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1.Introduction Density or gravity currents are predominantly slender flows that are impelled through density differences, established either by salinity,

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Presentation on theme: "1.Introduction Density or gravity currents are predominantly slender flows that are impelled through density differences, established either by salinity,"— Presentation transcript:

1 1.Introduction Density or gravity currents are predominantly slender flows that are impelled through density differences, established either by salinity, temperature or particles in suspension within a fluid [1]. The latter, currents where fine sediments in suspension are accountable for the extra density are titled turbidity currents. Some of the reported outcomes of these stratified flows in large deep reservoirs comprise, among other consequences, inlet and bottom outlet structures blockage and storage capacity lessening [2], and, at broader scales, water quality and biodiversity degradation [3]. In virtue of multiple water bodies stressors (e.g. climate change, increasing population, among others), the loss of storage in reservoirs caused by turbidity currents is currently a topic of forceful scientific research ([4], [5], among others). In this context, the use of Computational Fluid Dynamics (CFD) tools as an appliance of water bodies monitoring programs is undoubtedly of foremost importance. The main objective of this study is to validate a CFD code (ANSYS-CFX) applied to the simulation of the interaction between turbidity currents and passive retention systems, designed to induce sediment deposition. To accomplish the proposed objective, laboratory tests were initially conducted using a straightforward obstacle configuration exposed to the passageway of a turbidity current. Afterwards, the experimental data was used to build a benchmark case to validate the 3D CFD software ANSYS-CFX. Mitigation of turbidity currents in reservoirs with passive retention systems: validation of CFD modeling 6. Conclusions In this work ASM fulfillment for modeling turbidity currents was assessed. Apart its demanding computational requirements and even though the numerical solution represents a fairly reasonable prediction of the observed flow, results reveal, at the present stage, its inadequacy to describe a number of aspects: i) the velocity maximum is under-predicted; ii) a sharp difference is observed at the near wall region and iii) a significant discrepancy between experimental and numerical suspended sediment concentration outcomes is verified downstream the obstacle. Issues i) and ii) may be due to a variety of factors, namely the grid density and the goodness of the choice of the turbulence model and its parameters, and issue iii) to the overprediction of sediment deposition upstream the obstacle. In the near future, the impact of these uncertainties will be investigated by means of a systematic sensitivity analysis. References [ 1] Simpson, J. E (1999). Gravity Currents: In the Environment and the Laboratory. Cambridge University Press. [2] Oehy, C. D., Schleiss, A. J. (2007). Control of turbidity currents in reservoirs by solid and permeable obstacles. Journal of Hydraulic Engineering, 133(6), 637-648. [3] Chung, S.W., Hipsey, M.R., Imberger, J. (2009). Modeling the propagation of turbid density inflows into a stratified lake: Daecheong Reservoir, Korea. Environmental Modelling and Software, 24(12), 1467-1482. [4] Alves, E., Ferreira, R. M. L., Cardoso, A.H. (2010). One-dimensional numerical modeling of turbidity currents: hydrodynamics and deposition. River Flow 2010 – International Conference on Fluvial Hydraulics, Braunschweig, Germany, 8-10 September 2010, 1097 - 1104. [5] Rossato, R., Alves, E. (2011). Experimental study of turbidity currents flow around obstacles. 7th International Symposium on Stratified Flows, Rome, Italy, 22 – 26 August 2011. [6] Ansys, CFX-Solver Theory Guide (2009). [7] W. Rodi (1993). "Turbulence models and their application in hydraulics - a state of the art review", International Association for Hydraulic Research, Delft, 3rd edition 1993, Balkema. [8] B. Launder, B. Sharma (1974). Application of the energy-dissipation model of turbulence to the calculation of flow near a spinning disc, Letters in Heat Mass Transfer, 1, 131– 138. [9] Gerber, G., Diedericks, G., Basson, G.R. (2011). Particle image velocimetry measurements and numerical modeling of a saline density current. Journal of Hydraulic Engineering,137(3), 333– 342. [10] Huang, H., Imran, J., Pirmez, C. (2005). Numerical modeling of turbidity currents with a deforming bottom boundary. Journal of Hydraulic Engineering, 131(4), 283-293. Acknowledgements This study was funded by the Portuguese Foundation for Science and Technology through the project PTDC/ECM/099485/2008. The first author thanks the assistance of Professor Moitinho from ICIST, to all members of the project PTDC/ECM/099485/2008 and to the Fluvial Hydraulics group of CEHIDRO. Edgar A. C. Ferreira 1, Elsa C. T. L. Alves 1 and Rui M. L. Ferreira 2 1 Hydraulics and Environment Department – LNEC, Portugal (email: edgaracf@civil.ist.utl.pt; ealves@lnec.pt ) 2 CEHIDRO – IST – TULisbon, Portugal (email: ruif@civil.ist.utl.pt) 2. Experimental Facilities and Instrumentation The experiments were performed at LNEC in a 16.45m long, 0.30m wide and 0.75m maximum height flume with its bottom devised to simulate hyperpycnal turbidity currents in reservoirs. During the experiments, longitudinal velocities were measured in five control sections with an Ultrasound Velocity Profiling (UVP) system and suspended sediment concentration profiles were collected at two control sections using syphon probes (Figure 1). The experimental conditions for the present study case are summarized in Table 1. 4. Initial and Boundary Conditions The numerical solution of the governing equations was achieved by employing the Finite Volume Method (Figure 2). At the inflow section, a uniform streamwise velocity distribution and a low level of turbulence intensity I = 0.01 (I=u rms /U with u rms being the root-mean square of turbulent velocity fluctuations and U the mean velocity) were imposed. At the outlet, in order to maintain a constant domain water level regardless of the upstream mass flow rate, a mixed boundary condition was attempted, i.e., associated to an orifice at atmospheric pressure a significant portion of the outlet was prescribed as a no-slip smooth wall. The free surface was modeled as a free slip rigid lid and in the bottom and lateral walls of the channel, including the obstacle, the no-slip condition with a scalable wall function formulation was introduced. Furthermore, the simulation was initialized with hydrostatic conditions. Figure 1 - Flow evolution of the turbidity current at inlet (top left) and outlet (top right) and the sampling system below Table 1 - Experimental conditions (h obst refers to the obstacle height, d 50 to the medium value of particles diameter, C s0 to the initial sediments concentration, U 0 to inlet velocity and H wat to the initial ambient fluid height). The downstream side of the barrier is located 8.25 meters from the domain final section. Figure 3 - ASM model results at time t = 17 s (left), 53 s (center) and 200 s (right) 5. Results The spatio-temporal turbidity current evolution is shown in Figure 3. In regards to the adequacy of the ASM approach, experimental and numerical results were likened (Figures 4 and 5). Figure 2 - Mesh detail of the CFD model in the obstacle´s vicinity Figure 5 - Variation of suspended sediment concentration with water depth. Experimental profiles were obtained during a brief sampling period whilst the numerical ones were acquired at t = 216 s (x = 5.75 m) and at t = 186 s (x=10.25m)


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