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Pascale Magaud

Publications and source records attributed to Pascale Magaud.

5 recordsLinked to original sources

Fluid flow in low aspect-ratio curved channels: from small to moderate Dean numbers

The pressure-driven flow is numerically investigated in curved channels at low aspect ratio, where centrifugal forces act along the largest dimension. The dynamics is studied numerically, as a function of the characteristic Dean number, $\mathrm{De}=\mathrm{Re}\sqrt{\delta}$, by varying independently the Reynolds number $\mathrm{Re}$ and the curvature ratio $\delta$, the ratio between the hydraulic diameter and the radius of curvature. A wide range of dimensionless numbers is considered; $\mathrm{De}\lesssim200$ and $0.005\leq\delta\leq0.15$. For $\mathrm{De}\lesssim 100$, the flow remains steady, whereas at larger Dean numbers, the flow is stable for several turns before transient structures developed. While investigating the flow features in the stable regime, only one pair of counter-rotating vortices is observed. At small $\mathrm{De}$ and large $\delta$, the peak of the streamwise velocity and the center of the vortices are located near the inner channel wall. They both shift toward the outer wall as $\mathrm{De}$ is increased and/or $\delta$ is decreased, a feature that is expected to affect the transport of particles in curved channels. A scaling law for the secondary flow is formulated from dimensional analysis, rather than relying on empirical correlations. The friction coefficient of the flow as well as the development angle are also rationalized in terms of both $\mathrm{Re}$ and $\delta$.

physics.flu-dyn

Inertial migration of bidisperse suspensions flowing in microchannels: effect of particle diameters ratio

Up to date, inertial migration of particles in microflows has demonstrated a great potential for a wide range of applications. In particular, this phenomenon is used to achieve particle separation or sorting in a suspension. Recent works reported that the focusing mode of particles can be modified in a polydisperse suspension. Nevertheless, the impact of the particle sizes in a mixture on their inertial migration has been rarely studied up to now. Thus, we have investigated in this work the influence of bidispersity on the lateral migration of the particles towards equilibrium positions and on their longitudinal ordering into trains. Different changes in the particles behavior were observed when the ratio between the particle sizes (dp1/dp2) varied from 1.64 to 4.58.

cond-mat.soft

Recent developments in miniaturized optical systems for continuous fluorescence detection in liquid flows

Miniaturization of continuous fluorescence detection is a challenging task due to the multiple and sensitive parameters intervening in the process. By analyzing fluorescence sensing architectures proposed during the last two years, this work has the goal to identify some trends in the process of fluorescence miniaturization for in-time liquid detection. A lack of postulated strategies regarding the miniaturization process was observed and this review tries to answer partially to this need. The identified integration strategies excel in fulfilling partially the desired functions of a fully autonomous miniaturized detector and further research is needed in order to develop sensing micro-system being capable to step outside of the lab world.

physics.app-ph

Inertial migration of neutrally buoyant particles in square channels at high Reynolds numbers

KEY WORDS suspensions, inertial focusing, particle-laden flows, high Reynolds numbers SHORT SUMMARY The inertial migration of particles in square channel flows at the micro-scale has been deeply investigated in the last two decades. The well-known four equilibrium positions are located near the center of each channel face at moderate Reynolds numbers [1]. More recently, Miura et al. [2] revealed experimentally the presence of eight equilibrium positions in millimetric square channels for Reynolds numbers higher than 250. The aim of the present work is to extend these results obtained at millimeter scale to the micrometer scale. To this end, in situ visualization of particles flowing in square micro-channels at Reynolds numbers ranging from 5 to 300 have been conducted and analyzed.

cond-mat.soft

Conditional stability of particle alignment in finite-Reynolds-number channel flow

Finite-size neutrally buoyant particles in a channel flow are known to accumulate at specific equilibrium positions or spots in the channel cross-section if the flow inertia is finite at the particle scale. Experiments in different conduit geometries have shown that while reaching equilibrium locations, particles tend also to align regularly in the streamwise direction. In this paper, the Force Coupling Method was used to numerically investigate the inertia-induced particle alignment, using square channel geometry. The method was first shown to be suitable to capture the quasi-steady lift force that leads to particle cross-streamline migration in channel flow. Then the particle alignment in the flow direction was investigated by calculating the particle relative trajectories as a function of flow inertia and of the ratio between the particle size and channel hydraulic diameter. The flow streamlines were examined around the freely rotating particles at equilibrium, revealing stable small-scale vortices between aligned particles. The streamwise inter-particle spacing between aligned particles at equilibrium was calculated and compared to available experimental data in square channel flow (Gao {\it et al.} Microfluidics and Nanofluidics {\bf 21}, 154 (2017)). The new result highlighted by our numerical simulations is that the inter-particle spacing is unconditionally stable only for a limited number of aligned particles in a single train, the threshold number being dependent on the confinement (particle-to-channel size ratio) and on the Reynolds number. For instance, when the particle Reynolds number is $\approx1$ and the particle-to-channel height size ratio is $\approx0.1$, the maximum number of stable aligned particles per train is equal to 3. This agrees with statistics realized on the experiments of (Gao {\it et al.} Microfluidics and Nanofluidics {\bf 21}, 154 (2017)).

physics.flu-dyn