Biomedical Engineering Reference
In-Depth Information
predict the composition profi le in a one sided gradient as well as for semi-
symmetrically graded plate-shaped components [Put et al., 2003]. The prediction
of the concentration profi les are based on the description of the deposition yield
by means of the effective charge of the suspended powder particles,
Q
eff
, the elec-
trophoretic mobility,
μ
, and the specifi c conductivity of the solvent,
σ
liq
. Although
this model predicts the yield during EPD well, the parameters
Q
eff
,
σ
liq
and
μ
are
fi tted parameters rather than real physical values.
If different powders
i
are present in the suspension, the deposition yield of
each powder on the deposition electrode can be described by [Biesheuvel and
Verweij, 1999 ]:
dy
dt
φ
φφ
i
di
=
ES f
μ
c
(10.1)
i
i
i
−
di
si
with
dy
dt
i
, the deposition rate of powder
i
on the electrode (g/s)
E
, the electric fi eld strength (V/m)
μ
i
, the electrophoretic mobility of powder
i
(m
2
/V.s)
c
i
, the concentration
i
of powder
i
in suspension (g/cm
3
)
f
i
, factor for powder
i
which takes in account that not all powder brought to
the electrode is incorporated in the deposit
S
, the surface area of the deposition electrode (m
2
)
φ
di
concentration (vol. %) of the powder in the deposit
φ
si
concentration (vol. %) of the powder in the suspension
The concentration
c
i
,
t
of powder
i
at time
t
is a function of the powder mass in
the suspension and the suspension volume at (
t
−
1) and the change in mass and
volume during
Δ
t
:
t
MM
dy
dt
∫
i
+
Δ
−
dt
it
,
−
1
i
,
Δ
t
c
=
t
−
1
(10.2)
it
,
VV
+
Δ
t
−
1
Δ
t
1) (g)
With
M
i
,
t
− 1
the mass of powder
i
in suspension at time (
t
−
Δ
M
i,
Δ
t
the change in mass of powder
i
by adding or removing suspen-
sions between (
t
1) and
t
(g)
V
t
− 1
the total volume suspension at time (
t
−
−
1) (cm
3
)
Δ
V
Δ
t
change in suspension volume between (
t
−
1) and
t
(
s
)
The total amount of powder deposited (
Δ
Y
tot
) during
Δ
t
is given by:
t
dy
dt
∑
∫
i
Δ
Y
=
dt
(10.3)
tot
i
t
1
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