CHARACTERIZATION OF NEAR-WALL HYDRODYNAMIC LIFT FORCES USING SEDIMENTATION FIELD-FLOW FRACTIONATION
- 1 January 1992
- journal article
- research article
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 111 (1) , 121-147
- https://doi.org/10.1080/00986449208935984
Abstract
In field-flow fractionation (FFF), a family of high resolution techniques for the separation of particles and polymers, the measured retention time of entrained particles eluting through a thin (50-500 μm) parallel plate channel is determined by the transverse forces acting on the particles during their migration. For particles in the size range ∼l-100μm an applied transverse driving force (in the present case sedimentation) rapidly brings the particles into balance with hydrodynamic lift forces, so that the two force vectors are equal in magnitude but opposite in direction. By subjecting latex microspheres of known size and density to a specified rotation rate in a centrifuge, the applied sedimentation force is known and thus the magnitude of the lift forces is immediately obtained. The transverse particle position can be determined from the measured particle retention time. Thus lift forces can be determined as a function of particle size, transverse position, and flowrate. This strategy has been used to characterize the lift forces acting on spherical particles driven close to one channel wall. This characterization promises to be useful for the improved understanding and optimization of FFF, crossflow membrane separation, and other processes involving particle motion close to walls In this study, 519 retention measurements were made on eight latex microsphere standards of 2.0-44.6 μm diameter using flowrates of 1.88-38.0 mL/min in a 254 μm thick FFF channel subjected to 7-343 gravities. Multiple linear regression analysis yielded an expression for the lift force FL of the form where a is the particle radius, η is the fluid viscosity, s0 is the undisturbed shear rate at the wall, δ is the distance of closest approach of the sphere to the wall, and C is a coefficient that may itself depend on other system parameters. Possible sources of experimental error were examined but none changed the general form of the above equation. Since the expression is inconsistent with an inertial lift mechanism it is postulated that the lift forces observed are related to lubrication phenomena.Keywords
This publication has 60 references indexed in Scilit:
- Rapid particle size analysis of ground minerals by flow/hyperlayer field-flow fractionationPowder Technology, 1989
- Gravity-augmented high-speed flow/steric field-flow fractionation: simultaneous use of two fieldsAnalytical Chemistry, 1988
- ELECTROKINETIC REPULSION BETWEEN TWO CHARGED BODIES UNDERGOING SLIDING MOTIONChemical Engineering Communications, 1987
- Crossflow Gradients in Thin Channels for Separation by Hyperlayer FFF, SPLITT Cells, Elutriation, and Related MethodsSeparation Science and Technology, 1986
- The lift on a small sphere touching a plane in the presence of a simple shear flowZeitschrift für angewandte Mathematik und Physik, 1985
- Characterization of fine coal particles by steric field-flow fractionationFuel, 1984
- Verification of retention and zone spreading equations in sedimentation field flow fractionationAnalytical Chemistry, 1981
- The lateral migration of solid particles in a laminar flow near a planeInternational Journal of Multiphase Flow, 1977
- Particle motions in sheared suspensions XXII: Interactions of rigid spheres (experimental)Rheologica Acta, 1967
- Radial Particle Displacements in Poiseuille Flow of SuspensionsNature, 1961