creeping flows
DESCRIPTION
Creeping Flows. Steven A. Jones BIEN 501 Wednesday, March 21, 2007 Start on Slide 53. Creeping Flows. Major Learning Objectives: Compare viscous flows to nonviscous flows. Derive the complete solution for creeping flow around a sphere (Stokes’ flow). - PowerPoint PPT PresentationTRANSCRIPT
Louisiana Tech UniversityRuston, LA 71272
Slide 1
Creeping Flows
Steven A. Jones
BIEN 501
Wednesday, March 21, 2007
Start on Slide 53
Louisiana Tech UniversityRuston, LA 71272
Slide 2
Creeping Flows
Major Learning Objectives:
1. Compare viscous flows to nonviscous flows.
2. Derive the complete solution for creeping flow around a sphere (Stokes’ flow).
3. Relate the solution to the force on the sphere.
Louisiana Tech UniversityRuston, LA 71272
Slide 3
Creeping Flows
Minor Learning Objectives:1. Examine qualitative inertial and viscous effects.2. Show how symmetry simplifies the equations.3. Show how creeping and nonviscous flows
simplify the momentum equations.4. Give the origin of the Reynolds number.5. Use the Reynolds number to distinguish
creeping and nonviscous flows.6. Apply non-slip boundary conditions at a wall
and incident flow boundary conditions at .
Louisiana Tech UniversityRuston, LA 71272
Slide 4
Creeping Flows
Minor Learning Objectives (continued):7. Use the equations for conservation of mass and
conservation of momentum in spherical coordinates.8. Use the stream function to satisfy continuity.9. Eliminate the pressure term the momentum
equations by (a) taking the curl and (b) using a sort of Gaussian elimination.
10. Rewrite the momentum equations in terms of the stream function.
11. Rewrite the boundary conditions in terms of the stream function.
12. Deduce information about the form of the solution from the boundary conditions.
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Slide 5
Important Concepts
• Flow Rate
• Cross-sectional average velocity
• Shear Stress (wall shear stress)
• Force caused by shear stress (drag)
• Pressure loss
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Slide 6
Creeping Flows
Minor Learning Objectives (continued):13. Discuss the relationship between boundary conditions
and the assumption of separability.14. Reduce the partial differential equation to an ordinary
differential equation, based on the assumed shape of the solution.
15. Recognize and solve the equidimensional equation.16. Translate the solution for the stream function into the
solution for the velocity components..17. Obtain the pressure from the velocity components.18. Obtain the drag on the sphere from the stress
components (viscous and pressure).
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Slide 7
Creeping vs. Nonviscous Flows
Nonviscous Flows
Viscosity goes to zero (High Reynolds Number)
Left hand side of the momentum equation is important.
Right hand side of the momentum equation includes pressure only.
Inertia is more important than friction.
Creeping Flows
Viscosity goes to (Low Reynolds Number)
Left hand side of the momentum equation is not important.
Left hand side of the momentum equation is zero.
Friction is more important than inertia.
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Slide 8
Creeping vs. Nonviscous FlowsNonviscous Flow Solutions
Use flow potential, complex numbers.
Use “no normal velocity.”
Use velocity potential for conservation of mass.
Creeping Flow Solutions
Use the partial differential equations. Apply transform, similarity, or separation of variables solution.
Use no-slip condition.
Use stream functions for conservation of mass.
In both cases, we will assume incompressible flow.
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Slide 9
Flow around a Sphere
Nonviscous FlowCreeping Flow
Larger velocity near the sphere is an inertial effect.
Velocity
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Slide 10
Flow around a Sphere
A more general case
Increased velocity as a result of inertia terms.
Incident velocity is approached far from the sphere.
Shear region near the sphere caused by viscosity and no-slip.
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Slide 11
Stokes Flow: The Geometry
3ev v
r
Use Standard Spherical Coordinates, (r, , and )
Far from the sphere (large r) the velocity is uniform in the rightward direction. e3 is the
Cartesian (rectangular) unit vector. It does not correspond to the spherical unit vectors.
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Slide 12
The Objective
1. Obtain the velocity field around the sphere.
2. Use this velocity field to determine pressure and drag at the sphere surface.
3. From the pressure and drag, determine the force on the sphere as a function of the sphere’s velocity, or equivalently the sphere’s velocity as a function of the applied force (e.g. gravity, centrifuge, electric field).
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Slide 13
Some Applications
1. What electric field is required to move a charged particle in electrophoresis?
2. What g force is required to centrifuge cells in a given amount of time.
3. What is the effect of gravity on the movement of a monocyte in blood?
4. How does sedimentation vary with the size of the sediment particles?
5. How rapidly do enzyme-coated beads move in a bioreactor?
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Slide 14
Symmetry of the Geometry
The flow will be symmetric with respect to .
r
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Slide 15
Components of the Incident Flow
3ev v
r
cosv
Incident Velocity
Component of incident velocity in the radial direction,
sinvComponent of incident velocity in the - direction,
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Slide 17
Creeping Momentum Equation
To see how creeping flow simplifies the momentum equation, begin with the equation in the following form (Assume a Newtonian fluid):
For small v, 2nd term on the left is small. It is on the order of v2. (v appears in the right hand term, but only as a first power).
Dv
2P
t
Dvvv
2P
t
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Slide 18
Convective Term in Spherical Coordinates
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Slide 19
Reynolds Number
The Reynolds number describes the relative importance of the inertial terms to the viscous terms and can be deduced from a simple dimensional argument.
dominant.aretermswhichdetermines
thatalone,velocityorthanratherratio,thisisItor
,isratioThe)termtypicalaofthinktohelp
may(Itlikegoeslength. sticcharacteri a is and
velocity sticcharacteri a iswhere,likegoes
.
.
.V
2
2
2
2
2
2
VL
L
V
L
V
x
v
LL
VL
V
D
vv
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Slide 20
Reynolds Number
VLVL
ReRe or
Different notations are used to express the Reynolds number. The most typical of these are Re or Nr.
Also, viscosity may be expressed as kinematic ( ) or dynamic () viscosity, so the Reynolds number may be
In the case of creeping flow around a sphere, we use v for the characteristic velocity, and we use the sphere diameter as the characteristic length scale. Thus,
DuRe
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Slide 22
Boundary Conditions (B.C.s) for Creeping Flow around a Sphere
rv
Rr
for
for
3
0
ev
v
There is symmetry about the -axis. Thus (a) nothing depends on , and (b) there is no - velocity.
0
,
,
v
rvv
rvv rr
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Slide 23
Summary of Equations to be Solved
0 v
0sin
1sin
sin
11 22
vr
vr
vrrr r
We must solve conservation of mass and conservation of momentum, subject to the specified boundary conditions.
Conservation of mass in spherical coordinates is:
Which takes the following form in spherical coordinates (Table 3.1):
0&00sinsin
11 22
vv
rvr
rr r WhenOr
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Slide 24
Summary of Equations (Momentum)
0sin
1
0cot222
22
222
r
vvv
p
r
vr
v
rv
rv
r
p
r
rr
H
H
sinsin
11 22 rr
rrr
HWhere
Because there is symmetry in , we only worry about the radial and circumferential components of momentum.
Which takes the following form in spherical coordinates (Table 3.4):
0P τ (Incompressible, Newtonian Fluid)
Radial
Azimuthal
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Slide 25
Simplified Differential Equations
22 2 2
1 1 1sin 0
sin sinrv v vvp
rr r r r r r
Yikes! You mean we need to solve these three partial differential equations!!?
Conservation of Radial Momentum
Conservation of Azimuthal Momentum
22 2 2 2
1 1 2 2 2sin cot 0
sinr r
r
vv vpr v v
r r r r r r r r
22
1 1sin 0
sinrr v vr r r
Conservation of Mass
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Slide 26
Comments
22 2 2
1 1 1sin 0
sin sinrv v vvp
rr r r r r r
Three equations, one first order, two second order.
Three unknowns ( ).
Two independent variables ( ).
Equations are linear (there is a solution).
22 2 2 2
1 1 2 2 2sin cot 0
sinr r
r
vv vpr v v
r r r r r r r r
22
1 1sin 0
sinrr v vr r r
, andrv v P
andr
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Slide 27
Stream Function Approach
We will use a stream function approach to solve these equations.
The stream function is a differential form that automatically solves the conservation of mass equation and reduces the problem from one with 3 variables to one with two variables.
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Slide 28
Stream Function (Cartesian)
Cartesian coordinates, the two-dimensional continuity equation is:
0u v
x y
If we define a stream function, , such that:
, ,, 0
x y x yu v
y x
Then the two-dimensional continuity equation becomes:
2 2
0u v
x y x y y y x y y x
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Slide 29
Summary of the Procedure
1. Use a stream function to satisfy conservation of mass.
a. Form of is known for spherical coordinates.
b. Gives 2 equations (r and momentum) and 2 unknowns ( and pressure).
c. Need to write B.C.s in terms of the stream function.
2. Obtain the momentum equation in terms of velocity.
3. Rewrite the momentum equation in terms of .
4. Eliminate pressure from the two equations (gives 1 equation (momentum) and 1 unknown, namely ).
5. Use B.C.s to deduce a form for (equivalently, assume a separable solution).
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Slide 30
Procedure (Continued)
6. Substitute the assumed form for back into the momentum equation to obtain an ordinary differential equation.
7. Solve the equation for the radial dependence of .
8. Insert the radial dependence back into the form for to obtain the complete expression for .
9. Use the definition of the stream function to obtain the radial and tangential velocity components from .
10. Use the radial and tangential velocity components in the momentum equation (written in terms of velocities, not in terms of ) to obtain pressure.
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Slide 31
Procedure (Continued)
11. Integrate the e3 component of both types of forces (pressure and viscous stresses) over the surface of the sphere to obtain the drag force on the sphere.
Louisiana Tech UniversityRuston, LA 71272
Slide 32
Stream Function
Recall the following form for conservation of mass:
rrv
rvr
sin
1,
sin
12
If we define a function (r,) as:
then the equation of continuity is automatically satisfied. We have combined 2 unknowns into 1 and eliminated 1 equation.
Note that other forms work for rectangular and cylindrical coordinates.
0sinsin
11 22
vr
vrrr r Slide 22
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Slide 33
Exercise
With:
rrv
rvr
sin
1,
sin
12
0sinsin
11 22
vr
vrrr r
Rewrite the first term in terms of .
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Slide 34
Exercise
With:
rrv
rvr
sin
1,
sin
12
0sinsin
11 22
vr
vrrr r
Rewrite the second term in terms of .
Louisiana Tech UniversityRuston, LA 71272
Slide 35
Momentum Eq. in Terms of
Userr
vr
vr
sin
1,
sin
12
Substitute these expressions into the steady flow momentum equation (Slide 23) to obtain a partial differential equation for from the momentum equation (procedure step 2):
0sin
1sin2
22
2
rr
and conservation of mass is satisfied (procedure step 1).
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Slide 36
Elimination of Pressure
0 vp
The final equation on the last slide required several steps. The first was the elimination of pressure in the momentum equations. The second was substitution of the form for the stream function into the result. The details will not be shown here, but we will show how pressure can be eliminated from the momentum equations. We have:
We take the curl of this equation to obtain:
v p
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Slide 37
Elimination of Pressure
But it is known that the curl of the gradient of any scalar field is zero (Exercise A.9.1-1). In rectangular coordinates:
0eee
eee
312
2
21
2
213
2
31
2
123
2
32
2
321
321
321
xx
p
xx
p
xx
p
xx
p
xx
p
xx
p
x
p
x
p
x
pxxx
p
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Slide 38
Elimination of Pressure
ikj
ijk
kkk
k
ij
kijk
x
p
xp
x
pp
x
pp
x
v
e
e
ev
,
Alternatively:
So, for example, the e1 component is:
012332
123
13232
12311
e
ee
x
p
xx
p
x
x
p
xx
p
xx
p
x kjjk
Louisiana Tech UniversityRuston, LA 71272
Slide 39
Exercise: Elimination of Pressure
One can think of the elimination of pressure as being equivalent to doing a Gaussian elimination type of operation on the pressure term.
This view can be easily illustrated in rectangular coordinates:
2 2
2 2
2 2
2 2
0 momentum
0 momentum
Take of the first equation and of the second and subtract.
x x
y y
v vpx
x x y
v vpy
y x y
y x
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Slide 40
Elimination of Pressure
momentum
momentum
yyx
v
x
v
yx
p
xy
v
xy
v
xy
p
yy
xx
2
3
3
32
3
3
2
32
0
0
2
3
3
3
3
3
2
3
0yx
v
x
v
y
v
xy
v yyxx
This view can be easily illustrated in rectangular coordinates:
23
3
2
3
2
3
3
3
0.,. Ex
v
yx
v
xy
v
y
vei yyxx
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Slide 41
Exercise: 4th order equation
With:
3 33 3
3 2 2 30y yx x
v vv v
y y x x y x
What is the momentum equation:
, ,, 0x y
x y x yv v
y x
in terms of ?
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Slide 42
Exercise: 4th order equation
Answer:
4 4 4 4
4 2 2 2 2 40
y y x x y x
or
22 2
2 20
y x
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Slide 43
Elimination of Pressure
Fortunately, the book has already done all of this work for us, and has provided the momentum equation in terms of the stream function in spherical coordinates (Table 2.4.2-1). For v=0:
4
2
22
22 sin
1cos
sin
2
,
,
sin
1E
rrr
E
r
E
rE
t
Admittedly this still looks nasty. However, when we remember that we have already eliminated all of the left-hand terms, the result for the stream function is relatively simple.
Louisiana Tech UniversityRuston, LA 71272
Slide 44
Momentum in terms of
4
2
22
22 sin
1cos
sin
2
,
,
sin
1E
rrr
E
r
E
rE
t
How does this simplify for our problem?
Recall:
Steady state
Low Reynolds number
If:
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Slide 45
Stream Function, Creeping Flow
When the unsteady (left-hand side) terms are eliminated:
.0sin
1sin
.sin
1sin,0
2
22
2224
rr
rrEE
Thus
where
This equation was given on slide 35.
Louisiana Tech UniversityRuston, LA 71272
Slide 46
Boundary Conditions in Terms of
From
0 atrv r R 0 at ,v r R
2
1
sinrvr
1
sinv
r r
and
Exercise: Write these boundary conditions in terms of .
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Slide 47
Boundary Conditions in Terms of
From
Rr at0
Rrr
vr
at0sin
12
andr
must be zero for all at r=R. Thus,
must be constant along the curve r=R. But since it’s constant of integration is arbitrary, we can take it to be zero at that boundary. I.e.
,0sin
1Rr
rrv
at
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Slide 48
QuestionConsider the following curves. Along which of these curves must velocity change with position?
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Slide 49
Comment
does not change as changes.
As r changes, however, we move off of the curve r=R, so can change.
A key to understanding the previous result is that we are talking about the surface of the sphere, where r is fixed.
curve.thatalongconstantbemust
becausesoAndBecause
,
0.0sin
1,0
2
allforr
vr
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Slide 50
Boundary Conditions in Terms of
From
3cos, e vvr rAt
sin,
sin
1 22
rvr
v rr
Thus, in contrast to the surface of the sphere, will change with far from the sphere.
32
32 sincossincos, ee
rvrvr
asThus,
(See Slide 14)
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Slide 51
Boundary Conditions in Terms of
From
rgvr
dvrdrvd rr
22
0 0
2
0
2
sin2
1
sincossin
sin,
sin
1 22
rvr
v rr
which suggests the -dependence of the solution.
2sin vrf
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Slide 52
Comment on Separability
For a separable solution we assume that the functional form of is the product of one factor that depends only on r and another that depends only on .
rr R,
Whenever the boundary conditions can be written in this form, it will be possible to find a solution that can be written in this form. Since the equations are linear, the solution will be unique. Therefore, the final solution must be written in this form.
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Slide 53
Comment on Separability
0, RR R
In our case, the boundary condition at r=R is:
Both of these forms can be written as a function of r multiplied by a function of . (For r=R we take R(r)=0). The conclusion that the dependence like sin2 is reached because these two boundary conditions must hold for all . A similar statement about the r-dependence cannot be reached. I.e. we only know about two distinct r locations.
2 21, sin
2v r
and the boundary condition at r is:
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Slide 54
Separability
0, RR RAgain, at r=R:
2 21, sin
2v r and at r :
For a separable solution, we look for a form:
,R R R
Because the -dependence holds for all , but the r-dependence does not, we must write:
2 21, sin
2r f r v r
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Slide 55
Momentum Equation
The momentum equation:
is 2 equations with 3 unknowns (P, vr and v). We have used the stream function to get 2 equations and 2 unknowns (P and ). We then used these two equations to eliminate P.
D 20 P
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Slide 56
Substitute Back into Momentum
With
0884
432
2
24
4
r
f
dr
df
rdr
fd
rdr
fd
(slide 45) becomes:
2sin vrf
0sin
1sin2
22
2
rr
Note the use of total derivatives.
Louisiana Tech UniversityRuston, LA 71272
Slide 57
Exercise: Substitute
2 2
2 2 2 2
sin 1 sin 10
sin sinr r r r
2sin vrf
into
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Slide 58
Exercise: Substitute
22
2 2
2 22
2 2
22
2 2
22
2 2
22
2
sin 1sin
sin
sin 1 sinsin
sin
sin 2sin cossin
sin
sin cossin 2
sinsin 2
f r vr r
f rv f r
r r
f rv f r
r r
f rv f r
r r
f rv
r
2
2f r
r
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Slide 59
Exercise: So we now need
22 22
2 2 2 2
4 2 222 2
4 2 2 2 2 4
4 22
4 2 2
sin 1 sinsin 2
sin
2sin sin 1 2sinsin sin
sin
sinsin 2sin
f rv f r
r r r r
f r f r f rv f r
r r r r r r
f r f rv
r r r
2
2
4 2 2 22
4 2 2 2 2
2sin cos 2cos
sin sin
sin cossin 2sin 2sin 2 1
sin
f rf r
r
f r f r f rv f r
r r r r
Louisiana Tech UniversityRuston, LA 71272
Slide 60
Substitute Back into Momentum
The student should recognize the differential equation as an equidimensional equation for which:
08842
22
4
44 f
dr
dfr
dr
fdr
dr
fdr
narrf
Substitution of this form back into the equation yields:
0,2
1,
4
3,
4
1 3
42
DvCRvBRvA
DrCrBrr
Arf with
Louisiana Tech UniversityRuston, LA 71272
Slide 61
Equidimensional Equation
The details are like this:
08814321
8814321
0884
12244
2
22
4
44
nnnnnnn
ar
ararnrarnnrarnnnnr
ardr
darr
dr
ardr
dr
ardr
n
nnnn
nnnn
bydivide
This is a 4th order polynomial, i.e. there are 4 possible values for n which happen to turn out to be -1, 1, 2 and 4.
Louisiana Tech UniversityRuston, LA 71272
Slide 62
Solution for Velocity Components
Once the boundary conditions are evaluated, the solution is:
sin4
1
4
31
cos2
1
2
31
3
3
r
R
r
R
v
v
r
R
r
R
v
vr
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Slide 63
Pressure
DP 2
To obtain pressure, we return to the momentum equation:
This form was 2 equations with 3 unknowns, but now vr and v have been determined. Once the forms for these two velocity components are substituted into this equation, one obtains:
23
sin
2
3cos3
rRv
P
rRv
r
P
Integrate to get P.
Louisiana Tech UniversityRuston, LA 71272
Slide 64
Pressure
The result of this exercise is:
20
cos
2
3cos
rRvgrPP
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Slide 65
Force
To obtain force on the sphere, we must remember that force is caused by both the pressure and the viscous stress.
2
0 0
23 sinsincos ddTTRF
Rrrrr
z3 is the direction the sphere is moving relative to the fluid.
Used to get the z3 component.
Louisiana Tech UniversityRuston, LA 71272
Slide 66
Potential Flow
0 v
Potential flow derives from the viscous part of the momentum equation.
vIf we write:
Then the viscous part of the momentum equation will automatically be zero.
Louisiana Tech UniversityRuston, LA 71272
Slide 67
Potential Flow
0 v
The continuity equation:
02
Becomes:
Therefore potential flow reduces to finding solutions to Laplace’s equation.