Film mass transfer coefficient expressions for electroosmotic flows

被引:19
作者
Liapis, AI [1 ]
Grimes, BA
机构
[1] Univ Missouri, Dept Chem Engn, Rolla, MO 65409 USA
[2] Univ Missouri, Biochem Proc Inst, Rolla, MO 65409 USA
关键词
film mass transfer coefficient; electroosmotic flow; packed bed; charged particles; charged porous monolith; microchannel devices;
D O I
10.1006/jcis.2000.7061
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Expressions are developed and presented that could be used to determine the film mass transfer coefficient of a solute in electroosmotic flows. In contrast to pressure-driven flows at low Reynolds numbers where the film mass transfer coefficient is independent of the linear characteristic dimension of the channel for how in electroosmotically driven flows at low Reynolds numbers the film mass transfer coefficient is shown to be a function of the ratio R/lambda, where R is the channel radius and lambda is the Debye length. This result implies that for electroosmotically driven flows in a packed bed or porous monolith with channels for flow having similar geometry but different sizes, the film mass transfer coefficient would vary with the size of the interstitial channels for bulk flow while in pressure-driven hows the film mass transfer coefficient would be the same for all interstitial channels. From the expressions presented in this work, one can show that for the same volumetric flow rate the film mass transfer coefficient of electroosmotically driven flows is proportional to that for pressure-driven flows, (C) 2000 Academic Press.
引用
收藏
页码:540 / 543
页数:4
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