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© Lahmeyer International (India) Pvt. Ltd. © Lahmeyer International (India) Pvt. Ltd.
One-dimensional sediment modelling for Chuzachen and Devsari hydroelectric power projects to check the feasibility of reservoirs’ usage as pseudo-desanders Author and Presenter : Pradyumna Machhkhand Senior Manager (Hydropower & Water Resources)| Lahmeyer International (India) Pvt. Ltd. | Gurgaon-122002
1
© Lahmeyer International (India) Pvt. Ltd.
Outline of the presentation
2
Introduction
Background Information
Reservoir Sedimentation
Sediment Modelling
Theory
Case Studies
Modelling Scheme
Model Set Up
Data Organization
Results
Comparison
Conclusion
Model Description
© Lahmeyer International (India) Pvt. Ltd.
• Reservoir sedimentation in hydroelectric projects (HEP): a major problem that interrupts the smooth functioning of hydropower plants.
A schematic and classical illustration of reservoir sedimentation
Introduction
3
© Lahmeyer International (India) Pvt. Ltd.
• In general, the problem is seen as a big hindrance and therefore, as a remedial measure – “n” number of desanders, based on studies, are usually proposed to manage the sediment removal operation.
• The presented case studies foray into the primary investigation of reservoir sedimentation prior to making decisions on sediment management.
• The investigation of sediments lies on two basic searches:
Where & How Much
Introduction
4
To examine the location and capacity of the reservoir in discrete form
To understand the relation between sediment concentration and discharge in the reservoir
© Lahmeyer International (India) Pvt. Ltd.
• Two different hydroelectric projects have been studied: a. Devsari HEP (Devsari Reservoir) b. Chuzachen HEP (Rangpo Reservoir & Rongli Reservoir) • Project features:
contd...
Background information
5
Project features Devsari HEP Chuzachen HEP
(Rangpo)
Location Uttarakhand, India Sikkim, India
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Background information
6
Project features Devsari HEP Chuzachen HEP
(Rangpo)
Type of structure Dam Dam
Height of structure 35m 48m
Extent of reservoir 4.8Kms from dam axis 508m from dam axis
Storage 9.026 Mm3 0.360 Mm
3
…contd
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• Empirical methods
a. Advantage : explicit methods (such as, Hazen, Vetter, and Camp), computational ease while computing the sediment trap efficiency.
b. Limitations : i. cover only the settling phase of reservoir operation, ii. and other factors which are NOT included in the empirical methods are:
the sediment transporting capacity of flow in a settling reach, the change in conditions as reservoir fills with sediment, the effect of variation in flow depth down a basin or reservoir, and the additional turbulence caused by inlet condition to a basin or
reservoir. contd...
Reservoir sedimentation
7
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• 1-dimensional numerical model
a. Advantages :
models the effect of turbulence in sediment movement and mass deposition,
not only simulates deposition, but also sluicing,
does not require grids to approximate cross-sections,
and requires less field data to set up.
Reservoir sedimentation
8
…contd
© Lahmeyer International (India) Pvt. Ltd.
• 1-dimensional numerical model
b. Limitations:
does not offer a detailed view of hydrodynamics of reservoir
system like 2-D or 3-D models.
Although 2-D or 3-D models have certain advantages, but at the cost of a
longer computational time and substantial amount of field data to
capture the complexities of 2-D or 3-D flow.
contd...
Reservoir sedimentation
9
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• SHARC , a software developed by HR Wallingford, UK, is a suite of integrated
programs designed to assist in the identification and solution of sediment problems at intakes in rivers and canal systems.
• DOSSBAS stands for Design of Sluiced Settling Basins.
• DOSSBAS is tool built within SHARC to model sediment depositions in basins/reservoirs and can model both regular and irregular basins.
• Two suites of DOSSBAS: 1) Deposition Model. 2) Sluicing Model.
Model description : DOSSBAS tool of SHARC
10
contd…
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• Deposition model
Assumptions: o the flow is steady,
o the velocities and concentrations are constant across the width of the
channel,
o and the concentrations in one size fraction do not affect other size fraction.
Model description : DOSSBAS tool of SHARC
11
…contd
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• Deposition model [Basic equation of turbulence (Dobbins ,1994)]
…Equation (1)
= sediment diffusion coefficient in y-direction (m2/sec) , = sediment diffusion coefficient in x-direction (m2/sec), = and settling velocity (formula by Gibbs et al, 1971) of sediment for the sediment size fraction (j) (m/sec).
Model description : DOSSBAS tool of SHARC
12
…contd
2
2
2
2
x
C
y
C
yV
y
C
x
Cu
j
x
jy
sj
j
y
j
where, u = flow velocity at height y above the bed (m/sec), y = height above bed (m), Cj = sediment concentration at height (y) above bed for size fraction( j), x = distance co-ordinate along channel (m),
y
x
sjV
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• Deposition model
Model description : DOSSBAS tool of SHARC
13
…contd
© Lahmeyer International (India) Pvt. Ltd.
Deposition model : Turbulent diffussion within a sub-reach
14
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•
Deposition model : Boundary conditions
15
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Overall structure of deposition model
16
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• Sluicing model
Sluicing model simulates only sand movements. It is assumed that any silt in the exposed bed material is sluiced instantly and therefore, only sand transport controls the sluicing rates.
Diffusion is not a dominant process in sluicing. Sluicing is modelled using equation,
Note: The threshold value to differentiate between silt and sand in DOSSBAS is 63 micron (default).
Model description : DOSSBAS tool of SHARC
17
…contd
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Overall structure of sluicing model
18
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Modelling scheme of reservoir sediment management plan
Modelling scheme
19
contd…
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Modelling scheme
20
…contd
• Set of parameters
X1 is the set of input parameters, viz., reservoir geometry, and sediment data
X2 is the set of parameters that includes the temperature, and the sand concentrations to be applied in both deposition and sluicing model.
The input parameters for deposition model can be expressed as, (X1 ∪ X2).
The set X3 is composed of additional parameters such as, flushing/sluicing discharge, the water level at the time of sluicing, and the duration of sluicing.
Y1 is the set of longitudinal bed profiles, which are results of deposition models.
The input parameters for sluicing model can be expressed as, (Y2 ∪ X2 ∪ X3).
The set Y2 comprises results of sluicing models in terms of elapsed time for flushing out the sediments and change in bed profiles at different time.
© Lahmeyer International (India) Pvt. Ltd.
• Hydrological year mean flow duration curves
Data organization
21
contd…
0
20
40
60
80
100
120
140
160
180
200
220
240
0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100%
Dis
char
ge (m
3/s
ec)
Exceedance probability (%)
Flow duration curve divisions: Devsari HEP
Flow duration curve
Qdesign (Intake) = 120.76 m3/sec
Division3 Qm = 44.8 m3/sec
Division2 Qm = 160.1 m3/sec
Division1 Qm = 205.3 m3/sec
0
20
40
60
80
100
120
140
160
0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100%
Dis
ch
arg
e (cum
ec)
Exceedance Probability (%)
Flow duration curve divisions : Rangpo
Flow duration curve
Qm = 33.2 m3/sec (Division 3)
Qm= 95.8 m3/sec (Division 1)
Qm= 58.1 m3/sec (Division 2)
Qm= 8.4 m3/sec (Division 4)
Qdesign = 21.5 m3/sec
© Lahmeyer International (India) Pvt. Ltd.
• Pre-processed data: average discharge and mean concentration
Data organization
22
contd…
Divisions
Devsari Rangpo
Qm
Mean conc.
Qm
Mean conc.
m3/s ppm m3/s ppm
1 205.3 511 95.8 707
2 160.1 436 58.1 389
3 44.8 192 33.2 187
4 - - 8.4 47
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• Optimization of input parameters
Data organization
23
contd…
y = 16.54x0.6445
R² = 0.6115
0
100
200
300
400
500
600
700
800
900
0 50 100 150 200 250
Me
an
Co
nc
en
tra
tio
n [
pp
m]
Mean Discharge [m3/s]
Mean discharge vs mean concentration
Obs.Mean …Power (Obs.Mean …
Devsari Reservoir
6445.054.161
xCm
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• Optimization of input parameters
Data organization
24
…contd
Rangpo Reservoir
o from the table of the pre-processed data, the annual sediment volume of Rangpo is about 70% the capacity of the Reservoir, and therefore, it is quite conservative to adopt the same values.
© Lahmeyer International (India) Pvt. Ltd.
• Bed gradation curves
Model setup
25
contd…
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• Input parameters
Model setup
26
…contd
Divisions
Flow
Sediment concentration
Deposition cycle time
Flushing discharge
Silt Sand
m3/sec ppm ppm Days Hours m3/sec
1 205.3 465 199 37 876 84.5
2 160.1 397 170 44 1051 39.3
3 44.4 174 74 285 6833 NA
Divisions
Flow
Sediment Concentration
Deposition cycle time
Flushing discharge
Silt Sand
m3/sec ppm ppm Days Hours m3/sec
1 95.8 495 212 37 876 74.3
2 58.1 273 117 37 876 36.6
3 33.2 131 56 73 1752 11.7
4 8.4 33 14 219 5256 NA
Devsari Rangpo
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• Input parameters
Model setup
27
…contd
© Lahmeyer International (India) Pvt. Ltd.
• Deposition model: Devsari
Results
28
1265
1270
1275
1280
1285
1290
1295
1300
1305
0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000
Distance downstream (m)
Minimum bed lev el (m)
Bed lev els at time 0.00 (hours )
Bed lev els at time 146.00 (hours )
Bed lev els at time 292.00 (hours )
Bed lev els at time 438.00 (hours )
Bed lev els at time 584.00 (hours )
Bed lev els at time 730.00 (hours )
Bed lev els at time 876.00 (hours )
Final w ater lev el
Longitudinal Profile Down Basin
Ele
vati
on
(m
)
Divisions
Sediment Volume
Outflow Sediment
Trap Efficiency
Reservoir Storage
Silt Sand Silt Sand Silt Sand Before run
After run
Mm3 Mm3 PPM PPM % % Mm3 Mm3
1 0.1 0.1 215 0 53.7 100.0 9.1 8.9
2 0.1 0.1 164 0 58.6 100.0 9.1 8.9
3 0.1 0.1 35 0 79.8 100.0 9.1 9.0
contd…
© Lahmeyer International (India) Pvt. Ltd.
• Sluicing model: Devsari
1265
1270
1275
1280
1285
1290
1295
1300
0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000
Distance downstream (m)
Minimum bed lev el (m)
Bed lev els at time 0.000 (hours )
Bed lev els at time 3.000 (hours )
Bed lev els at time 6.000 (hours )
Bed lev els at time 9.000 (hours )
Bed lev els at time 12.000 (hours )
Bed lev els at time 14.442 (hours )
Longitudinal Profile Down Basin
Elev
atio
n (m
)
Results
29
contd… …contd
Divisions
Volume removed Elapsed time for
flushing
Silt Sand Total
sediment
Mm3 Mm3 Mm3 Hours
1 0.1 0.1 0.2 14.44
2 0.1 0.1 0.2 28.59
3 NA
© Lahmeyer International (India) Pvt. Ltd.
• Deposition model: Rangpo
Results
30
contd…
880
885
890
895
900
905
910
915
0 100 200 300 400 500 600
Distance downstream (m)
Minimum bed lev el (m)
Bed lev els at time 0.00 (hours )
Bed lev els at time 146.00 (hours )
Bed lev els at time 292.00 (hours )
Bed lev els at time 438.00 (hours )
Bed lev els at time 584.00 (hours )
Bed lev els at time 730.00 (hours )
Bed lev els at time 876.00 (hours )
Final w ater lev el
Longitudinal Profile Down Basin
Ele
va
tio
n(m
)
Divisions
Sediment Volume
Outflow Sediment
Trap Efficiency
Reservoir Storage
Silt Sand Silt Sand Silt Sand Before
run After run
Mm3 Mm3 PPM PPM % % Mm3 Mm3
1 0.013 0.045 350.0 5.0 12.6 97.5 0.36 0.31
2 0.009 0.015 217.0 1.0 20.4 99.3 0.36 0.34
3 0.007 0.008 89.0 0.0 31.7 100.0 0.36 0.35
4 0.003 0.002 14.0 0.0 58.8 100.0 0.36 0.36
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• Sluicing model: Rangpo
Results
31
contd… …contd
880
885
890
895
900
905
910
0 100 200 300 400 500 600
Distance downstream (m)
Minimum bed lev el (m)
Bed lev els at time 0.000 (hours )
Bed lev els at time 0.200 (hours )
Bed lev els at time 0.400 (hours )
Bed lev els at time 0.410 (hours )
Longitudinal Profile Down Basin
Ele
vati
on
(m)
Divisions
Volume removed Elapsed time for
flushing
Silt Sand Total
sediment
Mm3 Mm3 Mm3 Hours
1 0.014 0.043 0.06 0.41
2 0.009 0.015 0.02 0.35
3 0.005 0.008 0.01 0.79
4 NA
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• Velocities and required length of reservoirs to settle 0.2mm particle:
Comparison with empirical method
32
Devsari Rangpo Units
Full reservoir level (FRL) = 1300 910 MASL
Minimum drawdown level(MDDL) = 1295 893 MASL
Division1 average discharge (Qa) = 205 90 m3/sec
The approximate average area of flow (A) = 4700 1978 m2
The corresponding flow through velocity (V) = Qa/A = 0.044 0.046 m/sec
Mean flow through velocity for 0.2mm particle to settle down, v’ = 0.2 0.2 m/sec
Settling velocity of 0.2mm particle, w = 0.022 0.022 m/sec
Length of reservoir required to settle 0.2mm particle, L*= v’/w x ( FRL-MDDL) = 45.5 154.5 m
Mid-Length from dam axis of reservoir, L = 2500 254 m
…contd
© Lahmeyer International (India) Pvt. Ltd.
• It can be safely inferred from the model results that the sediment grain size of 0.2mm and greater than 0.2mm shall be settling down in the reservoirs.
• If periodical flushing operations are realized during the whole life of the
reservoir, the entrance sill of the intake will not be affected by the deposited sediments; as it is already being witnessed in the model studies.
• The model studies have potential scopes to enhance the analysis; the sensitivity analysis of the models is one of them.
Conclusion
33
contd…
© Lahmeyer International (India) Pvt. Ltd.
• It would be in the interest of HEPs, if the utility of the desanders decelerates before placing them in the planning stages, thereby encouraging physically-based hydraulic modelling study of the sediments in the interim to assess whether the reservoirs are self-sufficient for managing the sediment processes or not.
• The case studies of this paper offer supporting results to the usage of
reservoirs for sediment management, but since the rapidification of desanders are commonly observed in HEPs; despite the reservoirs being gigantic in size, the term “pseudo-desanders”, used in the title of the paper, for reservoirs appears reasonable.
Conclusion
34
…contd
© Lahmeyer International (India) Pvt. Ltd.
• This work would have been due without the moral support of my wife, Imane Ibnoussina. The timely information and encouragement offered by Dr. S.K.Mazumder is highly appreciated; my sincere regards to him and his family. The intensity of the work is recognized and is supported for presentation by Dr. A.K.Jha. The encouragement offered by Lahmeyer International (India) Pvt Ltd. is highly appreciated.
• http://r4d.dfid.gov.uk/Output/5145/
Acknowledgements
35
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© Lahmeyer International (India) Pvt. Ltd.
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