Environmental Engineering Reference
In-Depth Information
Table 5.1 Some expressions for Newtonian suspension
'
s viscosity as a function of a solids volume fraction (see also Darby [
175
], Hanks [
176
], Steffe [
177
],
Bica et al. [
46
])
Author
Equation
Comment
Equation
number
Guth and Simha
[
178
]
1
/
V
þ
Interaction between particles
(5.4)
g
eff
¼
g
L
1
þ
2
:
5
/
V
þ
14
:
Vand (after
Darby) [
179
]
No interparticle forces
(5.5)
2
:
5
/
V
1
0
:
609
/
V
g
eff
¼
g
L
exp
/
V
1
0
:
609
/
V
Includes doublet collisions, but not triplet
(5.6)
2
:
5
/
V
þ
2
:
7
g
eff
¼
g
L
exp
0
Mooney [
180
]
K depends upon the system and is de
ned experimentally
(5.7)
2
:
5
/
V
1
K
/
V
g
eff
¼
g
L
exp
:
75
K
1
:
5
\
\
Frankel and Acri-
vos [
181
]
Concentrated suspensions only
(5.8)
1
3
1
/
V
=/
max
ð
/
V
=/
max
Þ
9
8
g
eff
¼
g
L
1
3
ð
Þ
Jeffrey and Acri-
vos [
182
]
g
eff
¼
g
L
1
ð
þ
A
/
V
Þ
2
:
5
A
10
Ellipsoid particles
(5.9)
\
\
Thomas [
183
]
g
eff
¼
g
L
1
þ
2
:
5
/
V
þ
10
:
05
/
V
þ
0
:
00273e
16
:
6
/
V
Also includes interaction between the solid particles
(5.10)
d
p
from 0
:
099 to 435
l
m
/
V
\
0
:
625
Batchelor [
184
]
2
/
V
Comprises particle interactions. Brownian motion and
inertia of higher importance
(5.11)
g
eff
¼
g
L
1
þ
2
:
5
/
V
þ
6
:
Bicerano [
185
]
g
eff
¼
g
L
1
þ hi/
V
þ
k
H
/
V
<
> is the intrinsic viscosity, k
H
is the dimensionless
Huggins coefcient
ʷ
(5.12)
Extended Einstein
'
s equation for higher concentrations
Brinkman [
186
]
g
eff
¼
g
L
1
1
/
V
(5.13)
2
:
5
ð
Þ
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