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Analysis of electrodynamic fluidization

Published online by Cambridge University Press:  06 September 2018

F. J. Higuera*
Affiliation:
ETSIAE, Universidad Politécnica de Madrid, Plaza Cardenal Cisneros 3, 28040 Madrid, Spain
*
†Email address for correspondence: f.higuera@upm.es

Abstract

Electrodynamic fluidization is a technique to generate suspensions of electrically conducting particles using electric forces to overcome their weight. An analysis of electrodynamic fluidization is presented for a monodisperse aerosol of non-coalescing particles of infinite electrical conductivity and negligible inertia suspended in a gas in the gap between two horizontal plate electrodes. A DC voltage is applied between the electrodes that charges the particles initially deposited on the lower electrode and leads to a vertical electric force that lifts the particles and pushes them upwards across the gap. The direction of this force reverses when the particles reach the upper electrode, pushing them downwards until they fall onto the lower electrode and repeat the cycle. Stationary distributions of particles are computed for given values of the applied voltage and the number of suspended particles per unit electrode area. Interparticle collisions play a role when the second of these parameters is of the order of the inverse of the particle cross-section or larger. The electric field induced by the charge of the particles opposes the field due to the applied voltage at the lower electrode and thus sets an upper bound to the number of particles that can be suspended for a given voltage. This bound is attained in the normal operation of a fluidization device, in which there is an excess of particles deposited at the lower electrode, and is computed as a function of the applied voltage. The predictions are compared to experimental results in the literature. A linear stability analysis for dilute aerosols with negligible collision effects shows that the stationary solution becomes unstable when the deposition threshold is approached with a number of suspended particles per unit electrode area larger than a certain critical value. A hydrodynamic instability appears near the lower electrode, where the electric force on a localized accumulation of charged particles leads to an upward gas flow that helps carrying the particles away from the electrode and increases the amplitude of the initial particle accumulation. The instability gives rise to electrohydrodynamic plumes whose dynamics involves collisions, mergers and generation of new plumes.

Information

Type
JFM Papers
Copyright
© 2018 Cambridge University Press 
Figure 0

Figure 1. Definition sketch.

Figure 1

Figure 2. (a) Dimensionless charges with which the particles detach from the lower ($q_{+}$, solid curves) and upper ($q_{-}$, dashed curves) electrodes as functions of the dimensionless voltage for values of the dimensionless number of particles per unit electrode area $N=0$, 1, 2, 4 and 6, increasing as indicated by the arrows. (b) Dimensionless electric current as a function of the dimensionless voltage for $N=1$, 2, 4 and 6.

Figure 2

Figure 3. (a) Maximum dimensionless number of suspended particles per unit electrode area as a function of the dimensionless voltage (solid curve, left-hand side scale), and dimensionless electric current in these conditions (dashed curve, right-hand side scale). The square and circle symbols are experimental results for the maximum number of suspended particles per unit electrode area from Yu & Colver (1987) and Shoshin & Dreizin (2002), respectively. (b) Distributions of positive particles (solid, right-hand side scale), negative particles (dashed) and electric field (dotted) for the maximum value of $N$. Results are shown for $V=2$, 3 and 4, increasing from bottom to top.

Figure 3

Figure 4. (a) Charges of the particles detaching from the lower ($q_{+}$, solid curves) and upper ($q_{-}$, dashed curves) electrodes, from the numerical solution of (3.1)–(3.5), as functions of the voltage for values of the number of particles per unit electrode area $N=0$, 2.07, 8.27, 16.54 and 24.80, increasing as indicated by the arrows. (b) Electric current scaled with $N$ as a function of the voltage for the same values of $N$. The inset shows the current scaled with $V^{3}$ as a function of $N$ for $V=4.55$, 6.82 and 9.09, increasing as indicated by the arrow.

Figure 4

Figure 5. Dimensionless electric current as a function of the dimensionless number of suspended particles per unit electrode area for a constant voltage. The circles show the current measured by Yu & Colver (1987), scaled with an effective electrode area, for copper particles of $96~\unicode[STIX]{x03BC}\text{m}$ enclosed between two horizontal electrode disks of 2.63 cm diameter spaced 1.1 cm and subjected to a voltage difference of 10 kV ($V=2.93$ in dimensionless variables). Deposition at the lower electrode occurs only when the current levels off. The dashed curve is the theoretical prediction for this case. The rightmost point of this curve marks the deposition threshold.

Figure 5

Figure 6. Growth rate (solid curves) and oscillation frequency (dashed curves, right-hand side scale) for the eigenvalue with largest real part as functions of the wavenumber for $N=2.067$, $R=12.92$, $\widetilde{a}=8.84\times 10^{-5}$ and four values of the dimensionless voltage, $V=2.05$, 2.11, 2.18 and 2.25, increasing as indicated by the arrows.

Figure 6

Figure 7. Stability limit in the ($N$, $V$) plane for $R=12.92$, $\widetilde{a}=8.84\times 10^{-5}$ (lower solid curve) and $R=29.07$, $\widetilde{a}=1.33\times 10^{-4}$ (upper solid curve). The dashed curve shows the deposition threshold $E(0)=1$ (the solid curve in figure 3a). In each case, the stationary state is linearly stable below the solid curve and particle deposition on the lower electrode occurs above the dashed curve.

Figure 7

Figure 8. Four snapshots of the number density of positive particles, from the numerical solution of (2.15), (2.16), (4.7) and (4.8) for $N=2.067$, $V=2.14$, $R=12.92$ and $\widetilde{a}=8.84\times 10^{-5}$ at times $t=1.225$ (a), 1.825 (b), 2.525 (c), and 4.225 (d).

Figure 8

Figure 9. Sketch of the excess and defect of charge induced by an external electric field on colliding particles.

Figure 9

Figure 10. Sketch of particle collisions in the absence of inertia.

Figure 10

Figure 11. (a) Dimensionless charges with which the particles detach from the lower ($q_{+}^{\ast }$, solid curves) and upper ($q_{-}^{\ast }$, dashed curves) electrodes, given by (B 2) as functions of the dimensionless voltage for $N=1$ and $\unicode[STIX]{x1D708}=1.5$, 2, 3, 4 and 10, increasing from bottom to top. (b) Dimensionless electric current as a function of the dimensionless voltage for $N=1$ and $\unicode[STIX]{x1D708}=1.5$, 2, 3, 4 and 10, increasing from bottom to top. (c) Dimensionless number of particles per unit electrode area at the threshold of particle deposition on the lower electrode, determined by the condition $q_{+}^{\ast }E(0)=1$, as a function of the dimensionless voltage for $\unicode[STIX]{x1D708}=1.5$, 1.6, 1.7, 2, 2.5 and 10, increasing from bottom to top. (d) Dimensionless electric current as a function of the dimensionless voltage in the conditions of (c).