Hostname: page-component-7b7567c8c-jswmv Total loading time: 0 Render date: 2026-11-15T21:34:26.516Z Has data issue: false hasContentIssue false

Erosion of a sharp density interface by a turbulent jet at moderate Froude and Reynolds numbers

Published online by Cambridge University Press:  25 January 2018

J. Herault*
Affiliation:
Institut de Radioprotection et de Sûreté Nucléaire (IRSN), 13115 Saint-Paul-lez-Durance, FranceAix–Marseille University, CNRS, Centrale Marseille, IRPHE, UMR 7342, 49 rue F. Joliot-Curie, 13013 Marseille, France
G. Facchini
Affiliation:
Aix–Marseille University, CNRS, Centrale Marseille, IRPHE, UMR 7342, 49 rue F. Joliot-Curie, 13013 Marseille, France
M. Le Bars
Affiliation:
Aix–Marseille University, CNRS, Centrale Marseille, IRPHE, UMR 7342, 49 rue F. Joliot-Curie, 13013 Marseille, France
*
†Email address for correspondence: johann.herault@imt-atlantique.fr

Abstract

Using water–salt water laboratory experiments, we investigate the mechanism of erosion by a turbulent jet impinging onto a density interface, for moderate Reynolds and Froude numbers. The Froude number is defined by $Fr_{i}=u_{i}/\sqrt{b_{i}g^{\prime }}$ , with $u_{i}$ and $b_{i}$ , the typical velocity and width of the jet at the interface, and $g^{\prime }$ the reduced gravitational acceleration. The Froude number $Fr_{i}$ characterizes the competition between inertial forces against the restoring buoyancy force. Contrary to previous observations reporting baroclinic destabilization of the interface, we show that the entrainment, in the range of parameters explored here, is driven by interfacial gravity waves. The waves are generated by the barotropic excitation coming from the turbulent fluctuations of the jet; they are then amplified by a mechanism of wave-induced stress; and they finally break and induce entrainment and mixing. Based on those physical observations, we introduce a scaling model for the entrainment rate, which varies continuously from $Fr_{i}^{3}$ to an $Fr_{i}$ power law from small to large Froude numbers, in agreement with the present and some of the previous laboratory data.

Information

Type
JFM Papers
Copyright
© 2018 Cambridge University Press 
Figure 0

Figure 1.(a) A schematic of the experimental set-up showing a rectangular tank filled with water ($h_{1}$) and a saline solution ($h_{2}$). The nozzle is located at a height $h$ from the interface. (b) We define the reference frame $(x,z)$ associated with the nozzle. The $z$ direction is descending.

Figure 1

Table 1.Experimental parameters for the four experiments conducted.

Figure 2

Figure 2.(a) Radius $b$ of the jet and (b) inverse of the axial velocity $u_{m}$ as a function of the distance from the nozzle $z$. Lengths and velocities are rescaled by the diameter of the nozzle $2b_{0}$ and by the injection velocity $U_{inj}$, respectively.

Figure 3

Table 2.Table of parameters of the turbulent jet compared to the measurements of Hussein, Capp & George (1994).

Figure 4

Figure 3.Streamlines (black curves) of the mean flow, superimposed on the vertical component of the mean velocity field $\langle u_{z}\rangle$ ($\text{cm}~\text{s}^{-1}$) (colour bar). The white curve corresponds to the time-averaged location of the interface separating the two fluids. The black dotted line corresponds to the ordinate $h_{0}-z=0$.

Figure 5

Figure 4.(a) Location of the points (circles) on the interface with the normal lines (dashed lines) showing where the tangential velocity $U_{t}$ is calculated. (b) The profiles of $U_{t}$ are calculated at the abscissa $x=0.1,0.35,0.475,0.575,0.7,0.775,0.825$ times the radius of the dome $b_{d}$, as shown on (a). The variable $z_{1}$ is the distance from the interface following the dashed lines in (a).

Figure 6

Figure 5.Mixing process in the vicinity (a) of the interface ($15~\text{cm}\times 20~\text{cm}$) and (b) of the dome head ($15~\text{cm}\times 8~\text{cm}$). The dense fluid has been dyed by rhodamine and corresponds to the bright region. See online supplementary material (movie 1 available at https://doi.org/10.1017/jfm.2017.891) for the movie corresponding to the panel (a).

Figure 7

Figure 6.Rescaled density field $\hat{\unicode[STIX]{x1D70C}}$ (colour level) from $\hat{\unicode[STIX]{x1D70C}}=0$ for $\unicode[STIX]{x1D70C}=\unicode[STIX]{x1D70C}_{1}$ (fresh water) to $\hat{\unicode[STIX]{x1D70C}}=1$ for $\unicode[STIX]{x1D70C}=\unicode[STIX]{x1D70C}_{2}$ (initial salt water). The full black curve corresponds to the height $h(x,t)$ where $\hat{\unicode[STIX]{x1D70C}}=0.5$. The dashed curve represents the time-averaged height $\langle h\rangle$.

Figure 8

Figure 7.Two-dimensional power spectrum $E(k,F)$ of the elevation $\unicode[STIX]{x1D702}(x,t)$. The wavenumber $k$ is rescaled by $k_{0}=2\unicode[STIX]{x03C0}/b_{d}$ and the energy density is rescaled by the total energy $E_{t}$.

Figure 9

Figure 8.(a) Spatiotemporal diagram of the height perturbation $\unicode[STIX]{x1D702}(x,t)=h(x,t)-\langle h\rangle$, filtered in the frequency range $f\in [0.3{-}0.4]$  Hz. The abscissae are rescaled by the radius of the dome $b_{d}$, the time by the mean wave period $T=2.9$  s, and the amplitude of the height by the depth of the dome $\unicode[STIX]{x1D709}$. (b) Zoom of the region $x\in [0{-}2.25]b_{d}$ and $t\in [11.5{-}14.5]T$.

Figure 10

Figure 9.(a) Three trajectories of the wave envelope (full lines), compared to a virtual trajectory (dashed line) with constant phase velocity $c_{p}=2~\text{cm}~\text{s}^{-1}$. Inset: distribution of the phase velocity $c$. (b) Amplitude of the height $A_{\unicode[STIX]{x1D702}}$ given by (4.1). From top to bottom, the three curves show the total amplitude of the waves, the fundamental component and the higher harmonics.

Figure 11

Figure 10.Richardson number as a function of $x/b_{d}$ with $Ri=(g^{\prime }/b_{d})/s_{0}^{2}$ and $s_{0}=(\unicode[STIX]{x2202}_{z_{1}}U_{t})_{z_{1}=0}$.

Figure 12

Figure 11.(a) Spatiotemporal diagram of the fluctuations $u_{z}^{\prime }$ in the range of frequencies $[0.3,0.4]$  Hz along the vertical axis $x=0.37b_{d}$. (b) Bandpass-filtered fluctuations of the vorticity field, calculated from a coarse-grained velocity field with width of $0.75$  cm (Gaussian filter). The dashed curve represents the vertical axis at $x=0.37b_{d}$.

Figure 13

Figure 12.(a) Tangential velocity $U_{t}$ divided by the phase velocity $c_{p}=2~\text{cm}~\text{s}^{-1}$. The black dashed curve represents the contour where $U_{t}=2~\text{cm}~\text{s}^{-1}$. The white curve corresponds to the interface. (b) Profile of the tangential velocity $U_{t}$ corresponding to the abscissa $x=0.7b_{d}$ extracted from figure 4(b). Its first $U_{t}^{\prime }$ and second $U_{t}^{\prime \prime }$ depth derivatives are represented, respectively, by dashed and dashed-dotted lines. The circles correspond to the points where the velocity is equal to $c_{p}$.

Figure 14

Figure 13.Production term $P(x,z)=\unicode[STIX]{x1D70F}S_{0}$ with $\unicode[STIX]{x1D70F}=-\langle u_{x}^{\prime }u_{z}^{\prime }\rangle$ the Reynolds stress and $S_{0}$ the large-scale shear. The black curve corresponds to the streamline passing close to the stagnation point.

Figure 15

Figure 14.Maxima (full line) and minima (dashed line) of the dimensionless energy transfer rate $\unicode[STIX]{x1D70E}=P/(2E)$ rescaled by the wave period $T$, where $P$ is the production term and $E$ the kinetic energy, for all heights $z$ in the dome as a function of $x/b_{d}$. The grey lines correspond to the abscissa $x=\pm 0.58b_{d}$ where the waves may propagate more slowly than the mean flow.

Figure 16

Figure 15.(a) Schematic and notation for the model of entrainment. (b) Entrainment rate as a function of the Froude number given by (5.7). The grey curves show the $Fr_{i}^{3}$ power law valid at low Froude number and the linear scaling $Fr_{i}$ valid at large Froude numbers.

Figure 17

Figure 16.Modified figure from Shrinivas & Hunt (2014, their figure 12a). The dotted line corresponds to the scaling law defined by (5.9). The black lines correspond to the scaling law $E_{i}=0.24Fr_{i}^{2}$ for small Froude numbers and $E_{i}=0.42Fr_{i}$ for large Froude number, as suggested by Shrinivas & Hunt (2014).

Figure 18

Figure 17.The black squares are 30 values from Kumagai (1984, figure 12). The dashed curve corresponds to the empirical model of Kumagai (1984). The full line is the scaling law established by Shrinivas & Hunt (2014) with $E_{i}=0.24Fr_{i}^{2}$. The dotted curve corresponds to (5.9) with $(\unicode[STIX]{x1D6FC},\unicode[STIX]{x1D6FD})=(0.015,14)$, associated with a cross-over point at $Fr_{t}=0.27$.

Herault et al. supplementary movie

Mixing process in the vicinity of the interface (15 × 20cm2) The dense fluid has been dyed by rhodamine and corresponds to the bright region.

Download Herault et al. supplementary movie(Video)
Video 9.3 MB