Streaming Potential and Electroosmotic Flow in
Heterogeneous Circular Microchannels with Nonuniform
Zeta Potentials: Requirements of Flow Rate and Current
Continuities
Jun Yang,
†
J. H. Masliyah,
‡
and Daniel Y. Kwok*
,†
Nanoscale Technology and Engineering Laboratory, Department of Mechanical Engineering
and Department of Chemical and Materials Engineering, University of Alberta,
Edmonton, Alberta T6G 2G8, Canada
Received July 9, 2003. In Final Form: December 3, 2003
Real surfaces are typically heterogeneous, and microchannels with heterogeneous surfaces are commonly
found due to fabrication defects, material impurities, and chemical adsorption from solution. Such surface
heterogeneity causes a nonuniform surface potential along the microchannel. Other than surface
heterogeneity, one could also pattern the various surface potentials along the microchannels. To understand
how such variations affect electrokinetic flow, we proposed a model to describe its behavior in circular
microchannels with nonuniform surface potentials. Unlike other models, we considered the continuities
of flow rate and electric current simultaneously. These requirements cause a nonuniform electric field
distribution and pressure gradient along the channel for both pressure-driven flow (streaming potential)
and electric-field-driven flow (electroosmosis). The induced nonuniform pressure and electric field influence
the electrokinetic flow in terms of the velocity profile, the flow rate, and the streaming potential.
I. Introduction
The presence of an electric double layer (EDL) at the
solid-liquid interface and its electrokinetic phenomena
have been used to develop various chemical and biological
instruments.
1-3
A common assumption is the uniformity
of surface properties during electrokinetic fluid transport
in microchannels.
4-9
Nevertheless, surface heterogeneity
can easily arise from fabrication defects or chemical
adsorption onto microchannels. For example, Norde et
al.
10
studied the relationship between protein adsorption
and streaming potentials. Ajdari
11,12
presented a theoreti-
cal solution for electroosmotic flow through inhomogeneous
charged surfaces. Ren and Li
13
numerically studied
electroosmotic flow in heterogeneous circular microchan-
nels with axial variation of the surface potential. Anderson
and Idol
14
studied electroosmosis through pores with
nonconformed charged walls. They showed that the mean
electroosmotic velocity within the capillary was given by
the classical Helmholtz equation with the local surface
potential replaced by the average surface potential. Keely
et al.
15
theoretically provided flow profiles inside capillaries
with nonuniform surface potentials. Herr et al.
16
theoreti-
cally and experimentally investigated electroosmotic flow
in cylindrical capillaries with nonuniform surface charge
distributions. A nonintrusive caged fluorescence imaging
technique was used to image the electroosmotic flow; a
parabolic velocity profile induced by the pressure gradient
due to the heterogeneity of the capillary surfaces was
observed. Cohen and Radke studied streaming potentials
of a slit with a nonuniform surface charge density.
17
Erickson and Li
18
studied microchannel flow with patch-
wise and periodic surface heterogeneity. However, all the
above studies
10-18
assumed uniform axial electric fields
along the microchannel and did not consider continuity
of electric current.
Phenomenologically, let us consider two independent
microchannels with the same geometry, electrolyte, and
flow rate. If these two channels have different surface
potentials, the electric fields associated with the electric
double layer would have to be different. If we assemble
these two independent channels in series as sections of
a channel, the electric field should be nonuniform along
the flow direction and current continuity should also be
satisfied. It is the purpose of this paper to study oscillating
electrokinetic (streaming potential and electroosmotic)
flow in a microchannel with different surface potentials
in every section which satisfy both flow rate and current
continuity requirements.
* To whom correspondence should be addressed. Phone: (780)
492-2791. Fax: (780) 492-2200. E-mail: daniel.y.kwok@ualberta.ca.
†
Department of Mechanical Engineering.
‡
Department of Chemical and Materials Engineering.
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10.1021/la035243u CCC: $27.50 © 2004 American Chemical Society
Published on Web 04/09/2004