Environmental Engineering Reference
In-Depth Information
the gravity (m/s
2
) and η
is the viscosity of water (Pa s). To suspend a spherical particle with
a diameter of
D
, the condition required is expressed by
2
D
(
ρρ
η
−
)
g
p
w
v
≥
(13.2)
w
18
or
18η
ρρ
v
D
≤
w
(13.3)
(
−
)
g
p
w
Thus, under a given convectional upward velocity, particles smaller than a given size
(weight) can be suspended and most of them can be transported with the convectional
water low. From Equation 13.2, the approximate
v
w
value against
D
= 0.075 mm, can be
estimated to be
v
w
= 4.4 mm/s. This can provide the approximate upward low velocity
necessary to suspend particles smaller than 0.075 mm. Field trials will allow for ine-tuning
of the low velocity requirements. In the case of particles larger than the anticipated maxi-
mum size, these will remain at the bottom. In a given water column system, convectional
low can segregate the suspended particles, as demonstrated in Figure 13.13 and smaller
suspended particles can be removed from a given water depth. The diameters of the par-
ticles in Figure 13.13 are expressed as
D
s
<
D
<
D
g
at steady state. It is noted that the speciic
gravity of particles and the viscosity of water will affect the result, as shown in Equation
D
s
suspended solids
are relatively small
ν
w
D
g
suspended
solids are
relatively large
Immovable large particles
FIGURE 13.13
Concept for suspending smaller particles by forced convection low.
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