Particle dynamics in dense suspensions flowing through microchannels
Somnath Ghosh, Frieder Mugele and Michel Duits
University of Twente, the Netherlands
Introduction
While colloidal hard sphere suspensions are well-known as model fluids, much less is known about their behavior when they are made to flow through microchannels. We have initiated a study into the spheres’ spatial distribution, flow profile and (apparent) diffusive behavior, as a function of the volume fraction (0.01-0.4), and the Péclet number (0 to 40) which indicates the strength of the shear flow as compared to Brownian motion: Pé=6𝜋η0γ
′𝑎3
𝑘𝑇 . Cross-sectional channel dimensions are taken 30-50 particle diameters,
while also the roughness of the wall is varied. After confocal microscopy measurements, the particles’ positions and displacements are analyzed using (adapted) tracking codes written in IDL language.
50μm
Observations
Flow
Conclusions
Velocity profileConcentration profile Apparent diffusivity normal to the flow
Use of both low- and high viscous solvents allows to address a broad range of Peclet numbers, while keeping the maximum flow velocity low enough for particle tracking.
Separating the diffusive displacements from the convective ones requires great care, both at high and low Pe. Velocity profiles are nearly parabolic. Slip is always suppressed at the rough wall.
The dependence of D┴ on Pe and the distance relative to the walls still needs to be understood.
Experiments
CSLM: 488 nm (λwave) @ 15 mW 100X /oil
objective,10 to 15 fps glass cover slip
PDMS Channel cross-section Pressure head (0-20mm) FITC-labeled silica (2a = 1μm) suspensions in polar solvent y z Rough wall Smoot h wall
solvents:
1._Methanol + Bromoform (low viscous)
2._Water + Glycerol (high viscous)
both refractive index matching for silica solvent 1 is also density-matching.
flow speeds: 0.1 – 10 µm/s
movies: 500-1000 frames per condition measurables:
1. local particle number density
2. local mean velocity along flow direction 3. Mean Square Displacement normal to flow: <∆y2> = 2 D┴ t Low Pe High Pe 0 10 20 30 40 50 60 0.0 0.1 0.2 0.3 0.4 Pe = 4.34 Pe = 7.31 Pe= 11.83 Pe= 22.65 Pe= 26.76 Pe= 29.28
Distance from the rough wall (m)
Parti cl e cover age 0 10 20 30 40 50 60 0 2 4 6 8 10
Distance from the rough wall (m)
A verage vel oci ty ( m/ s ) 0 10 20 30 40 50 60 0.0 5.0x10-4 1.0x10-3 1.5x10-3 2.0x10-3 2.5x10-3 3.0x10-3
Distance from the rough wall (m)
MSD
(
m