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The Journal of Chemical Physics logoLink to The Journal of Chemical Physics
. 2013 Aug 22;139(8):084101. doi: 10.1063/1.4818733

Aris-Taylor dispersion with drift and diffusion of particles on the tube wall

Alexander M Berezhkovskii 1, Alexei T Skvortsov 2,a)
PMCID: PMC3765244  PMID: 24006968

Abstract

A laminar stationary flow of viscous fluid in a cylindrical tube enhances the rate of diffusion of Brownian particles along the tube axis. This so-called Aris-Taylor dispersion is due to the fact that cumulative times, spent by a diffusing particle in layers of the fluid moving with different velocities, are random variables which depend on the realization of the particle stochastic trajectory in the radial direction. Conceptually similar increase of the diffusivity occurs when the particle randomly jumps between two states with different drift velocities. Here we develop a theory that contains both phenomena as special limiting cases. It is assumed (i) that the particle in the flow can reversibly bind to the tube wall, where it moves with a given drift velocity and diffusivity, and (ii) that the radial and longitudinal diffusivities of the particle in the flow may be different. We derive analytical expressions for the effective drift velocity and diffusivity of the particle, which show how these quantities depend on the geometric and kinetic parameters of the model.

INTRODUCTION

The increase of the diffusivity of Brownian particles due to a radial gradient of advection velocity (often referred to as the Aris-Taylor or shear dispersion1, 2, 3) is of a significant importance in a number of fields of science and technology covering many practical applications. Examples include chemical engineering (microfluidics,4 chromatography,5, 6 heterogeneous catalysis2), biophysics (vascular flow,7 airflow in lungs,8 targeted drug delivery9), and transport processes in geophysical systems (capillary flows in fractures,10 colloid filtration,11 mixing in rivers12). Starting with the seminal works of Taylor,13, 14 who calculated the diffusivity of a passive tracer in the Poiseuille flow (laminar flow in a cylindrical tube), followed by a more rigorous derivation of Aris,15 this problem has been in the focus of both theoretical and experimental studies for the last six decades. There is a vast amount of literature devoted to this subject (see Refs. 1, 2, 3, 16, 17 and references therein). Although the Aris-Taylor dispersion is nowadays discussed in textbooks,1, 2, 16, 17 it is still the area of active research.18, 19, 20, 21, 22, 23

The celebrated result obtained by Taylor13, 14 can be summarized as follows. Consider a laminar stationary flow of viscous fluid in a cylindrical tube of radius a (Fig. 1). The velocity profile of the Poiseuille flow is given by the well-known expression

vf(r)=2v¯f1r2a2, (1.1)

where v¯f is the velocity averaged over the tube cross-section, v¯f=(2/a2)0avf(r)rdr. Taylor showed that the effective diffusivity of a point Brownian particle along the tube axis is given by

Deff=Df+v¯f2a248Df, (1.2)

where Df is the particle diffusivity in the absence of the flow.

Figure 1.

Figure 1

The Aris-Taylor dispersion of a Brownian particle with reversible binding to the tube walls: a is the tube radius, vf(r) is the velocity profile of the Poiseuille flow, vw is the particle velocity on the wall, Df and Dw are the particle diffusivities in the fluid and on the wall, κ and kw are the intrinsic rate constants (see Eq. 1.3).

Since the pioneering work of Taylor this problem has been extended to cover more complicated settings including various geometrical complexities,24, 25 oscillating flows,7, 26 transient phenomena,19 effects of chemical reactions,27, 28, 29 and many others (see, for instance, books1, 2 and recent papers19, 21). An important generalization of the problem is to account for the “effect of wall” (absorption and desorption, as well as diffusion of the particle on the wall). The “wall effect” is especially important for the design of microfluidic devices (so-called “Lab-on-a-Chip”17, 30). It has been studied theoretically in a number of recent publications (see Refs. 20, 22, 27, 31, 32 and references therein).

When a Brownian particle is advected by a laminar flow, its reversible binding to the tube wall can be described by the kinetic scheme

flow κkw wall , (1.3)

where κ and kw are the intrinsic rate constants (see Fig. 1). Let Pweq and Pfeq be the equilibrium probabilities of funding the particle on the wall and in the flow, Pweq+Pfeq=1. As follows from the principle of detailed balance the ratio of these probabilities is

PweqPfeq=2κakw=K, (1.4)

where K is the equilibrium constant. This allows us to write Pweq,Pfeq in terms of the equilibrium constant

Pfeq=11+K,Pweq=K1+K. (1.5)

If the particle on the wall diffuses with the diffusivity Dw and has no drift velocity, the effective drift velocity and diffusivity are given by1, 5, 20, 27

veff=v¯fPfeq, (1.6)
Deff=DfPfeq+DwPweq+D, (1.7)

where

D=Pfeq3v¯f2Kkw+a248Df(1+6K+11K2). (1.8)

An interesting result was obtained by Dorfman and Brenner,33 who pointed out that the increase of the particle diffusivity, which is conceptually identical to the Aris-Taylor dispersion, occurs when the particle randomly jumps between two states with different drift velocities. To formulate the Dorfman–Brenner results using the kinetic scheme in Eq. 1.3, we assume that the particle diffusion in the flow is anisotropic, namely, its radial diffusivity is infinite, while its diffusivity along the tube axis is finite and equal to Df. Then, when the particle enters the flow from the wall, it instantly equilibrates over the tube cross section. As a result, (i) the particle drift velocity in the flow does not fluctuate and is equal to v¯f, and (ii) its survival probability in the flow decays as a single exponential with the rate constant kf = 2κ/a. In addition, we assume that the particle on the wall has drift velocity vw and diffusivity Dw. In this case the Dorfman–Brenner theory leads to (see also Ref. 34)

veff=v¯fPfeq+vwPweq, (1.9)

and the effective diffusivity given by Eq. 1.7, in which △D is

D=Pfeq3(v¯fvw)2K/kw. (1.10)

In the present paper, we extend the results in Eqs. 1.6, 1.7, 1.8, 1.9, 1.10. More specifically, we developed a general theory assuming (i) that the radial diffusivity Dr of the particle in the flow can be arbitrary, and (ii) that the particle on the wall has a finite drift velocity vw. We will see that the effective drift velocity is given by Eq. 1.9, and the effective diffusivity has the form of Eq. 1.7 with △D given by

D=Pfeq3{(v¯fvw)2Kkw+a248Dr[(1+6K+11K2)v¯f24K(K+1)v¯fvw+6K2vw2]}. (1.11)

This is a modification of the expression for △D in Eq. 1.8 due to a finite particle drift velocity on the wall and its anisotropic diffusivity in the flow. Note that the product (Pfeq)3 and the first term in the curly brackets is identical to the Dorfman–Brenner formula for △D, Eq. 1.10. At vw=v¯f Eq. 1.11 simplifies and takes the form

D=Pfeq3v¯f2a248Dr(1+2K+13K2). (1.12)

The expressions in Eqs. 1.7, 1.9, 1.11 are the main results of the present paper. When vw = 0 and Dx = Dr = Df they reduce to Eqs. 1.6, 1.7, 1.8. In the other limiting case of Dr → ∞, we recover the Dorfman–Brenner formulas 1.7, 1.9, 1.10.

A number of methods have been developed for analytical treatment of the Aris-Taylor dispersion including the method of statistical moments (originally proposed by Aris15), the method of matched asymptotic expansions,27 the center manifold approach3, 35 and some others (see Refs. 19, 32 and references therein). In the present study, we apply the approach proposed in Ref. 18, which is based on consideration of the axial displacement of a single particle that moves in the plane perpendicular to the tube axis along a given trajectory {r}t. The approach exploits the fact that the radial motion of the particle is independent of its axial coordinate. Averaging the displacement and its square over realizations of {r}t, we find the first two moments of the particle displacement along the tube axis, which in turn are used to calculate veff and Deff.

The outline of the paper is as follows. The expressions for the effectively velocity, Eq. 1.9, and the effective diffusivity, Eqs. 1.7, 1.11, are derived in Secs. 2, 3, respectively. Some concluding remarks are made in Sec. 4.

EFFECTIVE DRIFT VELOCITY

Let r(t) be the particle position in the plane normal to the tube axis at time t; r = a corresponds to the particle on the tube wall, while r < a corresponds to the particle in the bulk flow. The particle velocity along the tube axis at time t is given by

x˙(t|r(t))=v(r(t))+f(t|r(t)), (2.1)

where the velocity v(r) is

v(r)=vf(r),r<a,vw,r=a, (2.2)

and f(t|r) is the Gaussian δ-correlated random force

f(t|r)=ff(t),r<a,fw(t),r=a, (2.3)

with zero mean ⟨ff(t)⟩ = ⟨fw(t)⟩ = 0. The correlation functions of the two components of the random force are ⟨ff(t)fw(t′)⟩ = 0, and

1Dfff(t)ff(t)=1Dwfw(t)fw(t)=2δ(tt), (2.4)

where the angular brackets ⟨…⟩ denote averaging over realizations of the random force.

Let {r}t be a particle trajectory observed for time t: {r}t={r(t),0tt}. We can formally integrate Eq. 2.1. Taking x(0) = 0, we find that

x(t|{r}t)=0tv(r(t)|{r}t)dt+0tf(t,r(t)|{r}t)dt. (2.5)

Averaging this over realizations of the random force and taking that the particle starts from r0=r(0), we obtain

x(t)r0=0tv(r(t)|{r}t)r0dt, (2.6)

where the subscript r0 indicates the particle initial position in the plane perpendicular to the tube axis. Using the identity

δ(rr(t))dr=1, (2.7)

Eq. 2.6 can be written as

x(t)r0=v(r)0tδ(rr(t)r0dtdr, (2.8)

where v(r) is given by Eq. 2.2.

The averaged δ-function is the particle propagator (the Green function) in the plane perpendicular to the tube axis

δ(rr(t))r0=G(r,t|r0). (2.9)

Therefore,

x(t)r0=v(r)0tG(r,t|r0)dtdr. (2.10)

This formula has a transparent interpretation.18 Since 0tG(r,t|r0)dtdr is the mean cumulative time spent by the Brownian particle observed for the time t in the small vicinity of point r, the integrand in Eq. 2.10 is the particle displacement during this cumulative time. Thus, Eq. 2.10 gives x(t)r0 as the sum of such displacements.

Next, we average x(t)r0, Eq. 2.10, over the equilibrium initial distribution peq(r0), where

peq(r)=1πa2PfeqH(ar)+12πaPweqδ(ra) (2.11)

with H(z) denoting the Heaviside step function. Hereafter, we assume that H(0) = 0 and 0aδ(ra)dr=1. The averaging leads to

x(t)eq=x(t)r0peq(r0)dr0=0tdtv(r)G(r,t|r0)peq(r0)drdr0. (2.12)

Finally, invoking the relation

G(r,t|r0)eq=G(r,t|r0)peq(r0)dr0=peq(r), (2.13)

we arrive at

x(t)eq=vefft, (2.14)

where the effective drift velocity of the particle is given by

veff=v(r)peq(r)dr=v¯fPfeq+vwPweq. (2.15)

This is the main result of this section.

EFFECTIVE DIFFUSIVITY

In this section, we derive the expression for the effective diffusivity Deff given in Eqs. 1.7, 1.11. We begin with the definition of Deff,

Deff=12limt1tx2(t)eqx(t)eq2, (3.1)

where ⟨x2(t)⟩eq is the second moment of the particle displacement x(t|{r}t), Eq. 2.5, averaged over the realizations of the random trajectory {r}t and the equilibrium radial distribution of the starting point, Eq. 2.11,

x2(t)eq=x2(t)r0peq(r0)dr0. (3.2)

The expression for x(t)eq2 immediately follows from Eq. 2.14:

x(t)eq2=veff2t2. (3.3)

Averaging the square of the displacement in Eq. 2.5 over the trajectories that start from r0, we can present x2(t)r0 as a sum of two terms

x2(t)r0=[x(t|{r}t)]2r0=T1(t|r0)+T2(t|r0), (3.4)

where

T1(t|r0)=0t0tv(r(t1)|{r}t)v(r(t2)|{r}t)r0dt1dt2 (3.5)

and

T2(t|r0)=0t0tf(t1,r(t1)|{r}t)f(t2,r(t2)|{r}t)r0dt1dt2. (3.6)

Then we can write ⟨x2(t)⟩eq as

x2(t)eq=T1eq(t)+T2eq(t), (3.7)

where

T1,2eq(t)=T1,2(t|r0)eq=T1,2(t|r0)peq(r0)dr0. (3.8)

We begin with T2(t|r0), Eq. 3.6. Using Eqs. 2.3, 2.4, one can check that the correlation function of the random force is

f(t1,r(t1)|{r}t)f(t2,r(t2)|{r}t)r0=2[DfPf(t|r0)+DwPw(t|r0)]δ(t1t2), (3.9)

where Pf(t|r0) and Pw(t|r0) are the probabilities of finding the particle in the flow and on the wall at time t, conditional on that it starts from r0 at t = 0. Substituting the correlation function, Eq. 3.9, into Eq. 3.6 we obtain

T2(t|r0)=20t[DfPf(t1|r0)+DwPw(t1|r0)]dt1.

Averaging this over the particle initial position and using the relationship

Pf,w(t|r0)eq=Pf,w(t|r0)peq(r0)dr0=Pf,weq, (3.10)

we arrive at a simple formula for T2eq(t),

T2eq(t)=2DfPfeq+DwPweqt, (3.11)

where Pf,weq are given by Eq. 1.5.

Next we proceed to the evaluation of T1(t|r0), Eq. 3.5. Using the relationships in Eqs. 2.7, 2.9, T1(t|r0) can be written as

T1(t|r0)=2v(r1)dr1v(r2)dr20tdt2×0t2G(r2,t2t1|r1)G(r1,t1|r0)dt1. (3.12)

Averaging this over r0 and using Eq. 2.13, we obtain

T1eq(t)=2v(r1)dr1v(r2)dr20tdt×0tG(r2,t|r1)peq(r1)dt. (3.13)

As t → ∞ the propagator G(r,t|r0) tends to peq(r), Eq. 2.11. Denoting the difference between the propagator and peq(r) by u(r,t|r0), we can write

G(r,t|r0)=peq(r)+u(r,t|r0), (3.14)

where u(r,t|r0)0 as t → ∞. In addition, u(r,t|r0) satisfies

u(r,t|r0)eq=u(r,t|r0)peq(r0)dr0=u(r,t|r0)dr=0. (3.15)

Substituting the propagator in Eq. 3.14 into Eq. 3.13, we can find the large-t asymptotic behavior of T1eq(t),

T1eq(t)=veff2t2+2tv(r2)dr2v(r1)θ(r2,r1)peq(r1)dr1, (3.16)

where

θ(r2,r1)=0u(r2,t|r1)dt. (3.17)

This integral is the Laplace transform of u(r2,t|r1) at the zero value of the Laplace parameter

θ(r2,r1)=u^(r2,s|r1|s=0, (3.18)

where F^(s) denotes the Laplace transform of function F(t), F^(s)=0F(t)exp(st)dt.

Eventually using the relationships in Eqs. 3.7, 3.11, 3.16, we find that the definition in Eq. 3.1 leads to the expression for Deff in Eq. 1.7, in which △D is

D=v(r2)dr2v(r1)θ(r2,r1)peq(r1)dr1. (3.19)

Thus, to finish the calculation of the effective diffusivity, we have to evaluate the double integral in Eq. 3.19.

Since the particle can be in two states (in the flow and on the wall), the angle-averaged particle propagator has two components, gf(r, t|σ) and Pw(t|σ), which are the probability density of finding the particle in the flow and the probability of finding the particle on the wall at time t, conditional on that it starts from state σ at t = 0. Initially, the particle can also be either in the flow or on the wall. Therefore, σ = r0, if the particle starts in the flow at distance r0 from the tube axis, and σ = w, if the particle is on the wall at t = 0. The four functions, gf(r, t|σ) and Pw(t|σ), satisfy

gft=Drrrrgfr,gfrr=0=0, (3.20)
dPwdt=2πaκgfr=akwPw=2πaDrgfrr=a, (3.21)

with the initial conditions

Pw(0|w)=1,gf(r,0|w)=0 (3.22)

and

Pw(0|r0)=0,gf(r,0|r0)=12πrδ(rr0), (3.23)

where gfgf(r, t|σ) and PwPw(t|σ).

It is convenient to introduce notations for the deviations of the two components of the propagator from their large-t asymptotic values (cf. Eq. 3.14),

Uw(t|σ)=Pw(t|σ)Pweq, (3.24)
uf(r,t|σ)=gf(r,t|σ)Pfeq/πa2. (3.25)

Denoting the Laplace transforms of these functions at s = 0 by U^w(σ)U^w(s|σ)|s=0 and u^f(r|σ)u^f(r,s|σ)|s=0, we can write Eq. 3.19 as

D=(Θff+Θwf)Pfeq/(πa2)+(Θfw+Θww)vwPweq, (3.26)

where

Θff=(2π)20a0au^f(r2|r1)vf(r2)vf(r1)r2r1dr2dr1, (3.27)
Θwf=2πvw0aU^w(r)vf(r)rdr, (3.28)
Θfw=2π0au^f(r|w)vf(r)rdr, (3.29)
Θww=vwU^w(w). (3.30)

These four constants correspond to particular sets of realizations of the particle trajectory that is reflected in their indices. Terms Θff and Θwf are due to realizations that start in the flow and end in the flow (Θff) or on the wall (Θwf) at time t. Analogously, terms Θfw and Θww take into account those realizations in which the particle is initially on the wall and is still on the wall (Θww) or in the flow (Θfw) at the time t.

Explicit expressions for the four constants, in terms of the geometrical and kinetic parameters of the system are (see derivations in the Appendixes):

Θff=πa2v¯f2kwPfeq2K+kwa248Dr(1+6K+11K2), (3.31)
Θwf=πa2vwv¯fkwPfeq2κa12Dr+1+κa3DrK, (3.32)
Θfw=v¯fkwPfeq21+κa3Dr+kwa224Dr, (3.33)
Θww=vwkwPfeq21+κa4Dr. (3.34)

Substituting these expressions into Eq. 3.26 we arrive at △D in Eq. 1.11. Thus, we have derived the formula for the effective diffusivity given by Eqs. 1.7, 1.11, starting from the definition in Eq. 3.1.

CONCLUDING REMARKS

Main results of the present paper are the expressions for the effective velocity, Eq. 1.9, and diffusivity, Eqs. 1.7, 1.11, derived in Secs. 2, 3, respectively. The expressions show how these quantities depend on the parameters of the model, v¯f,vw, Df, Dr, Dw, κ, kw, and a. In this section, we briefly discuss the dependence of the effective diffusivity on the velocities v¯f and vw, as well its dependence on the equilibrium constant K = 2κ/(akw), Eq. 1.4. It is worth mentioning that the non-monotonic dependence of Deff on K has been reported earlier.1, 5, 20, 27, 33, 34

The velocity dependence of the effective diffusivity is completely determined by the term △D, Eq. 1.11, which is a quadratic form in v¯f and vw. One can see that △D (and hence Deff) being considered as function of vw at a given value of v¯f has a minimum at some vw=vw*, which is proportional to v¯f, i.e., vw*=Av¯f, where the pre-factor A is a function of Dr, κ, kw and a. As Dr → ∞, Eq. 1.11 reduces to Eq. 1.10, so that vw* tends to v¯f, and A approaches unity.

Next we consider the Deff dependence on K at fixed values of all other parameters, assuming that diffusion in the flow is isotropic, i.e., Dr = Df. As K increases from zero to infinity, Deff changes from Deff(0) given by the Taylor formula, Eq. 1.2, to Deff(∞) = Dw. It can be seen that the large-K asymptotic behavior of Deff is given by

Deff(K)Dw+BK,K, (4.1)

where B=Df+[a2/(48Df)](11v¯f24v¯fvw+6vw2). Since B > 0, Deff(K) always approaches its asymptotic value Dw from above. As K tends to zero, Deff takes the form

Deff(K)Df+a2v¯f248Df+QK,K0, (4.2)

where

Q=DwDf+1kw(v¯fvw)2+a248Dfv¯f(3v¯f4vw). (4.3)

One can see that Q can be both positive and negative. Therefore, Deff(K) may both increase and decrease with K at small K.

Now we employ the asymptotic expressions, Eqs. 4.1, 4.2, to discuss the K-dependence of the effective diffusivity over the entire range of K. When Q > 0, Deff increases with K at small K, reaches a maximum and then decreases approaching the limiting value Deff(∞) = Dw from above. If Q < 0 and Deff initially decreases, the behavior of Deff can be qualitative different depending on whether Deff(0) is smaller or lager than Deff(∞). If Deff(0) < Deff(∞), Deff(K) first decreases, reaches a minimum, then increases and reaches a maximum, and then it decreases again finally approaching its limiting value Dw from above. When the opposite inequality holds, i.e., Deff(0) > Deff(∞), in addition to the “wavy” profile of Deff(K) discussed above (decrease-increase-decrease), the effective diffusivity can be a monotonically decreasing function of K.

To summarize, the effective diffusivity is a complex function of the model parameters. Therefore, its profiles in the multidimensional parameter space may have very different shapes, as can be seen from the above discussion.

ACKNOWLEDGMENTS

This study was supported by the Intramural Research Program of the National of Institutes of Health (NIH), Center for Information Technology. We are grateful to Vemuri Balakotaiah and Chiu-On Ng for helpful discussions. We thank Chris Woodruff for his careful reading of the paper and useful comments.

APPENDIX A: EVALUATION OF CONSTANTS Θfw, Θww FROM EQS. 3.29, 3.30

Consider a particle that is bound to the wall at t = 0. According to Eqs. 3.20, 3.21, 3.22, functions Uw(t|w), uf(r, t|w), Eqs. 3.24, 3.25, satisfy

uft=Drrrrufr,ufrr=0=0, (A1)
dUwdt=2πaκufr=akwUw=2πaDrufrr=a, (A2)

with the initial conditions

Uw(0|w)=Pfeq,uf(r,0|w)=Pfeq/(πa2), (A3)

and an additional relationship

Uw(t|w)+2π0auf(r,t|w)rdr=0, (A4)

which follows from Eq. 3.15.

Laplace transforming Eqs. A1, A2, A3, A4, we arrive at

su^f+1πa2Pfeq=Drrddrrdu^fdr,du^fdrr=0=0, (A5)
sU^wPfeq=2πaκu^fr=akwU^w=2πaDru^frr=a, (A6)
U^w(s|w)+2π0au^f(r,s|w)rdr=0, (A7)

where U^w(s|w) and u^f(r,s|w) are the Laplace transforms of Uw(t|w) and uf(r, t|w), respectively.

Solving these equations at s = 0, we find that

U^w(w)=1kwPfeq21+κa4Dr, (A8)
u^f(r|w)=1πa2kwPfeq21+κa2Dr+kwa28Dr+r24πa2DrPfeq. (A9)

Substituting the solution for u^f(r|w) into Eq. 3.29 and carrying out the integration, we obtain the expression for Θfw in Eq. 3.33.

The term Θww, Eq. 3.34, is simply the product of vw and the solution for U^w(w) in Eq. A8.

APPENDIX B: EVALUATION OF CONSTANTS Θwf, Θff FROM EQS. 3.27, 3.28

For the evaluation of Θff and Θwf consider the particle in the flow that at t = 0 is separated by distance r0, 0 ⩽ r0 < a from the tube axis. As follows from Eqs. 3.20, 3.21, 3.23 functions Uw(t|r0) and uf(r, t|r0), Eqs. 3.24, 3.25, satisfy Eqs. A1, A2 with the initial conditions

Uw(0|r0)=Pweq,uf(r,0|r0)=12πrδ(rr0)1πa2Pfeq, (B1)

and an additional relationship

Uw(t|r0)+2π0auf(r,t|r0)rdr=0, (B2)

which follows from Eq. 3.15.

Functions U^w(r0) and u^f(r|r0) entering into Eqs. 3.27, 3.28 are evaluated from the Laplace transforms of Eqs. A1, A2, B2 at s = 0. They obey the following system of equations:

Drrddrrdu^f(r|r0)dr=1πa2Pfeq12πrδ(rr0),du^f(r|r0)drr=0=0, (B3)
Pweq=2πaκu^f(r|r0)r=akwU^w(r0)=2πaDrdu^f(r|r0)drr=a, (B4)
U^w(r0)+2π0au^f(r|r0)rdr=0. (B5)

In order to simplify calculations, it is convenient to introduce new auxiliary functions

W=2π0aU^w(r0)vf(r0)r0dr0, (B6)
w(r)=2π0au^f(r|r0)vf(r0)r0dr0. (B7)

As follows from Eqs. B3 to B5, W and w(r) satisfy

Drrddrrdwdr=v¯fPfeqvf(r),dwdrr=0=0, (B8)
πa2v¯fPweq=kwW2πκw(a)=2πaDrdwdrr=a, (B9)
W+2π0aw(r)rdr=0. (B10)

Solving Eqs. B8, B9, B10, we obtain

W=πa2v¯fkwPfeq2κa12Dr+1+κa3DrK, (B11)
w(r)=w(0)+v¯f8a2Drr42Pfeq(1+2K)a2r2, (B12)
w(0)=v¯fkwPfeq2kwa212Dr+2κa3Dr+1+3κa4DrK. (B13)

We can write Θff, Eq. 3.27, in terms of w(r),

Θff=(2π)20a0avf(r1)u^f(r|r0)vf(r2)r2dr1dr2=2π0avf(r)w(r)rdr. (B14)

Finally, using Eqs. B12, B13 and performing the integration we arrive at the expression in Eq. 3.31.

The constant Θwf, Eq. 3.33, is simply the product of vw and the solution for W in Eq. B11.

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