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Research paper

Assessment of interfacial turbulence treatment models for free surface flows

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Pages 651-667 | Received 12 Aug 2022, Accepted 05 Aug 2023, Published online: 15 Sep 2023

Figures & data

Figure 1 Aerated nappe profile for steady overflows

Figure 1 Aerated nappe profile for steady overflows

Figure 2 (a) Computational domain of the numerical wave model; (b) mesh detail

Figure 2 (a) Computational domain of the numerical wave model; (b) mesh detail

Figure 3 Sketch of the free overflow weirs. (a) experimental set-up, P1 is the pressure sensor to measure water pressure near the bottom; P2 is the pressure sensor to measure water pressure near the water surface; P3 is the pressure sensor to measure air pressure within the cavity; (b) calculation domain of the numerical model

Figure 3 Sketch of the free overflow weirs. (a) experimental set-up, P1 is the pressure sensor to measure water pressure near the bottom; P2 is the pressure sensor to measure water pressure near the water surface; P3 is the pressure sensor to measure air pressure within the cavity; (b) calculation domain of the numerical model

Figure 4 Time series of free surface elevation with respect to the bottom (z = 0 m) at downstream distances (a) x = 5 m; (b) x = 10 m; (c) x = 15 m; (d) x = 17 m

Figure 4 Time series of free surface elevation with respect to the bottom (z = 0 m) at downstream distances (a) x = 5 m; (b) x = 10 m; (c) x = 15 m; (d) x = 17 m

Table 1 Relative errors on wave surface elevation predictions using different turbulence models

Figure 5 Turbulent quantities at t = 25 s using different turbulence treatment methods (instantaneous results). (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixed air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulent viscosity

Figure 5 Turbulent quantities at t = 25 s using different turbulence treatment methods (instantaneous results). (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixed air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulent viscosity

Figure 6 Turbulent kinematic viscosity at t = 25 s using the SGDH model and the stabilized k-ε model with buoyancy

Figure 6 Turbulent kinematic viscosity at t = 25 s using the SGDH model and the stabilized k-ε model with buoyancy

Figure 7 Turbulence quantities of fully-aerated nappe flow at t = 30 s using different turbulence treatment methods. (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixing air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulence viscosity

Figure 7 Turbulence quantities of fully-aerated nappe flow at t = 30 s using different turbulence treatment methods. (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixing air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulence viscosity

Figure 8 Comparison of pressure on the downstream face of the caisson and nappe trajectory using experimental data, ballistic model, the standard k-ε model, the turbulence dissipation model and the SGDH model for a fully-aerated nappe (a) bottom water pressure; (b) top water pressure; (c) air pressure; (d) nappe trajectory (the numerical data are instantaneous when the nappe trajectory is steady)

Figure 8 Comparison of pressure on the downstream face of the caisson and nappe trajectory using experimental data, ballistic model, the standard k-ε model, the turbulence dissipation model and the SGDH model for a fully-aerated nappe (a) bottom water pressure; (b) top water pressure; (c) air pressure; (d) nappe trajectory (the numerical data are instantaneous when the nappe trajectory is steady)

Figure 9 Turbulence quantities of the non-aerated nappe at t = 10 s using different turbulence treatment methods. (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixing air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulence viscosity

Figure 9 Turbulence quantities of the non-aerated nappe at t = 10 s using different turbulence treatment methods. (a) Phase volume fraction, alpha.water = 1 is water phase, alpha.water = 0 is air phase, 0 < alpha.water < 1 is mixing air and water; (b) TKE; (c) turbulence dissipation rate; (d) turbulence viscosity

Figure 10 Comparison of pressure on the rear of the caisson surface and nappe trajectory using experimental data, ballistic model, the standard k-ε model, the turbulence dissipation model and the SGDH model for a non-aerated nappe (a) bottom water pressure sensor; (b) top water pressure sensor; (c) air pressure sensor; (d) nappe trajectory (the numerical data are instantaneous when the nappe trajectory is steady)

Figure 10 Comparison of pressure on the rear of the caisson surface and nappe trajectory using experimental data, ballistic model, the standard k-ε model, the turbulence dissipation model and the SGDH model for a non-aerated nappe (a) bottom water pressure sensor; (b) top water pressure sensor; (c) air pressure sensor; (d) nappe trajectory (the numerical data are instantaneous when the nappe trajectory is steady)