J. Rheol. 50, 77 (2006); http://dx.doi.org/10.1122/1.2139098 (16 pages)
Laser tweezer microrheology of a colloidal suspension
The microrheology of a colloidal suspension is measured using laser tweezers. Suspensions of refractive index-matched fluorinated ethylene propylene (FEP) particles are seeded with index-mismatched polystyrene or silica probe particles. Laser trapped probes are then subjected to steady uniform flows, enabling measurements of the suspension microviscosity as a function of FEP volume fraction and flow velocity. The microrheology results agree with bulk rheology, and both exhibit the same volume fraction dependence of the Krieger-Dougherty relationship for hard spheres. As volume fraction increases, the microrheology more closely agrees with the infinite shear bulk viscosity. In this regime, measurements using small probes exhibit additional shear thinning. Using confocal microscopy and fluorescent poly(methylmethacrylate) dispersions, we demonstrate that the nonlinear microrheology is consistent with the development of an anisotropic nonequilibrium pair distribution function between the probe and bath particles, with a denser region at the leading surface of the probe and a wake trailing it. The nonlinear response and underlying microstructure are in qualitative agreement with recent theory [
T. M. Squires and J. F. Brady, Phys. Fluids 17, 073101 (2005)
].
© 2006 The Society of Rheology
ACKNOWLEDGMENTS
The authors thank John Brady, Todd Squires, and Norman Wagner for helpful discussions and Andrew Hollingsworth, Michael Solomon, and Bill Russel for providing PMMA particles. They also acknowledge supporting experimental instrumentation by John Bishop. Financial support for this work was provided by the National Science Foundation (CTS-0238689).
Article Outline
- INTRODUCTION
- EXPERIMENTAL METHODS
- Materials
- Laser tweezer microrheology
- Experimental error
- Confocal microscopy
- Bulk rheology
- RESULTS AND DISCUSSION
- CONCLUSIONS
KEYWORDS and PACS
RELATED DATABASES
ARTICLE DATA
History
Received 01 Sep 05
Revised 13 Oct 05
Revised 13 Oct 05
Digital Object Identifier
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Figures (click on thumbnails to view enlargements)
Scanning electron micrograph of the FEP bath particles. The average particle diameter is 157±20 nm.
The laser tweezer experimental geometry. An index-mismatched probe particle is held far from the sample interface (>100 μm) using an optical trap. By translating the microscope stage, a uniform flow of the index-matched bath suspension is generated past the probe. The displacement Δx of the probe center from the equilibrium trap position, measured using video microscopy, gives the corresponding drag force. Note that the schematic is not to scale.
The drag force on a 3.2 μm PS probe particle in a suspension of FEP plotted as a function of fluid velocity. The slope of the force increases with the FEP volume fraction for ϕ = 0.08 (solid triangle), 0.16 (open triangle), 0.23 (solid square), and 0.31 (open circle).
The drag force on a 2.25 μm silica probe particle in a suspension of FEP plotted as a function of fluid velocity for ϕ = 0.02 (closed circle), 0.04 (open square), 0.16 (closed triangle), 0.19 (open triangle), 0.28 (solid square), and 0.31 (open circle).
The drag force on a 1.0 μm PS probe particle in a suspension of FEP plotted as a function of the velocity for ϕ = 0.08 (inverted triangle), 0.16 (triangle), and 0.23 (closed square). The line for ϕ = 0.23 is fit to the first half of the points and shows nonlinear behavior at high velocities.
The relative microviscosity ηr,micro = ηmicro/ηs using laser tweezer microrheology and relative viscosity ηr from bulk rheology (open circles) are plotted vs the FEP volume fraction ϕ. Measurements are shown for probe particles of various sizes and chemistries, including 3.2 μm PS (solid squares), 2.25 μm silica (solid diamonds), 1.1 μm PS (solid circles), 1.0 μm PS (solid inverted triangle) and 2.8 μm PS (solid upright triangle). The solid line is the Krieger-Dougherty equation with an effective diameter deff = 0.18 μm, effective packing fraction ϕm = 0.62, and intrinsic viscosity [η] = 2.46. The dashed line is an estimate of the high-shear relative viscosity using ϕm = 0.71.
The relative viscosity is plotted as a function of the Peclet number for 1.0 μm (closed symbols) and 3.2 μm (open symbols) PS probe particles in FEP at volume fractions ϕ = 0.08 (inverted triangles), 0.16 (triangles), and 0.23 (squares). The error bars reflect the accuracy of the laser tweezer force measurements, but do not take into account sample-to-sample variations, which can shift each series of data as much as ±0.2.
The microviscosity (squares) compared with the macroviscosity (diamonds) for ϕ = 0.23 FEP. The solid and open squares represent 1.0 and 2.8 μm probes, respectively. (a) The macroviscosity is plotted vs Pe, while the microviscosity is plotted vs Pemicro. The dashed line is an estimate of ηr∞ based on the Krieger-Dougherty equation with ϕm = 0.71. (b) Shifting Pemicro by a factor 1/β collapses the data onto a master curve.
Averaged confocal frames showing the structure of a dilute PMMA suspension (2ab = 1 μm, ϕ = 0.04) flowing past a stationary, optically trapped 2 μm melamine probe. The bright ring around the melamine particle is due to attached PMMA particles, giving an effective probe diameter of 4 μm. The flow is from left to right for Pemicro = 50 (a), 150 (b), and 300 (c). The scale bar is 10 μm.
Intensity profiles from confocal imaging taken along the flow centerlines for Pemicro = 50 (circles), 150 (squares), and 300 (triangles). The flow is directed from the left to the right. The two largest peaks in each case are the attached PMMA particles. The inset shows the upstream profile in greater detail.



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