Environmental Engineering Reference
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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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