December 2024
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198 Reads
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December 2024
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198 Reads
November 2024
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2 Reads
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1 Citation
Journal of Fluid Mechanics
The featured article ‘Break-up of a falling drop containing dispersed particles’ (Nitsche and Batchelor, J. Fluid Mech. , 1997, vol. 340, pp. 161–175) is G. K. Batchelor's last published paper with his former postdoctoral associate J. M. Nitsche. The objective of the study was to investigate the randomness of the velocities of interacting rigid particles falling under gravity through a viscous fluid at a small Reynolds number and its consequence for the breakup of a falling cloud of particles. The study focused on a quintessential problem of the collective dynamics of interacting particles and has been an inspiration for subsequent work.
October 2024
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30 Reads
Journal of Fluid Mechanics
The spreading of large viscous drops of density-matched suspensions of non-Brownian spheres on a smooth solid surface is investigated experimentally at the global drop scale. The focus is on dense suspensions with a solid volume fraction equal to or greater than , and for drops larger than the capillary length, i.e. for which the spreading is governed by the balance of gravitational and viscous forces. Our findings indicate that all liquids exhibit a power-law behaviour typical of gravity-driven dynamics, albeit with an effective suspension viscosity that is smaller than the bulk value. When the height of the drop is of the order of the particle size, the power law breaks down as the particles freeze while the contact line continues to advance.
October 2024
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72 Reads
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3 Citations
Journal of Rheology
Concentration inhomogeneities occur in many flows of non-Brownian suspensions. Their modeling necessitates the description of the relative motion of the particle phase and of the fluid phase, as well as the accounting for their interaction, which is the object of the suspension balance model (SBM). We systematically investigate the dynamics and the steady state of shear-induced migration in a wide-gap Couette flow for a wide range of particle volume fraction, and we test the ability of the SBM to account for the observations. We use a model suspension for which macroscopic particle stresses are known. Surprisingly, the observed magnitude of migration is much lower than that predicted by the SBM when the particle stress in the SBM is equated to the macroscopic particle stress. Another noteworthy observation is the quasi-absence of migration for semidilute suspensions. From the steady-state volume fraction profiles, we derive the local particle normal stress responsible for shear-induced migration according to the SBM. However, the observed dynamics of migration is much faster than that predicted by the SBM when using this stress in the model. More generally, we show that it is not possible to build a local friction law consistent with both the magnitude and the dynamics of migration within the standard SBM framework. This suggests that there is a missing term in the usual macroscopic constitutive law for the particle normal stress driving migration. The SBM is indeed capable of accurately predicting both the magnitude and the dynamics of migration when a tentative phenomenological term involving a concentration gradient is added to the particle normal stresses determined in macroscopic experiments.
September 2024
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130 Reads
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2 Citations
Physical Review Fluids
Dense granular suspensions, which consist of concentrated mixtures of non-Brownian particles suspended in a liquid, are ubiquitous in many natural phenomena (e.g., landslides, debris flows, and sediment transport) and industrial processes (e.g., concrete and pastes). Despite their prevalence, the rheology of these suspensions is not fully understood, and the establishment of a unified theoretical framework for different flow regimes remains a challenge. The present work reviews rheological measurements of granular suspensions in the dense regime, performed at imposed volume fractions and at imposed values of particle normal stress. It proposes a unified granular rheology over the viscous to inertial flow regime based on the superposition of inertial and viscous stress scales. This granular rheology, found for suspensions of hard spheres, can be extended to a soft granular rheology for soft particles. This soft granular rheology results in the approximate collapse of the rheological data into two branches when scaled with the distance to jamming, in a manner analogous to that found for viscous soft colloids, but now extended into the inertial regime.
August 2024
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240 Reads
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2 Citations
Physical Review Letters
The rheology of suspensions of non-Brownian soft spheres is studied across jamming but also across the viscous and inertial regimes using a custom pressure- and volume-imposed rheometer. The study shows that the granular rheology found for suspensions of hard spheres can be extended to a soft granular rheology (SGranR) by renormalizing the critical volume fraction and friction coefficient to pressure-dependent values and using the addition of the viscous and inertial stress scales. This SGranR encompasses rheological behaviors on both sides of the jamming transition, resulting in an approximate collapse of the rheological data into two branches when scaled with the distance to jamming, as observed for soft colloids. This research suggests that suspensions of soft particles across flow regimes can be described by a unified SGranR framework around the jamming transition.
July 2024
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17 Reads
Soft Matter
We present a simple route to obtain large quantities of suspensions of non-Brownian particles with stimuli-responsive surface properties to study the relation between their flow and interparticle interactions. We perform...
June 2024
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12 Reads
Suspensions of particles play an important role in a wide variety of natural phenomena and industrial processes. Familiar examples of suspensions of particles include sediments in rivers or estuaries, raindrops, pastes, biological suspensions (such as blood), paints, ink, and waste waters carrying suspended solids. Suspensions are also present in many technological and industrial processes such as water treatment and filtration, separation in mineral processing, synthesis of composite materials, paper making, to name but a few.
March 2024
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391 Reads
Concentration inhomogeneities occur in many flows of non-Brownian suspensions. Their modeling requires describing the relative motion of the particle phase and of the fluid phase and accounting for their interaction, which is the object of the Suspension Balance Model (SBM). We systematically investigate the dynamics and the steady-state of shear-induced migration in a wide-gap Couette flow for a wide range of particle volume fraction, and we test the ability of the SBM to account for the observations. We use a model suspension for which macroscopic particle stresses are known. Surprisingly, the observed magnitude of migration is much lower than that predicted by the SBM when the particle stress in the model is matched with the macroscopic particle stress. Another remarkable observation is the quasi-absence of migration for semi-dilute suspensions. From the steady-state volume fraction profiles, we derive the local particle normal stress at the origin of shear-induced migration according to the SBM. However, the observed dynamics of migration is much faster than that predicted by the SBM when using this stress in the model. This suggests that there is a missing term in the usual macroscopic constitutive law for the particle normal stress driving migration. The SBM is indeed capable of accurately predicting both the magnitude and the dynamics of migration when a phenomenological term involving a concentration gradient is added to the particle normal stresses determined in macroscopic experiments.
January 2024
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29 Reads
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5 Citations
Journal of Fluid Mechanics
We experimentally investigate the rotational dynamics of neutrally buoyant axisymmetric particles in a simple shear flow. A custom-built shearing cell and a multi-view shape-reconstruction method are used to obtain direct measurements of the orientation and period of rotation of particles having oblate and prolate shapes (such as spheroids and cylinders) of varying aspect ratios. By systematically changing the viscosity of the fluid, we examine the effect of inertia (which may be originated from either phase) on the dynamical behaviour of these suspended particles up to a particle Reynolds number of approximately one. While no significant effect on the period of rotation is found in this small-inertia regime, a systematic drift among several rotations toward limiting stable orbits is observed. Prolate particles are seen to drift towards the tumbling orbit in the plane of shear, whereas oblate particles are driven either to the tumbling or to the vorticity-aligned spinning orbits, depending on their initial orientation. These results are compared with recent small-inertia asymptotic theories, assessing their range of validity, as well as to numerical simulations in the small-inertia regime for both prolate and oblate particles.
... 29,44 Variations of the local packing fraction due to particle migration might be responsible for inducing this transition in the central region of the gap and thus for the onset of plug-like flow. Particle migration and associated complex velocity profiles have been also observed in non-Brownian particulate suspensions 43,45,46 and interpreted in terms of the suspension balance model. 47 However, Brownian diffusion plays a key role in our suspensions. ...
October 2024
Journal of Rheology
... Various constitutive models have been introduced based on defining appropriate dimensionless numbers, but their validity is often limited to specific scenarios [5][6][7][8][9][10]. Therefore, identifying suitable quantities to establish constitutive laws to describe the rheology of different types of dense suspensions under various driving conditions has been a topic of intense research [6,[11][12][13][14][15][16][17]. ...
September 2024
Physical Review Fluids
... The solvent has a contact angle θc < 5 o on the glass substrate. Note that the presence of particles does not modify the density or the surface tension of the suspension (See Ref. 43,44 ). We disperse the nylon fibers of various aspect ratios A = L/D at different volume fractions ϕ in the solvent. ...
January 2023
Journal of Fluid Mechanics
... As in recent studies, constitutive laws describing steady uniform flows (i.e. at the critical state) are written in terms of a combination of two dimensionless numbers, based on the assumption of additivity of inertial and viscous stresses [2,12,13,60,62]. These two independent numbers I and J characterize inertial and viscous regimes, respectively: ...
August 2022
Physical Review Letters
... Finally, the inertial number squared, I 2 = ργ 2d2 /p c , is a ratio of the bulk measure of the inertial pressure to the confining pressure in the material. Based on the additive property of stress, it has been shown recently that the µ(I) rheology can be extended to a wide range of cohesive materials and suspensions (i.e., submerged flows), provided that I is computed in a more general way, i.e., as a ratio of the linear combination of all stresses related to the grains' motion to the linear combination of stresses related to grain contacts [39,40]. Thus -again, importantly for potential applications to sea ice -cohesive and viscous interactions associated with the presence of fluid in spaces between grains can be included together with the 'standard' elastic and frictional graingrain interactions. ...
February 2022
... These studies have successfully reproduced experimental observations regarding the threshold for sediment erosion Θ c [97] and the scaling of the sediment particle flux for Θ > Θ c [6]. Figure 6.8a shows the particle flow rate as a function of the Shields number obtained from the PR-DNS by Kidanemariam & Uhlmann [72], recovering the well-known cubic variation of the particle flow rate with the Shields number for Θ > Θ c . Furthermore, the direct access to the hydrodynamic and collision forces acting upon individual particles in PR-DNS has enabled the investigation of the rheological proprieties of the mobile sediment bed and the contribution of fluid and particle stresses to the momentum transfer between the two phases [68,137]. ...
August 2021
Journal of Fluid Mechanics
... 33,35 The interplay between the particle size and the film thickness on the entrainment regime has allowed the development of a capillary sorting method for polydisperse suspensions. 36,38 The interplay between interfacial dynamics and particles can become even more challenging to describe with anisotropic particles, such as suspensions of fibers, 39,40 An additional complexity with suspensions of fibers is that they are characterized by two dimensions: the diameter d and the length L, leading to the definition of the aspect ratio a = L/d. In the case of dip coating, it remains unclear how the entrainment threshold and the different coating regimes reported for suspensions of spherical particles translate to situations where the particles to be deposited are of more complex shapes. ...
April 2021
Physical Review Fluids
... [21][22][23][24][25] A recent paper also proposed that even if inertia is negligible at the low Reynolds numbers considered for small particles, the effect of inertia may be non-negligible at Reynolds numbers considered for large blobs. 26 In other words, the inertial effects considered for blobs may reduce velocity fluctuations. ...
May 2021
Journal of Fluid Mechanics
... Measurements (Franceschini et al., 2011;Strednak et al., 2021) and simulations (Snook et al., 2012;Strednak et al., 2021) of the orientation distribution under oscillatory flows also demonstrate a remarkable transition in the alignment as a function of strain amplitude. As shown in Fig. 9b for the same aspect ratio A = 11 and a concentration of ϕ = 0.20, the order parameter S θ is maximized when γ 0 ≈ 2.5 (γ 0 ϕ/Φ c ≈ 1.25 where Φ c = 0.4). ...
January 2021
Physical Review Fluids
... The one-way coupling point-wise approach is safe for particles smaller than the Kolmogorov scale and in dilute conditions [28,7]. Yet, when the number of particles is high and/or the diameter is large, the flow becomes semi-dilute or even moderately dense, with a dramatic impact on the flow [3,29,30,7,31]. On the other hand, even in dilute conditions, the interaction between particles larger than the Kolmogorov scale and the flow may lead to non-trivial phenomena, including long-range interactions, e.g. wakes. ...
February 2021
Journal of Fluid Mechanics