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Inviscid versus viscous instability mechanism of an air–water mixing layer

Published online by Cambridge University Press:  06 March 2015

Jean-Philippe Matas*
Affiliation:
Université Grenoble Alpes, LEGI, CNRS, F-38000 Grenoble, France
*
†Email address for correspondence: matas@legi.grenoble-inp.fr
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Abstract

We study how confinement affects the viscous spatiotemporal instability of a two-phase mixing layer. We show that the absolute instability triggered by the inclusion of finite liquid and gas thicknesses leads to a good prediction of experimental data. In addition, this new mechanism provides a justification for the relevance of both simplified inviscid scaling laws and more sophisticated viscous approaches.

Information

Type
Papers
Copyright
© 2015 Cambridge University Press 
Figure 0

Figure 1. Sketch showing the typical base flow profile, including finite liquid and gas stream thicknesses.

Figure 1

Figure 2. Pinching at positive ${\it\omega}_{0i}$ occurs between confinement and shear controlled branches when confinement is taken into account; $U_{G}=27~\text{m}~\text{s}^{-1}$, $U_{L}=0.26~\text{m}~\text{s}^{-1}$, ${\it\delta}_{d}=1$, $H_{G}=1~\text{cm}$ and $H_{L}=1~\text{cm}$. Symbols correspond to ${\it\omega}_{r}$ in the range $(80{-}680)~\text{s}^{-1}$.

Figure 2

Figure 3. Comparison at $U_{G}=27~\text{m}~\text{s}^{-1}$ between experimental data of Matas et al. (2011) (▪) and available spatiotemporal predictions: *, prediction by Otto et al. (2013), for ${\it\delta}_{d}=0.1$; ○, prediction taking into account confinement without any velocity deficit (${\it\delta}_{d}=1$); ▫, prediction with confinement and a velocity deficit (${\it\delta}_{d}=0.5$).

Figure 3

Figure 4. Comparison at $U_{G}=22~\text{m}~\text{s}^{-1}$ between experimental data of Matas et al. (2011) (▪) and available spatiotemporal predictions: *, prediction by Otto et al. (2013), for ${\it\delta}_{d}=0.1$; ○, prediction taking into account confinement without any velocity deficit (${\it\delta}_{d}=1$).

Figure 4

Figure 5. Variation of the absolute growth rate ${\it\omega}_{0i}$ at the pinch point caused by the confinement branch, as a function of liquid velocity, for fixed $U_{G}=27~\text{m}~\text{s}^{-1}$, $H_{G}=1~\text{cm}$ and $H_{L}=1~\text{cm}$: ●, ${\it\delta}_{d}=1$; ▫, ${\it\delta}_{d}=0.5$. The growth rate decreases when liquid velocity is increased, and increases when a velocity deficit is included.

Figure 5

Table 1. Energy budget for the data (○) and (*) of figure 3. Values are as a percentage of the total (positive) kinetic energy rate.

Figure 6

Figure 6. Impact of a variation in viscosity on spatial branches for $U_{G}=27~\text{m}~\text{s}^{-1}$, $U_{L}=0.26~\text{m}~\text{s}^{-1}$ and ${\it\delta}_{d}=1$: *, ${\it\nu}_{G}=1.5\times 10^{-5}~\text{m}~\text{s}^{-1}$, ${\it\nu}_{L}=10^{-6}~\text{m}~\text{s}^{-1}$ and ${\it\omega}_{i}=85~\text{s}^{-1}$; ▫, ${\it\nu}_{G}=1.5\times 10^{-6}~\text{m}~\text{s}^{-1}$, ${\it\nu}_{L}=10^{-7}~\text{m}~\text{s}^{-1}$ and ${\it\omega}_{i}=65~\text{s}^{-1}$; ●, ${\it\nu}_{G}=1.5\times 10^{-7}~\text{m}~\text{s}^{-1}$, ${\it\nu}_{L}=10^{-8}~\text{m}~\text{s}^{-1}$ and ${\it\omega}_{i}=50~\text{s}^{-1}$; $+$, ${\it\nu}_{G}=1.5\times 10^{-7}~\text{m}~\text{s}^{-1}$, ${\it\nu}_{L}=10^{-6}~\text{m}~\text{s}^{-1}$ and ${\it\omega}_{i}=45~\text{s}^{-1}$. The shear branch is displaced when viscosity is reduced, but the location of the pinch point associated with confinement remains unchanged.

Figure 7

Figure 7. Change in the confinement branches when $H_{G}$ and $H_{L}$ are reduced, for fixed $U_{G}=27~\text{m}~\text{s}^{-1}$, $U_{L}=0.26~\text{m}~\text{s}^{-1}$, ${\it\delta}_{d}=1$, ${\it\omega}_{i}=120~\text{s}^{-1}$ and ${\it\omega}_{r}$ in the range $(60{-}430)~\text{s}^{-1}$: ●, $H_{G}=H_{L}=2~\text{cm}$; $\times$, $H_{G}=H_{L}=1~\text{cm}$; ○, $H_{G}=H_{L}=0.5~\text{cm}$.

Figure 8

Figure 8. Pinching for $U_{G}=27~\text{m}~\text{s}^{-1}$, $U_{L}=0.26~\text{m}~\text{s}^{-1}$, ${\it\delta}_{d}=1$, ${\it\omega}_{i}=60~\text{s}^{-1}$ and ${\it\omega}_{r}$ in the range $(60{-}280)~\text{s}^{-1}$: ○, $H_{G}=3~\text{cm}$ and $H_{L}=1~\text{cm}$; *, $H_{G}=1~\text{cm}$ and $H_{L}=3~\text{cm}$. Both thicknesses play a symmetric role.

Figure 9

Figure 9. Influence of liquid velocity $U_{L}$, for fixed $U_{G}=27~\text{m}~\text{s}^{-1}$, $H_{G}=H_{L}=1~\text{cm}$, ${\it\delta}_{d}=1$ and ${\it\omega}_{i}=120~\text{s}^{-1}$: ●, $U_{L}=0.26~\text{m}~\text{s}^{-1}$; ○, $U_{L}=0.5~\text{m}~\text{s}^{-1}$; *, $U_{L}=1~\text{m}~\text{s}^{-1}$. The ranges of ${\it\omega}_{r}$ are respectively (120–370), (170–500) and $(260{-}820)~\text{s}^{-1}$. When liquid velocity is increased, the shear branch is shifted away from the confinement branch.

Figure 10

Figure 10. Influence of vorticity thickness ${\it\delta}_{G}$ on ${\it\omega}_{r}$ (circles) and ${\it\omega}_{0i}$ (squares), for fixed $U_{G}=27~\text{m}~\text{s}^{-1}$, $U_{G}=0.26~\text{m}~\text{s}^{-1}$, ${\it\delta}_{d}=1$ and $H_{G}=H_{L}=1~\text{cm}$. Open symbols correspond to ${\it\delta}_{L}=500~{\rm\mu}\text{m}$ and filled symbols to ${\it\delta}_{L}={\it\delta}_{G}$.