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8/13/2019 Seminario Redentor
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NUMERICAL SIMULATION OF POWER-LAW
FLUID FLOWS IN A POROUS CHANNEL
Jess Alfonso Puente Angulo ([email protected])
Maria Laura Martins-Costa ([email protected])
Heraldo da Costa Mattos ([email protected])
Laboratory of Theoretical and Applied Mechanics, Mechanical Engineering Graduate Program
Universidade Federal Fluminense
UFF
Presented by: Jess Alfonso Puente Angulo
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1. INTRODUCTION
PROBLEM: Power-law fluid flows in a porous channel limited by two
impermeable flat plates.
MODEL: mixture theory approach fluid saturated porous media
fluid and porous matrix treated as superimposed continuous constituents
of a binary mixture - each of them occupying its whole volume.
NUMERICAL APPROXIMATION: Runge-Kutta method coupled with ashooting strategy.
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1. INTRODUCTION
Time independent fluids
Shear-thinning
or
pseudoplastic
fluid
Bingham Plastic
Shear-
thickening or
dilatant fluid
Newtonian
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1. INTRODUCTION
Mixture Theory
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2. MECHANICAL MODEL
Mass and Momentum Equations
Porous channel
( ) 0F FF F F F F F F F
t t
vv v v T m g
Problem statement
Hypothesis
Rigid porous matrix
Incompressible fluid
Steady state fluid
Impermeable flat plates
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2. MECHANICAL MODEL
Constitutive model
2
2
=
I
I
-p
K
D
D
F
F
F F
F F
T I +D
m v
D
D .D
2
, , ,
I
I
1
DK
with
n K
and
D
F Fm v
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2. MECHANICAL MODEL
Constitutive model
0 0
1 0
K
K
F
F
m
m
1
a
a
b
K
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2. MECHANICAL MODEL
The generalized permeability function Kis then given by
-12 1
2
-12 1
2
4 3 12 1 3 6
or using the definition of
1 4 3 12 1 3 6
n n
n
n nan
a
nK Kn K
K
nK b n K
F
F
v
v
If n=0 then K K
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2. MECHANICAL MODEL
Permeability and Porosity behaviour
Identification of the parameter a
1 1
1 2
0.2, 0.3
1000 and 10000K D K D
Permeability versus porosity
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2. MECHANICAL MODEL
Neglecting gravity effects and considering fully developed steady
state horizontal flow
2
0
2 ( ) 0
0 on
F
nn
F F F F F
F
p
y H
v
I D D D v v
v
Defining
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2. MECHANICAL MODELThe governing equations for the flow are:
Two-point boundary-value problem
Analytical solution for maximum flow velocity
1
2 1
max
1
ndpw
dx
yat0
02
12 22
22
2
Hw
HyHwwdy
wd
dy
dwn
dx
dp nn
n
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2. MECHANICAL MODEL
Dimensionless variables
* * * *
2 1
max max
, , w = , pF nx y w p
x yL H w w
H
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2. MECHANICAL MODEL
Dimensionless expression for porosity and permeability
2 2
12 1
2 2
1
combining some equations and simplifying
63 2 1
1 4 3 1
n
nana
n a a
H
bb n
H n
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3. NUMERICAL PROCEDUREIn order to apply the Runge-Kutta method coupled with a shooting
strategy
Variables redefinition
1 2;dwz w zdy
The boundary value problem is transformed into an equivalent Initial
Value Problem
2 2 222 1 1
1
112
2
02 1
0
n n ndz dpz z zz at y Hdy n dx
withz at y Hdz
zdy
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3. NUMERICAL PROCEDUREThe two-point boundary-value problem is transformed into an equivalent
Initial Value Problem
22 22
2 1 1
1
212
2
02 1 ;
nn ndz dp
z z zz at y Hdy n dx
for H y H such thatz t at y Hdz
zdy
Find the root of a scalar function represented as ,where for a given t, the value of is the value of the variable at
point y = -H. Essentially this procedure is a shooting technique.
2( ) ( ; )t t z y H t ( )t 2z
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Variation of the parameter with the permeability, for distinct power-law
indexes
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4. RESULTSFlow of a power-law fluid through a porous plane channel
First estimative of the derivative for shear-thinning behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Velocity profiles for shear-thinning behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Dimensionless velocity profiles for shear-thinning behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
First estimative of the derivative for shear-thickening behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
First estimative of the derivative for shear-thickening behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Velocity profiles for shear-thickening behavior
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Dimensionless velocity profiles for shear-thickening fluids (n0)
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4. RESULTSFlow of a power-law fluid through a porous plane channel
Behavior of the maximum velocity in a porous channel.
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4. RESULTSFlow of a power-law fluid through a porous plane channel
One-dimensional shear stress versus shear strain
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5. CONCLUSIONS
The proposed model is adequate to study power-law fluid flows for
different values of n.
The fourth-order Runge-Kutta method coupled with a shooting strategy
proved to be suitable to solve this kind of problems.
The fluid constituent velocity is strongly influenced by the shear-
thickening and by the shear stress increase.
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ACKNOWLEDGMENTS