This study centres round the problem of flow of a liquid past a vertical porous flat plate. Considering two cases, when the plate is stationary and when it is in motion, the effect of porosity on the flow has been determined. It is found that, when the plate is stationary, the velocity of the liquid increases with increase in the suction velocity and decreases with increase in the injection velocity, and for a given suction or injection velocity, the velocity of the liquid increases with increase in time and approaches to the steady state case. But, when the plate is in motion, the velocity of the liquid decreases with increase in the suction velocity and increases with increase in the injection velocity in the constant film thickness region and also in the dynamic meniscus region provided that the gravitational force is greater than the surface tension force. In this case, the stagnation point and the minimum pressure point on the free surface have also been determined. In the case of injection there always exists a unique stagnation point and also a minimum pressure point. But in the case of suction the stagnation point does not always exist and there is no minimum pressure point.Nomenclature
A
n
roots of equation (3.18)
-
C
function defined by equation (4.20)
-
C
n
coefficients defined by equation (4.15)
-
F
function of
R
0 and
T
0 defined by equation (4.23)
-
g
acceleration of gravity
-
h
film thickness at any point
-
h
0
film thickness in the constant thickness region
-
h
m
film thickness at the minimum pressure point
-
h
st
film thickness at the stagnation point
-
L
m
location of the minimum pressure point=
h
m
/
h
0
-
L
st
location of the stagnation point=
h
st/
h
0
-
n
summation index
-
N
function defined by equation (4.11)
-
p
pressure
-
q
flow rate
-
q
0
flow rate in the constant thickness region
-
Q
non-dimensional flow rate
-
R
suction or injection Reynolds number=
v
0
h
0/
v
-
R
0
suction or injection Reynolds number corresponding to the constant thickness region=
v
0
h/
-
t
time
-
T
non-dimensional time=
t/
h
2
-
T
0
non-dimensional parallel flow film thickness=
h
0(
g/u
w
)
1/2
-
u
vertical velocity
-
u
perturbation velocity for
u
-
u
s
surface velocity
-
u
W
withdrawal velocity of the plate
-
U
steady part of the velocity
u for the stationary plate
-
non-dimensional velocity=
u/gh
2
-
U*
non-dimensional velocity=
U/gh
2
-
v
horizontal velocity
- v
perturbation velocity for
V
-
v
0
velocity of suction or injection
-
V
transient part of the velocity u for stationary plate
-
x, y
coordinates
-
X
non-dimensional
x-coordinate=
x
2/
gh
4
-
Y
non-dimensional
y-coordinate=
y/h
Greek Symbols
n
roots of equation (3.14)
-
n
eigenvalues defined by equation (4.13)
-
n
functions defined by equation (4.14)
-
n
eigenvalues defined by equation (3.15)
-
n
non-dimensional eigenvalues=
n
h/
-
kinematic viscosity
-
liquid density
-
surface tension of the liquid air interface
-
stream function
-
non-dimensional stream function=
/gh
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