Motion of a sphere parallel to plane walls in a Poiseuille flow. Application to field-flow fractionation and hydrodynamic chromatography

被引:31
作者
Pasol, L. [2 ]
Martin, M. [2 ]
Ekiel-Jezewska, M. L. [3 ]
Wajnryb, E. [3 ]
Blawzdziewicz, J. [4 ]
Feuillebois, F. [1 ]
机构
[1] LIMSI, UPR CNRS 3251, F-91403 Orsay, France
[2] Univ Paris Diderot, PMMH, UMR CNRS 7636, Univ Paris 06,ESPCI ParisTech, F-75231 Paris 05, France
[3] Polish Acad Sci, Inst Fundamental Technol Res, PL-02106 Warsaw, Poland
[4] Texas Tech Univ, Dept Mech Engn, Lubbock, TX 79409 USA
关键词
Creeping flow; Particle; Suspension; Interaction with walls; Separations; Selectivity; SLOW VISCOUS MOTION; CREEPING FLOW; PARTICLE; CHANNELS; FORCES; SIZE;
D O I
10.1016/j.ces.2011.05.033
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The motion of a solid spherical particle entrained in a Poiseuille flow between parallel plane walls has various applications to separation methods, like field-flow fractionation and hydrodynamic chromatography. Various handy formulae are presented here to describe the particle motion, with these applications in mind. Based on the assumption of a low Reynolds number, the multipole expansion method coupled to a Cartesian representation is applied to provide accurate results for various friction factors in the motion of a solid spherical particle embedded in a viscous fluid between parallel planes. Accurate results for the velocity of a freely moving solid spherical particle are then obtained. These data are fitted so as to obtain handy formulae, providing e.g. the velocity of the freely moving sphere with a 1% error. For cases where the interaction with a single wall is sufficient, simpler fitting formulae are proposed, based on earlier results using the bispherical coordinates method. It appears that the formulae considering only the interaction with a nearest wall are applicable for a surprisingly wide range of particle positions and channel widths. As an example of application, it is shown how in hydrodynamic chromatography earlier models ignoring the particle-wall hydrodynamic interactions fail to predict the proper choice of channel width for a selective separation. The presented formulae may also be used for modeling the transport of macromolecular or colloidal objects in microfluidic systems. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4078 / 4089
页数:12
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