Hostname: page-component-74656f9884-2dmjx Total loading time: 0 Render date: 2026-11-10T14:34:19.928Z Has data issue: false hasContentIssue false

Weakly nonlinear stability analysis of subcritical electrohydrodynamic flow subject to strong unipolar injection

Published online by Cambridge University Press:  03 March 2016

Mengqi Zhang*
Affiliation:
Département Fluides, Thermique, Combustion, Institut PPrime, CNRS-Université de Poitiers-ENSMA, UPR 3346, 43 Route de l’Aérodrome, Poitiers CEDEX F86036, France
*
†Email address for correspondence: mengqi.zhang@univ-poitiers.fr

Abstract

We analyse in detail the weakly nonlinear stability of electrohydrodynamic (EHD) flow of insulating fluids subject to strong unipolar injection, with and without cross-flow. We first consider the hydrostatic electroconvetion induced by a Coulomb force confined between two infinite flat electrodes, taking into account the charge diffusion effect. The effects of various non-dimensionalized parameters are examined in order to depict in detail and to understand better the subcritical bifurcation of hydrostatic electroconvetion. In addition, electrohydrodynamics with low- or high- $Re$ cross-flow is also considered for investigating the combined effect of inertia and the electric field. It is found that the base cross-flow is modified by the electric effect and that, even when the inertia is dominating, the electric field can still strengthen effectively the subcritical characteristics of canonical channel flow. In this process, however, the electric field does not contribute directly to the subcriticality of the resultant flow and the intensified subcritical feature of such flow is thus entirely due to the modified hydrodynamic field as a result of the imposed electric field. This finding might be important for flow control strategies involving an electric field. Theoretically, the above results are obtained from a multiple-scale expansion method, which gives rise to the Ginzburg–Landau equation governing the amplitude of the first-order perturbation. The conclusions are deduced by probing the changes of value of the coefficients in this equation. In particular, the sign of the first Landau coefficient indicates the type of bifurcation, being subcritical or supercritical. Moreover, as a quintic-order Ginzburg–Landau equation is derived, the effects of higher-order nonlinear terms in EHD flow are also discussed.

Information

Type
Papers
Copyright
© 2016 Cambridge University Press 
Figure 0

Figure 1. Illustration of flow configuration for 2-D EHD flow. Black dots represent fluid particles. Circles with a positive sign are unipolarly charged ions subject to an electric field $E$ as a result of an imposed potential difference. Dashed grey curves with arrows denote the convection formed in hydrostatic EHD flow due to the electric Coulomb force.

Figure 1

Figure 2. Base states for $\bar{{\it\phi}},\bar{E},\bar{Q},\bar{Q}C$ at $C=12.5,Fe=10^{5}$ (blue solid line with dots), $C=100,Fe=10^{5}$ (red dash-dotted line) and $C=12.5,Fe=10^{3}$ (black dashed line). Inset in each figure zooms in part of the figure.

Figure 2

Figure 3. Supercritical bifurcation (a) and subcritical bifurcation (b). The solid lines are the stable solutions and the dashed lines unstable solutions. The arrows indicate that the unstable solution will eventually become stable. The grey dotted circle is the neighbourhood of the critical condition. (a) $\text{Re}(a_{3})<0$, (b) $\text{Re}(a_{3})>0$.

Figure 3

Table 1. Comparison of present calculation of the Landau coefficients for Poiseuille channel flow with Davey, Hocking & Stewartson (1974) and Fujimura (1989). $N=201$. The notions for the Landau coefficients are different in their works, but can be easily identified. In Davey et al. (1974), there is no data for $a_{5}$ and there is a difference of sign convention in $c_{g}$. In Fujimura (1989), there is no data for $c_{g}$ and $a_{2}$. We deliberately show more significant figures than Fujimura (1989) to facilitate the comparison.

Figure 4

Table 2. Convergence check for hydrostatic EHD flow at $C=50,M=100,Fe=10^{3},T=140.41884,{\it\alpha}=2.58674$.

Figure 5

Figure 4. Dispersion relation for hydrostatic EHD flow at $C=50,M=100,Fe=10^{3},T=140.41884,{\it\alpha}=2.58674,N=201$. (a) ${\it\mu}_{r}$ and ${\it\mu}_{rf}$, see (4.3), (b) ${\it\mu}_{i}$, as a function of ${\it\alpha}$.

Figure 6

Figure 5. Shape of the direct and the adjoint eigenvectors at the critical condition: (a) $\tilde{{\it\psi}_{1}}$ (real), (b) $\tilde{{\it\varphi}_{1}}$ (imaginary), (c) $\tilde{{\it\psi}_{1}}^{\dagger }$ (imaginary) and (d) $\tilde{{\it\varphi}_{1}}^{\dagger }$ (real) at $C=50,M=100,Fe=10^{3},T=140.41884,{\it\alpha}=2.58674$.

Figure 7

Figure 6. The effect of $M$ at $C=50,Fe=10^{3},T=140.41884$,${\it\alpha}=2.58674$. (a) The growth rate ${\it\omega}_{i}$, (b) $a_{3}$ and (c) $a_{5}$.

Figure 8

Figure 7. The effect of $Fe$ at $C=12.5,M=100$ at the critical condition. (a) The critical $T_{c}$, (b) $a_{3}$ and (c) $a_{5}$.

Figure 9

Figure 8. The effect of $C$ at $Fe=10^{3},M=100$ at the critical condition. (a) The critical $T_{c}$, (b) $a_{3}$ and (c) $a_{5}$.

Figure 10

Figure 9. Modification of base electric field in hydrostatic EHD. $Fe=10^{3},M=100$. Blue solid lines: $C=50,T=140.41884,{\it\alpha}=2.58674$. Red dashed lines: $C=10,T=144.48175,{\it\alpha}=2.57780$. Black lines with dots: $C=3,T=152.62120,{\it\alpha}=2.5575$. (a) Modification of base potential $\tilde{{\it\varphi}}_{20}^{\prime }$, (b) modification of base charge distribution $\tilde{{\it\varphi}}_{20}^{\prime \prime }/(-C)$.

Figure 11

Figure 10. Modification of base flow $\tilde{{\it\psi}}_{20}^{\prime }$ (real part) for EHD with low-$Re$ cross-flow. (a) $C=10,M=100,Fe=10^{3}$. Blue line with circles: $T=143.5852,{\it\alpha}=2.5628,Re=T/(2M^{2})=0.0071$. Red solid line: $T=142.0188,{\it\alpha}=2.5015,Re=T/M^{2}=0.0142$; (b) $M=100,Fe=10^{3}$. Blue solid line: $C=50,T=138.4069,{\it\alpha}=2.5108,Re=T/M^{2}=0.0138$. Red dashed line: $C=10,T=142.0188,{\it\alpha}=2.5015,Re=T/M^{2}=0.0142$. Black line with circles: $C=3,T=150.3564,{\it\alpha}=2.4765,Re=T/M^{2}=0.0150$.

Figure 12

Figure 11. The effect of $T$ at the critical condition with $C=50,Fe=10^{3},M=\sqrt{T/Re}$. (a) $Re_{c}$ as a function of $T$, (b) the real part of $a_{3}$ as a function of $T$ and (c) the real part of $a_{5}$ as a function of $T$.

Figure 13

Figure 12. Base flow modification at the critical condition. (a) Real part of $\tilde{{\it\psi}}_{20}^{\prime }$. Blue solid line: canonical Poiseuille flow at $Re=5772.2218,{\it\alpha}=1.0205474$; red dashed line: EHD-Poiseuille flow at $T=100,Re=5557.2000,{\it\alpha}=1.0244,C=50,Fe=10^{3},M=\sqrt{T/Re}=0.13414$; black lines with pluses: $T=500,Re=4606.5458,{\it\alpha}=1.0443,C=50,Fe=10^{3},M=\sqrt{T/Re}=0.32946$. (b) The difference between base flow modifications of EHD-Poiseuille flow (real part of $\tilde{{\it\psi}}_{20,EHD\text{-}P}^{\prime }$) and canonical Poiseuille flow (real part of $\tilde{{\it\psi}}_{20,Poiseuille}^{\prime }$). Red dashed line: $T=100$, black line with pluses: $T=500$ with the other parameters the same as in (a).