18.5 Entrance Effects in Hagen-Poiseuille Flow

18.5.1 Introduction

Until now we have worked with the equations for time-dependent flow phenomena. We will now turn to effects which are mathematically very similar, yet of a different physical nature. We will assume a fluidic system as depicted in Fig. 18.10. A fluid is driven by a pressure drop dpdzsi67_e from a reservoir. Depending on the shape of the container, a stable velocity profile will have developed. We will assume this velocity to be constant vav. The fluid is driven into the capillary by the pressure drop. Initially the fluid will have a constant velocity profile which will gradually converge to the Hagen-Poiseuille flow profile given by Eq. 16.36 as

f18-10-9781455731411
Fig. 18.10 Entrance flow at a circular cross-section showing the development of the characteristic Hagen-Poiseuille flow profile which is obtained after a characteristic length zchar.

vr=2vav1rR2

si101_e  (Eq. 18.63)

The flow in the regime of conversion from the constant velocity profile to the fully-developed steady-state profile is referred to as entrance flow. Over a certain length zchar the profile slowly changes until it is stabilized to the steady-state profile.

This is another example of a transient and steady-state problem. Here the transient state is not timedependent, but length-dependent on z. We therefore expect a solution in the form of

vzrz=vz,steadystater+vz,transientrz

si102_e  (Eq. 18.64)

In the following, we will derive the fluid mechanics of the transient flow for the Hagen-Poiseuille flow. As you will see, the method of solving these problems is identical to the method of solving time-dependent transient problems.

Continuity. As you can see, we have chosen the velocity vav because it allows us to satisfy the continuity, i.e., the amount of fluid transported by the constant velocity profile is identical to the amount of fluid transported by the parabolic flow profile. This is how we initially derived vav (see section 16.3.4).

18.5.2 Navier-Stokes Equation for the Entrance Flow

18.5.2.1 Derivation

General Version of the Navier-Stokes Equation. The first thing we need is the modified Navier-Stokes equation. We neglect changes with respect to time, as the entrance effects are not time-dependent, but only dependent on z, which is why we can set vt=0si103_e. The flow is again driven by a pressure along the z-axis and there are no volume forces involved. Taken together, these assumptions will simplify Eq. 11.40 to

ρv·v=dpdz+ηΔv

si104_e  (Eq. 18.65)

Eq. 18.65 is the Navier-Stokes equation that we need to solve. It is in general form, i.e., it can also be applied for systems which are not radially symmetric.

Neglecting the Convection Term.Eq. 18.65 is still a rather complex equation and we would have a hard time finding a general solution to it. We will therefore make another assumption that is in line with the assumption made for Poiseuille flow. We will consider only flows at a very low Reynolds number Re, i.e., we neglect momentum transport by convection. In most microfluidic systems, this is a valid assumption and it will make our problem significantly easier to solve. For low Reynolds numbers we can drop the entire left side of Eq. 18.65 and are left with

0=dpdz+ηΔvηΔv=dpdz

si105_e  (Eq. 18.66)

This equation should look familiar - it is the fundamental equation for pressure-driven Poiseuille flow (see Eq. 15.14) when neglecting effects of the volume forces.

Cylindrical Coordinates. We now convert Eq. 18.66 into cylindrical coordinates. For this we need the Laplace (see Eq. 7.99) operator in cylindrical coordinates that once applied to Eq. 18.66, results in the following equation

ηrrrvr+1r22vφ2+2vz2=dpdz

si109_e  (Eq. 18.67)

Please note that we have used the scalar Laplacian as we have converted the velocity vector vsi107_e to the scalar vz, because there is no flow in radial and azimuthal direction, thus vφ = vr = 0. This reduces the vector notation to a single equation of vz. There are no changes of vz in azimuthal direction, but now we need to consider changes along the z-axis. This is in contrast to the fully developed Hagen-Poiseuille flow which we derived in section 16.3 where we assumed a fully developed flow profile and thus neglected changes along the z-axis, i.e., vxz=0si108_e. See section 16.3.2 for details on this assumption. Taking together we simplify Eq. 18.67 to

ηrrrvzr+1r22vzφ2+2vzx2=dpdzηrrrvzr+2vzz2=dpdz

si106_e  (Eq. 18.68)

Eq. 18.68 is as far as we can go with the simplifications. This is the equation that we will need to solve.

18.5.2.2 Transient and Steady-State Solution

We now apply our solution consisting of a steady state and transient solution as given by Eq. 18.64 to Eq. 18.68. In doing so we find

ηrrrvz,steadystate+vz,transientr+2vz,steadystate+vz,transientz2=dpdzηrrrvz,steadystater+rvz,transientr+2vz,steadystatez2+2vz,transientz2=dpdz

si110_e  (Eq. 18.69)

At this point we note that the steady-state solution is not a function of z therefore 2vz,steadystatez2=0si111_e. Furthermore we already know the steady-state solution to the Poiseuille flow that we derived in section 16.3 and that is given by Eq. 18.63. For Eq. 18.69 we need the derivative with respect to the radius that is given by

vz,steadystater=4vavrR2

si112_e

We therefore rewrite Eq. 18.69 to

ηrrvz,steadystater+rvz,transientr+2vz,transientz2=dpdzηr4vavr2R2r+rvz,transientr+2vz,transientz2=dpdzηr8vavrR2+rvz,transientr+2vz,transientz2=dpdz8ηvavR2+ηrrvz,transientr+2vz,transientz2=dpdz

si113_e  (Eq. 18.70)

From Eq. 16.34 we know that

vav=R28ηdpdz

si114_e

which simplifies Eq. 18.70

8ηR2R28ηdpdz+ηrrvz,transientr+2vz,transientz2=dpdz1rrvz,transientr+2vz,transientz2=01rvz,transientr+r2vz,transientr2+2vz,transientz2=0

si115_e  (Eq. 18.71)

where we now, once again, have a homogeneous PDE. Please note that this is expected, as the steady-state solution must satisfy the Navier-Stokes equation (see Eq. 18.65) and this solution is effectively derived from this inhomogeneous PDE. This procedure is identical to the procedure we have taken when deriving the solution to the time-dependent transient problem in section 18.3. We now proceed to solving Eq. 18.71 again with a substitution and separation of variables approach.

18.5.3 Substitution and Separation of Variables

18.5.3.1 Approach

For Eq. 18.71 we assume a solution of the form

vz,transientrz=ArZz

si116_e

which after inserting into Eq. 18.71 yields the following equation

1rZAr+Xr2Ar2+A2Zz2=0η1A1rAr+2Ar2=1Z2Zz2=λ

si117_e

which yields the two ODEs

1A1rdAdr+d2Adr2=λ

si118_e  (Eq. 18.72)

1Zd2Zdz2=λ

si119_e  (Eq. 18.73)

18.5.3.2 Solution for A (r)

The first ODE will look familiar by now if rewritten to

dAdrr+d2Adr2r2=λAr2r2d2Adr2+rdAdr+λr20A=0

si120_e

which is a Bessel differential equation according to Eq. 3.44 with α=λsi49_e and ν = 0 with the solution according to Eq. 3.46

Ar=c0J0λr

si122_e

18.5.3.3 Boundary Conditions

Obviously, we also need to apply the boundary conditions which are given by

AR=c0J0λR=!0λ=λiR2

si123_e

where λi is the ith root of the Bessel function Jν (see section 3.2.4.3). We therefore find the general solution for A (r) by

Ar=iciJ0λirR

si124_e  (Eq. 18.74)

18.5.3.4 Solution for Z (z)

The general solution for Z (z) from Eq. 18.73 can be simply taken from Tab. 8.2 as

Zz=c1eλiRz+c2eλiRz

si125_e  (Eq. 18.75)

We have one initial condition that will solve for one of the unknowns of Eq. 18.75. The second we can derive by stating that we expect the effects of z on the flow profile to diminish as z increases. This is due to the fact that the flow profile will eventually become fully-developed and thus independent of z. As for z → ∞ the first term of Eq. 18.75 will become large and we know that c1=!0si126_e in order for the solution to be physically meaningful.

18.5.3.5 General Solution

We now have our general solution given by

vz,transientrz=ArZz=iciJ0λirReλiRz

si127_e  (Eq. 18.76)

for which we obviously still have to determine the missing constants ci. These we can derive by the initial conditions.

18.5.3.6 Applying Initial Conditions

We know that for z = 0 the overall velocity profile must be equal to the constant vav. Therefore

vzr0=vz,steadystater+vz,transientr0=2vav1rR2+iciJ0λirReλiR0=2vav1rR2+iciJ0λirR=!vav

si128_e  (Eq. 18.77)

from which we derive

iciJ0λirR=vav2rR21

si129_e  (Eq. 18.78)

We now have to compare coefficients in order to derive ci.

18.5.3.7 Fourier-Bessel Series Expansion

In order to find ci we have to perform a Fourier-Bessel series expansions (see section 4.4). We know that the coefficients are determined by Eq. 4.51 as

ci=vav2R2J12λi0RrJ0λirR2rR21dr

si130_e  (Eq. 18.79)

Fortunately we have already derived the two terms of the integral during an introductory example in section 4.4.2.1. Using Eq. 4.58 we can immediately write down the first integral as

20RrJ0λiRrrR2dr=2RλiRJ1λiRR4λiR2J2λiRR

si131_e  (Eq. 18.80)

Using Eq. 4.57 we can write down the integral for the second term as

0RrJ0λiRrdr=RλiRJ1λiRR

si132_e  (Eq. 18.81)

Summing up Eq. 18.80 and Eq. 18.81 we find

0RrJ0λirR2rR21dr=2RλiRJ1λiRR4λiR2J2λiRRRλiRJ1λiRR=RλiRJ1λi4λiR2J2λi

si133_e  (Eq. 18.82)

Here we can apply the recurrence relation for expression the Bessel function of order 2, as Bessel functions of lower order according to Eq. 3.60 from which we find for ν = 1

J2λi=2λiJ1λiJ0λi

si134_e

in which case we can rewrite Eq. 18.82 to

0RrJ0λirR2rR21dr=RλiRJ1λi8λi3R2J1λi2J0λi=R2λi3λiJ1λi28J1λi=R2J1λiλi3λi28

si135_e  (Eq. 18.83)

where we have used the fact that λi are the roots of J0 and thus J0 (λi) = 0. We can now write down the missing coefficients ci according to Eq. 18.79 as

ci=vav2R2J12λiR2λi3λi2J1λi8J1λi=vav2λi3J1λiλi28

si136_e  (Eq. 18.84)

Eq. 18.84 gives us the coefficients we are seeking.

18.5.4 Transient Solution and Overall Solution

Combining Eq. 18.84 and Eq. 18.76 gives us the transient solution as

vz,transientrz=vavi2λi3J1λiλi28J0λirReλiRz

si137_e  (Eq. 18.85)

Combining Eq. 18.65, Eq. 18.63, and Eq. 18.85 gives us the overall solution of the velocity profile of the transient Hagen-Poiseuille entry profile as

vzrz=vz,steadystater+vz,transientrz=vav21rR2+i2λi3J1λiλi28J0λirReλixR

si138_e  (Eq. 18.86)

Visualization.Fig. 18.11 visualizes Eq. 18.86 as the normalized velocity profile for different values of z. As you can see, for z = 0 the profile starts out as a constant velocity profile with values vav and gradually evolves into the parabolic profile known from Hagen-Poiseuille flow. For zR>10si1_e there is no change in the profile anymore and the velocity profile can be considered as being fully-developed. Therefore we can assume that a fully developed profile will be obtained for zR>10si1_e.

f18-11-9781455731411
Fig. 18.11 Normalized velocity profiles of the Hagen-Poiseuille entrance flow in a system with very low Reynolds numbers Re. As you can see, the profile starts from the constant velocity profile and gradually develops into the parabolic profile known from Hagen-Poiseuille flow. After a relative length along the z-axis of zR>10si1_e there is no more change in the profile and a fully-developed profile is obtained.

18.5.5 Interpretation

As stated initially, we have made one major simplification during the derivation of Eq. 18.86: We assumed the Reynolds number to be so small that we could neglect all momentum flow due to convection. Obviously, this is only true for a microfluidic system at very low flow speeds. Obviously, we are interested in the question if our solution can also be used for predicting the entrance flow in systems with higher Reynolds number. Referring to Eq. 18.65, we would retain the term on the left-hand side of the equation when taking into account momentum transport by convection. If this term remains in the equation, momentum is transported into and out of our control volume via convection. This in turn will make the momentum diffusion less relevant as it operates on longer time scales. This will significantly reduce the speed at which the steady-state profile evolves. This in turn will increase the characteristic length zchar after which the stable steady-state solution is found. This means that our assumption is a rather optimistic one. In systems with higher Reynolds numbers, the profile will develop significantly after a distance zR>10si1_e. In section 33.3 we will use a numerical scheme to directly compare the influence of momentum convection on the length and time scales it takes a flow profile to fully establish.

Qualitative Estimation. As stated, evaluating Eq. 18.65 with the convection analytically is very challenging. Therefore one usually defaults to either using experimental data or numerical evaluation in order to find a quantitative correlation between the Reynolds number and zchar. There are several commonly used equations for estimating zchar, one of the most commonly used ones being

zchar=zRRe60

si142_e

Please note that this equation is empirical - it is derived from experimental data in which zchar is determined for flow fields with different Reynolds numbers thus establishing a correlation.

18.5.6 Other Cross-Sections

The derivation of the transient velocity profile during entrance flow was derived for a circular cross-section and thus based on the Hagen-Poiseuille flow. Obviously, the mathematics is identical for other cross-sections. In this case, Eq. 18.66 will serve as a basis which will, after inserting the combined steady-state and transient solution, yield a PDE just as it did for all transient/steady-state problems we discussed in this section. Solving this PDE for a given initial condition will result in the velocity profiles sought.

18.6 Summary

In this section we have studied time- and space-dependent effects during accelerating and deceleration of fluids, as well as during entrance flow. As we have seen, the time-dependent equations can be derived from the modified Navier-Stokes equation, taking into account the time-dependent term on the left-hand side, whereas the spacedependent equations can be derived from the modified Navier-Stokes equation, taking into account the changes along the x-axis. In all cases, we assumed the solution to the velocity distribution to consist of a time- or spacedependent transient solution and the time- or space-independent steady-state solution. The latter we have already derived while studying steady-state fluid flows in section 15. In all cases, we ended up with a homogeneous PDE which we solved by a substitution and separation of variables approach.

For the time-dependent transient solution, we then found a time-independent steady-state term and a time-dependent exponential term which reflects the time-dependency of the flow profiles. For the space-dependent transient solutions, we found a space-independent steady-state term and a space-dependent transient term, which reflects the space-dependency of the flow profile. For the time-dependent transient solutions, we found that the profiles can be scaled to a characteristic timescale which depends, as we expected initially, on the momentum diffusion properties of the fluid and on the length scale of the system. For the space-dependent transient solutions, we found a term which was purely dependent on the variable x. In all cases, we were able to derive dimensionless flow profiles from which we derived realistic flow profiles for chosen sets of geometric parameters.

As you can see, transient problems occur regularly in fluid mechanics, but they are not complicated to solve and the methods of solving these equations is always the same. It may be conveniently extended to other profiles and cross-sections that we did not study in this section, e.g., the planar infinitesimally extended channel.

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