Sediment Evacuation from Reservoirs through Intakes by Jet Induced Flow

Reservoir sedimentation is worldwide a significant long term problem and requires in view of the current mitigation measures an alternative and more sustainable solution. This challenge motivated the present study with the purpose to develop an alternative efficient method to release sediment out of a reservoir. The concept is based on the release of sediment through the headrace tunnel and turbines whereby a special focus was set on the fine sediment in the area in front of the power intakes. Specific jet arrangements should provide the energy and generate the optimum circulation needed to maintain the sediment in suspension and enhance its entrainment into the power intakes during turbining sequences. This new idea was experimentally tested in a rectangular laboratory tank with the following dimensions: 2 m wide, 1.5 m high and 4 m long. Two jet configurations were systematically investigated: a configuration of four jets arranged in a circle on a horizontal plane and a linear jet configuration located parallel to the front wall. The influence of the jet characteristics (nozzle diameter dj, jet velocity vj, jet discharge Qj, and jet angle θ) and the geometrical configuration parameters on the sediment release was investigated. As initial condition an almost homogeneous sediment concentration distribution was induced by air bubbles. This condition simulated a muddy layer like in front of the dam by the fading of a turbidity current. The water level during all the experiments was held constant by releasing the same discharge through the water intake as was introduced by the jets (experiments with jets) or through the back wall (experiments without jets), respectively. Turbidity measurements combined with flow velocity measurements gave information about the sediment release efficiency. The sediment release (evacuated sediment ratio, ESR) is defined as the evacuated sediment weight Pout divided by the sediment weight initially supplied Pin and represents the normalized temporal integral of the released sediment amount: ESR = Pout/Pin. Analogously, the settled sediment ratio is the settled sediment divided by the sediment weight initially supplied Pin. Experiments without jets as reference configuration showed an almost linear relation between the sediment release and the discharge within the tested range: the higher the discharge, the higher the evacuated sediment ratio. For a constant discharge the ultimate sediment release as well as the settled sediment ratio was easily estimated by a simple physical approach taking into account the settling velocity and the flow field generated by the discharge through the water intake and the back wall. For the tested discharge range the sediment release was between 0.09 and 0.37 for reference configuration. Jets are effectively mixing: after roughly half an hour the standard deviation of the suspended sediment concentration was approximately 5 %, what in chemistry is considered as homogeneous. Consequently, less sediment was settled and, hence, the sediment release was higher than without jets and reached for the highest tested discharge (ΣQj = 4050 1/h) ESR = 0.73. Moreover, contrary to the experiments without jets, with jets resuspension of settled sediment was observed. Resuspension started once steady state conditions for the circulation were reached. It has been detected for discharges higher than an experimentally determined threshold. The observed evolution of the resuspension rate suggests that for a final stage all of the initially supplied sediment can be evacuated. The circular jet arrangement was identified as the most efficient configuration regarding sediment release. Additionally, the normalized optimal geometrical parameter combination was determined as follows: off-bottom clearance of the jet arrangement C/B = 0.175, water intake height hi/B = 0.25, distance of the jet arrangement to the front wall daxis/B = 0.525, distance between two neighbouring jets lj/B = 0.15, jet angle θ = 0° and water height in the tank h/B = 0.6. Under optimum conditions and with the highest tested jet discharge (ΣQj = 4050 1/h) after four hours a sediment release of ESR = 0.73 was achieved. Without jets and with the same discharge through the water intake the sediment release reached ESR = 0.37. The corresponding flow pattern in the transversal plane was similar to an axial mixer, which in the literature is reported as favourable for suspension. In the longitudinal flow patterns resulting from higher discharges, a single rotor was found between jets and water intake, whereas for smaller discharges the flow pattern was similar to a radial mixer. A variation of a single geometrical parameter within the tested range (i.e. 60 to 200 % of the optimum value) caused a sediment release reduction of up to 40 %, depending on the parameter and the duration. The linear jet arrangement was found to be much less favourable in view of sediment release. Its results were in the same magnitude as for the experiments without jets (ESR between 0.37 and 0.45). This is due to the direction of the induced rotation which is unfavourable regarding sediment suspension: the sediment is drawn to the bottom where it is settled and difficult to be put in suspension again. The efficiency of the jets was established by comparing the sediment release obtained under different conditions: once when jets were employed, once without jets. The predicted efficiency based on time and discharge independent empirical relationships is around 1.7 for the optimum jet configuration. Using the measured data the efficiency depends on discharge and increases with time. At the end of the transient phase and when resuspension started the efficiency was approximately 1.5. With the highest tested discharge the efficiency reached after four hours almost 2 (ΣQj = 4050 1/h). Due to the fine grain size used in the experiments (mean diameter of 60 µm) the application focuses on large reservoirs where the sediment is well sized along the thalweg and only fine particles are expected in front of the dam as it is the case for sediments transported by turbidity currents. In the case study of Mauvoisin with a 520 m long dam crest creating a large reservoir in Switzerland, a first attempt was made to up-scale the research results. Based on the available discharge and head of the existing water transfer tunnel a preliminary optimal circular jet arrangement was suggested. However, the width of the reservoir was estimated at approximately three times as large as optimal experimental conditions. Nevertheless, with a circular jet arrangement could definitely more sediment be evacuated than without jets. Moreover, the region near the outlet devices could be maintained free of sediment and their clogging could be avoided. An economic study revealed that a jet arrangement is a low cost installation which, based on the performed experiments, is essential when aiming for high sediment release and fighting against reservoir sedimentation.

VENTING OF TURBIDITY CURRENTS: WHEN TO ACT?

Sabine Chamoun

During floods, sediments are transported from watersheds into reservoirs, slowly decreasing water volumes and this leading to economic losses. Thus, in the long term, sedimentation endangers reservoirs’ sustainability. Sediments can also block low-level hydraulic structures such as bottom outlets and powerhouse intakes and cause abrasion of gates and turbines. Additionally, the trapped sediments induce downstream starvation and thus the impoverishment of the river’s morphology and ecosystem. Many measures are taken to deal with the sedimentation of reservoirs. Among the most common methods is venting turbidity currents approaching the dam. In fact, these sediment-laden currents carry the major part of sediments found near the dam and thus their evacuation before they settle can be a very effective method to reduce sedimentation. However, dam operators lack information and guidelines to perform efficient venting operations. The present research experimentally and numerically investigates the venting of turbidity currents applied with different timings of outlet opening: (1) before the current reaches the outlet, (2) after the current has reached the outlet and climbed up to the top of the dam, and (3) after the upstream reflection of the muddy lake has begun. The high data acquisition frequency offers the possibility to examine temporal variations of inflow and outflow concentrations and discharges and thus variations of the efficiency of venting in time during the tests. In addition, the experimental results are extended numerically for a better understanding of the effect of opening timing on venting. Results show that opening the outlet before the current reaches the wall can be more efficient than opening after the current has reached the wall. Outputs of this study lead to crucial information for dam operators dealing with reservoirs facing high sedimentation rates due to the formation of turbidity currents.

2017

Influence of outlet discharge on the efficiency of turbidity current venting

Sabine Chamoun

Sediment yield into reservoirs was underestimated during the design of dams in the past. As a result, today, reservoir sedimentation is endangering the sustainability of dams. Moreover, the obstruction of rivers hinders their capacity to transport sediments and causes the alteration of their morphology and ecosystems. The rate of sedimentation is expected to increase in the future due to climate change. Turbidity currents are one of the main processes transporting sediments into long and deep reservoirs during floods. They are capable of transporting suspended sediments from the plunge point at the delta to the dam. Hence, venting of turbidity currents through bottom outlets is an appealing solution to reduce reservoir sedimentation. Using a flume of 8.55 m length and 0.27 m width, venting was investigated experimentally and numerically. Governing parameters such as the bottom outlet's discharge, the timing of venting relatively to the arrival of the turbidity current at the dam, the duration of venting, the reservoir's bed slope as well as the outlet's dimensions and level were studied. The efficiency of venting corresponding to the amount of sediments evacuated by the water used from the reservoir could be highlighted by systematic tests. The efficiency of venting increased with steeper bed slopes since the turbidity current was less reflected at the dam. Therefore, venting should be applied from the very beginning of dam impoundment to keep the cone upstream of the outlets free of sediments and the steepest bed slope possible close to the dam. The effect of the venting degree -defined as the ratio between outflow and turbidity current discharges- on the efficiency of venting was systematically studied. For turbidity currents reaching the outlet on a horizontal bed in the experimental configuration, a venting degree of about 100% resulted in the highest venting efficiency. For steeper reservoir bed slopes (i.e., 2.4% and 5.0%), the optimum efficiency can be obtained with a venting degree of about 135%. Venting was the most efficient when synchronized with the arrival of the turbidity current at the dam. Therefore, a gauging station should be placed around 300 m upstream of the low-level outlet to measure parameters such as velocity, indicating the arrival of the turbidity current. Furthermore, venting should last as long as there is inflow and should be maintained after the end of the flood for a duration that depends on the outflowing sediment concentration. In practice, venting can be stopped when the muddy lake has been evacuated and the vented water becomes clear again. This also allows cleaning the downstream river from fine sediment deposits after the venting operation. To optimize venting efficiency and minimize the dead storage, the outlet should be positioned at the lowest level possible. In addition, the height and width of the bottom outlet's entrance should be chosen in a way to create an aspiration cone that corresponds approximately to the dimensions of the body of the turbidity current. In order to keep the size of the low-level outlet reasonable, multiple outlets can be used to create the required aspiration cone.

EPFL2017

Influence of outlet discharge on the efficiency of turbidity current venting

Sabine Chamoun

EPFL2017

VENTING OF TURBIDITY CURRENTS: WHEN TO ACT?

Sabine Chamoun

2017