Anthony Wachs


Research Interests

Fluid mechanics
Particle-laden flows
Non Newtonian flows
Heat and mass transfer
Numerical simulation
High performance computing
Multi-scale modelling

Relevant Degree Programs

Affiliations to Research Centres, Institutes & Clusters

Research Options

I am available and interested in collaborations (e.g. clusters, grants).
I am interested in and conduct interdisciplinary research.

Research Methodology

Numerical modeling
Parallel code developement
Parallel computing


Doctoral students
Any time / year round
  • Development of massively parallel codes for granular and particle-laden flow simulation
  • Multi-scale modeling of particle-laden flows
  • Shape effect in granular and particle-laden flows
  • Heat and mass transfer in fluidized beds
  • Blood flow and application to targeted drug delivery
I support public scholarship, e.g. through the Public Scholars Initiative, and am available to supervise students and Postdocs interested in collaborating with external partners as part of their research.
I am open to hosting Visiting International Research Students (non-degree, up to 12 months).
I am interested in supervising students to conduct interdisciplinary research.

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Postdoctoral Fellows

Graduate Student Supervision

Doctoral Student Supervision (Jan 2008 - May 2021)
Particle-resolved simulations of inertial suspensions of spheres and polyhedrons: analysis and modeling (2021)

Particle-laden flows where a dispersion of a solid phase is carried by a fluid phase are at the core of numerous industrial and natural processes, such as fluvial sediment transport and fluidized-bed reactors. The dynamics of each phase is intimately coupled with that of the other phase, leading to the emergence of complex, nontrivial interactions that can span wide ranges of spatial and temporal scales. The focus of this thesis is two-fold; namely, analysis of particle shape effects, and modeling hydrodynamic forces and torques in particle-laden flows. To this end, direct numerical simulations are performed for the generation of high-fidelity data, based on which all analyses of this thesis are carried out. In the first part, we scrutinize the dynamics of an isolated polyhedron, i.e. a cube, in highly inertial regimes and various density ratios. Robust helical motions and wake patterns are found for Reynolds numbers at which a sphere moves rectilinearly. An isolated cube exhibits remarkably larger rotational and lateral motions compared to a sphere, by which the effective drag on the particle is greatly affected. We then extend the analysis to inertial suspensions of cubes, where detailed comparisons are made with their counterpart sphere suspensions for various solid volume fractions. While strong clustering occurs in sphere suspensions, cube suspensions are found to be remarkably more homogeneous, as evident from their microstructure and momentum transfer properties. As demonstrated by their intensive transverse velocity fluctuations, cubes are more likely to break up and escape clusters, thus resisting local accumulation and making suspensions better mixed. In the second part, we develop a novel probability-driven point-particle model for the prediction of hydrodynamic forces and torques based on local microstructure in dense arrays of spheres. Following probabilistic arguments, necessary statistical information is extracted from particle-resolved simulations to construct force/torque-conditioned probability distribution maps, which are in turn used as basis functions for a regressive-type model. We subsequently show that our model is capable of predicting a substantial part of the observed force and torque variations, and is thus conceived to be highly promising for accurate interphase coupling in Euler-Lagrange simulations.

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Particles in a yield-stress fluid: yield limit, sedimentation and hydrodynamic interaction (2018)

A theoretical and numerical study of yield-stress fluid creeping flow about a particle is presented motivated by theoretical aspects and industrial applications. Yield stress fluids can hold rigid particles statically buoyant if the yield stress is large enough. In addressing sedimentation of rigid particles in viscoplastic fluids, we should know this critical `yield number' beyond which there is no motion. As we get close to this limit, the role of viscosity becomes negligible in comparison to the plastic contribution in the leading order, since we are approaching the zero-shear-rate limit. Admissible stress fields in this limit can be found by using the characteristics of the governing equations of perfect plasticity (i.e., the sliplines). This approach yields a lower bound of the critical plastic drag force or equivalently the critical yield number. Admissible velocity fields also can be postulated to calculate the upper bound. This analysis methodology is examined for different families of particle shapes. Numerical experiments of either resistance or mobility problems in a viscoplastic fluid validate the predictions of slipline theory and reveal interesting aspects of the flow in the yield limit. For instance, the critical limit is not unique and here we show that for the same critical limit we may have different shaped particles that are cloaked inside the same unyielded envelope. The critical limit (or critical plastic drag coefficient) is related to the unyielded envelope rather than the particle shape. We show how to calculate the unyielded envelope directly. Here we also address the case of having multiple particles, which introduces interesting new phenomena. Firstly, plug regions can appear between the particles and connect them together, depending on the proximity and yield number. This can change the yielding behaviour since the combination forms a larger (and heavier) "particle". Moreover, small particles (that cannot move alone) can be pulled/pushed by larger particles or assembly of particles. Increasing the number of particles leads to interesting chain dynamics, including breaking and reforming.

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Master's Student Supervision (2010 - 2020)
Shear rheology of non-Newtonian emulsions made of viscoelastic droplets in a Newtonian matrix (2020)

In the case of an oil spill in a marine environment, an important aspect of an early response is to confine the oil spill and prevent it from getting dispersed. At the laboratory level, chemists are capable of designing new solidifiers known as "gellants", that when applied by spraying or injection in the marine oil-spill, are capable of making the oil regroup and create a gel-like material (gelled-oil). Even though gellants make the removing of oil-spill from a marine environment easier, it is not clear whether gelled-oil is more stable in terms of break-up and how gellants affect the dispersion rate of the oil-spill. Gellants create a gelled-oil emulsion in the marine environment, which can be modelled as a dispersion of non-Newtonian droplets (gelled-oil) in a Newtonian matrix (sea water). In this study we develop a better understanding of such a liquid/liquid system subjected to imposed shear. Both the rheological nature of the oil and the oil/water surface tension are the key parameters. We address this problem from a computational viewpoint using an advanced open source academic code to perform parallel simulations. We analyze two main problems: 1) the deformation of a single droplet in a simple shear flow, and 2) the rheological behaviour of an emulsion in a simple shear flow. We show that, since applying gellants increase the surface tension and viscosity of the dispersed oil phase, the oil-water emulsion is more stable (i.e. the dispersed oil droplets deform less) and the dispersion rate of the oil in the marine environment is reduced. Moreover, we obtain results showing that the elasticity of the dispersed gelled-oil phase has a non-monotonic impact on the flow features and a very limited influence on the general behaviour of the emulsion. The conducted analysis in this project and its outcome can help to provide recommendations on how these gelled materials behave.

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