Biomedical Engineering Reference
In-Depth Information
(
PA
P
A
)(
+
τ
A
τ
A
) 0
=
xx
x xx
+∆
rr
r rr
+∆
(2
P
π
r dr
P
2 )(2
π τπ τ π
r dr
+
r dx
2 )0
r dx
=
x
xx
+∆
r
rr
+∆
Cancelling out and grouping the x -terms and r -terms gives
(
PP
)(
τ
r
τ
) 0
r
x
xx
+∆
r
rr
+∆
r
+
=
dx
dr
Taking the limits as dx and
dr
0
dP
d
() 0
τ
r
r
+
=
dx
dr
Substituting Newton's law of viscosity formula (
τ µ
=−
/)
du dy
we get
dP
µ
d
du
=
r
dx
r dr
dr
which is rewritten as
2
dP
d u
µ
du
(4.9)
=
µ
+
2
dx
r dr
dr
This is the general equation for a steady laminar incompressible pipe flow in the
fully developed region. Its general solution is
1
dP
2
u r
()
=
r
+
Aln r
()
+
B
(4.10)
4
µ
dx
To obtain the velocity profile we define the boundary conditions which are:
I. At the centre of the pipe r = 0, u = U max which means A must be equal to zero for
the equation to balance.
II. Combining the above condition with the wall boundary condition of r = R (  R is the
distance from pipe centre to pipe wall), u = 0 means that
2
r
ur
()
=
U
1
(4.11)
max
2
R
 
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