
Syphon Barrel entrance loss Description
Applicable
Appendix D: Hydraulic Design Calculation
DED Vol: III Appendices
Slope S
Head loss HL=L*S
m
-
m
4769.57
0.002
7.9493 7.9493
Forebay and Transition Loss Description Applicable
HC
Width B1 m
Before transition Height Area H1 A1 = B1 x H1 2 m m
Velocity V1 =Qdesign /A1 m/s
Width B2 m
1.23
5.00
1.25
1.50
1.88
No.
Width
Height
Area
Velocity
-
B m
H m
A=BxH m
V =Qdesign /A m/s
1.00
6.00
3.00
18
0.14
After transition Height Area H2 A2 = B2 x H2 2 m m
3.00
15.00
fc-Expansion coefficient
Length
Slope
Velocity V2 =Qdesign /A2 m/s
-
L
S
-
m
-
HL=fc x (V2 - V1)^2/(2g) + L x S m
0.15
0.4
20.00
0.002
0.0570
Head loss
Forebay Trashrack Loss Description Applicable
Trashrack
k-bar shape coefficient
1.83
t-thickness of rack bars
-Rack inclination to the horizontal
b-clear spacing between bars
Head loss
-
-
-
mm
deg
mm
HL=k(t/b)^(1/8)xsin xV^2/(2xg) m
10
80
75
0.0002
Phawa Khola HEP
Appendix D: Hydraulic Design Calculation
DED Vol: III Appendices
Project Name : Location :
Descriptions
Symbols
Units
Qdesign_min
m /s
Qsettling_min
3
m /s
Design Discharge to Turbine
Qturbine
Diameter of Penstock
D Lpenstock
Discharge through intake Discharge to Settling Basin
Total Penstock Length Penstock Bend Losses after bifurcation Bend angle Bend number 1 deg Applicable
0+005.00 0+345.00 Total
30.00 30.00
3
Phawa Khola Hydropower Project
Taplejung Type : Detail Design Title : Head Loss Calculation for full Design Flow (Ashar to Aswin) Values
Remarks
2.52
HW components L osses upto Siphon
1.23
m
2.31
Siphon Losses
2.01
m
m /s
2.10
HW components L osses from S iphon to Fore
8.01
m
m
1.10
Losses in Pressure Pipe
1.88
m
m
483.00
3
R/D
Factor K90 0.214*(R/D)^-(0.66)
5 5
0.074 0.074
Total Losses Reduction Factor F -0.00007*Φ^2+0.017*Φ+0.036
0.483 0.483
13.126
K factor K90*F
Diameter D m
Area A m²
Velocity V m/s
Head loss HL=F x V^2/(2g) m
0.036 0.036
1.100 1.100
0.950 0.950
2.210 2.210
0.009 0.009 0.018
PenstockValve loss Bend number Applicable
1 total
Factor F
Head loss HL=F x V^2/(2g)
mks
m
0.3
0.075 0.075
Remarks
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