People | Locations | Statistics |
---|---|---|
Naji, M. |
| |
Motta, Antonella |
| |
Aletan, Dirar |
| |
Mohamed, Tarek |
| |
Ertürk, Emre |
| |
Taccardi, Nicola |
| |
Kononenko, Denys |
| |
Petrov, R. H. | Madrid |
|
Alshaaer, Mazen | Brussels |
|
Bih, L. |
| |
Casati, R. |
| |
Muller, Hermance |
| |
Kočí, Jan | Prague |
|
Šuljagić, Marija |
| |
Kalteremidou, Kalliopi-Artemi | Brussels |
|
Azam, Siraj |
| |
Ospanova, Alyiya |
| |
Blanpain, Bart |
| |
Ali, M. A. |
| |
Popa, V. |
| |
Rančić, M. |
| |
Ollier, Nadège |
| |
Azevedo, Nuno Monteiro |
| |
Landes, Michael |
| |
Rignanese, Gian-Marco |
|
Louvet, Nicolas
Université de Lorraine
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (6/6 displayed)
- 2017Shear-banding predicted by a constitutive model with a structural parameter in cylindrical Couette flows
- 2017Taylor-Couette instability in thixotropic yield stress fluids according a structural parameter model
- 2017Irreversible behavior of sheared dense non-Brownian fibers suspensions
- 2017Irreversible behavior of sheared dense non-Brownian fibers suspensions
- 2017Taylor-Couette instability in thixotropic yield stress fluidscitations
- 2014Nonuniversality in the Pinch-Off of Yield Stress Fluids: Role of Nonlocal Rheologycitations
Places of action
Organizations | Location | People |
---|
document
Irreversible behavior of sheared dense non-Brownian fibers suspensions
Abstract
Local rheometry of non-Brownian fibers suspensions is investigated using both classical rheometry and MRI measurements in a cylindrical Couette configuration (fig. 1 left). It allows us to extract the local and the global rheometry for different applied shear rates and volume fraction φ. We observed a localized flow. The fluid/solid interface position depends on φ and the shear rate ˙ γ. We discuss the irreversible behavior of the flow. Near the jamming transition, we observe that the suspension becomes like a yield stress fluid. Nevertheless , an irreversible destructuring behavior is put in evidence (fig. 1. right). Our data can be well fitted to a Hershel-Bulkley law. We discuss the evolution of the consistency, the shear-thinning index and the yield stress with the volume fraction of the suspension. Models using a structural parameter, such as Houska's model [1] or Mills' model [2] use a kinetic equation for the structural parameter which implies reversible destructuring flows. For exemple, Houska's model, used for waxy crud oils, can not reproduce irreversible behavior in flows with a complex history [3-4]. New kinetic for the structural parameter should be proposed to take into account irreversible flows. 0.008 0.009 0.01 0.011 0.012 0.013 0.014 0.015 Radial position (m) 0 0.002 0.004 0.006 0.008 0.01 0.012 0.014 0.016 Velocity (m/s) 6rpm (up) 9rpm (up) 15rpm (up) 21rpm (up) 15rpm (down) 9rpm (down) 6rpm (down) Figure 1: Couette setup and MRI velocity profiles in fibers suspension (mass ratio 24.7/120, i.e. φ =?). Full and dashed lines stand for growing and decreasing steps of velocity.