Biomedical Engineering Reference
In-Depth Information
"
p
2C
0
2
#
d
x
Z
1
C
2
2
k
B
T
b
k
a
1
f
mb
D
C
M
1
.A./
A..t
0
///
2
C
M
2
.V./
V..t
0
///
2
:
(58)
This will be the free energy density used in our cell model.
We denote
v
as the velocity of the mixture, and p the hydrostatic pressure. We
denote by
1
the mass density of the fluid outside the membrane and inside the core
and by
2
the mass density of the mixture in the cytoplasm. We assume the material
is incompressible in both domains, i.e.,
1
and
2
are constants. The density of the
mixture is defined as
1
2
.1
/
C
2
2
.1
C
/:
D
(59)
From mass conservation, we have
2
1
1
C
2
d
dt
:
r
v
D
(60)
This is true when
d
dt
C
r
1
:
v
D
(61)
d
dt
D
@
@t
C
Here,
r
is the material derivative and is the chemical potential of
the material system.
If we use
v
d
dt
D
1
(62)
to transport , the continuity equation should be
2
1
d
dt
:
r
D
v
(63)
The balance of linear momentum is governed by
d
v
dt
Dr
.
p
I
C
/
C
F
e
;
D
1
C
2
;
(64)
where
1
is the stress tensor for the fluid outside the membrane and inside the core,
2
is the stress tensor inside the cytoplasmic region, and
F
e
is the external force
exerted on the complex fluid.
Search WWH ::
Custom Search