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