...
Velocity
...
Gradient Experiment
Introduction
Stepping from previous research with velocity gradients, this experiment seeks to uncouple their effects on tube settler performance deterioration from those of the capture velocity. In the team's last experiments (detailed in Exploring the Coupled Effects of Capture Velocity on Settler Performance), it was hypothesized that maintaining a constant length to diameter ratio in tube settlers would minimize the effects of the capture velocity on performance.
The results showed that at a length to diameter ratio of 20, high capture velocities contributed significantly to poor settler performance at high flow rates. This can best be explained by the fact that at high capture velocities, our settlers fail to eliminate a large portion of the floc particles generated in our floc blanket system from the effluent stream. The flocs exist in this system in a wide range of densities and settling velocities, in a distribution that is currently unknown.
After considering these results, the team decided to allow the length to diameter ratio to change in order to keep the capture velocity constant among tubes of different diameters. A range of tube diameters (1", 1/2", 3/8", 1/4") was chosen based both upon available material and the fact that these diameters represent a reasonably applicable range for AguaClara spacing values. The team's original plan was to fix capture velocity at 0.12 mm/s because it corresponds to the value currently used in AguaClara plants; however, erroneous calculations resulted in the team fixing capture velocity at 0.1 mm/s. The flow rate equation listed below is the correct equation used to calculate the flow rate through the tube given a length, diameter, and capture velocity. When the calculations were originally done for a 0.12 mm/s capture velocity, the wrong equation to calculate flow rate was used. The team has adjusted the parameters for this experiment. The following parameters and methodology was used to design the experiment.
Starting from a capture velocity of 0.1 mm/s, the team chose to test three different up-flow velocities: 0.86, 1.73, and 4.32 mm/s. The first value is that currently used by AguaClara, and the range represents a considerable spectrum of flow rates, and thus velocity gradients, experienced in the tube settlers. The velocity of the influent water increases as it enters the settlers due to hydraulic contraction, and this is a velocity of interest to the team since it also represents the average flow rate through the settler, taking into account also its angle of inclination. These values for this experiment are: 1, 2, and 5 mm/s, and can be calculated from the following relationship:
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Experiment h3. Introduction Stepping from previous research with velocity gradients, this experiment seeks to uncouple their effects on tube settler performance deterioration from those of the capture velocity. In the team's last experiments (detailed in Exploring the Coupled Effects of Capture Velocity on Settler Performance), it was hypothesized that maintaining a constant length to diameter ratio in tube settlers would minimize the effects of the capture velocity on performance. The results showed that at a length to diameter ratio of 20, high capture velocities contributed significantly to poor settler performance at high flow rates. This can best be explained by the fact that at high capture velocities, our settlers fail to eliminate a large portion of the floc particles generated in our floc blanket system from the effluent stream. The flocs exist in this system in a wide range of densities and settling velocities, in a distribution that is currently unknown. After considering these results, the team decided to allow the length to diameter ratio to change in order to keep the capture velocity constant among tubes of different diameters. A range of tube diameters (1", 1/2", 3/8", 1/4") was chosen based both upon available material and the fact that these diameters represent a reasonably applicable range for AguaClara spacing values. The team's original plan was to fix capture velocity at 0.12 mm/s because it corresponds to the value currently used in AguaClara plants; however, erroneous calculations resulted in the team fixing capture velocity at 0.1 mm/s. The flow rate equation listed below is the correct equation used to calculate the flow rate through the tube given a length, diameter, and capture velocity. When the calculations were originally done for a 0.12 mm/s capture velocity, the wrong equation to calculate flow rate was used. The team has adjusted the parameters for this experiment. The following parameters and methodology was used to design the experiment. Starting from a capture velocity of 0.1 mm/s, the team chose to test three different up-flow velocities: 0.86, 1.73, and 4.32 mm/s. The first value is that currently used by AguaClara, and the range represents a considerable spectrum of flow rates, and thus velocity gradients, experienced in the tube settlers. The velocity of the influent water increases as it enters the settlers due to hydraulic contraction, and this is a velocity of interest to the team since it also represents the average flow rate through the settler, taking into account also its angle of inclination. These values for this experiment are: 1, 2, and 5 mm/s, and can be calculated from the following relationship: \\ {latex} \large $$ {{V_\alpha }} = {{ V_{up} } \over {\sin \alpha }} $$ {latex} |
Failure
...
is
...
defined
...
as
...
П
...
V,
...
the
...
ratio
...
of
...
the
...
average
...
floc's
...
settling
...
velocity
...
(a
...
function
...
of
...
both
...
the
...
capture
...
velocity
...
and
...
the
...
floc's
...
density,
...
and
...
thus
...
also
...
a
...
function
...
of
...
the
...
flocculation
...
process),
...
to
...
the
...
velocity
...
experienced
...
by
...
the
...
particle
...
at
...
its
...
diameter
...
exposed
...
to
...
the
...
effluent
...
stream.
...
Particles
...
on
...
the
...
bottom
...
wall
...
of
...
the
...
settler
...
that
...
experience
...
a
...
higher
...
velocity
...
at
...
their
...
exposed
...
edge
...
than
...
the
...
velocity
...
at
...
which
...
they
...
settle
...
out
...
of
...
the
...
tube
...
will
...
experience
...
a
...
torque
...
upwards
...
that
...
causes
...
them
...
to
...
exit
...
with
...
the
...
effluent.
...
Thus
...
when
...
П
...
V
...
is
...
less
...
than
...
one
...
under
...
specific
...
circumstances,
...
roll-up
...
is
...
expected
...
to
...
occur.
...
A
...
value
...
of
...
unity
...
suggests
...
an
...
equilibrium
...
point
...
where
...
roll-up
...
may
...
or
...
may
...
not
...
occur.
...
The
...
procedure
...
to
...
calculate
...
the
...
required
...
lengths
...
for
...
tubes
...
is
...
as
...
follows:
...
1.
...
Choose
...
a
...
range
...
of
...
tube
...
diameter
...
(1"
...
½"
...
3/8"
...
¼")
...
based
...
on
...
available
...
materials
...
and
...
to
...
ensure
...
a
...
good
...
range
...
of
...
spacings.
...
2.
...
Fix
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capture
...
velocity
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at
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10
...
m/day
...
based
...
on
...
the
...
value
...
used
...
for
...
AguaClara
...
plants
...
3.
...
The
...
team
...
used
...
the
...
following
...
relationship
...
for
...
Vα
...
to
...
find
...
the
...
necessary
...
length
...
for
...
each
...
tube
...
diameter
...
required
...
to
...
achieve
...
average
...
velocities
...
of
...
1.04
...
mm/s,
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2.31
...
mm/s,
...
and
...
5.77
...
mm/s.
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{latex} \large $$ {{V_\alpha \sin (\alpha )} \over {V_c }} = {L \over S}\cos \alpha \sin \alpha + \sin ^2 \alpha $$ {latex} |
4.
...
From
...
the
...
V
...
α 's,
...
the
...
team
...
determined
...
the
...
associated
...
velocity
...
gradients
...
by
...
the
...
equation:
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|---|
{latex} \large $$ {{\partial v_z } \over {\partial r}} = {{ - 2v_{ratio} Q} \over {\pi R^4 \sin \alpha }}r $$ {latex} |
where
...
v
...
ratio =
...
2
...
for
...
tubes
...
and
...
1.5
...
for
...
plates
...
α
...
=
...
60
...
degrees
...
R
...
=
...
radius
...
of
...
the
...
tube
...
5.
...
The
...
necessary
...
flow
...
rates
...
were
...
calculated
...
from
...
the
...
capture
...
velocities,
...
diameters,
...
and
...
lengths
...
determined
...
above
...
by
...
the
...
following
...
relationship:
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|---|
{latex} \large $$ Q = \left[ {L\cos (\alpha ) + d^2 \sin (\alpha )} \right]{{\pi n_{Tube} V_C } \over 4} $$ {latex} |
where
...
L
...
=
...
length
...
of
...
the
...
tube
...
d
...
=
...
diameter
...
of
...
the
...
tube
...
α
...
=
...
60
...
degrees
...
r
...
=
...
radius
...
of
...
the
...
tube
...
n
...
tube =
...
number
...
of
...
tubes
...
6.
...
П
...
V ratios
...
were
...
determined
...
for
...
each
...
tube
...
evaluated
...
by
...
the
...
following
...
equation:
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{latex} \large $$ \Pi _V = {{{{g\sin (\alpha )d_0 ^2 \rho _{floc.0} (C_{Alum,} C_{Clay} ) - \rho _{H20} } \over {18\varphi \nu \rho _{H20} }}({{d_{floc} (V_C )} \over {d_0 }})^{d_{fractal} - 1} } \over {{{2V_{UP} } \over {\sin \alpha }}(1 - ({{{d \over 2} - d_{floc} (V_C )} \over {{d \over 2}}}))^2 }} $$ {latex} |
where
...
d
...
0 =
...
diameter
...
of
...
clay
...
particle
...
d
...
floc (V
...
C )
...
-
...
diameter
...
of
...
floc
...
captured
...
based
...
on
...
capture
...
velocity
...
d
...
fractal number
...
generally
...
between
...
2-3
...
for
...
flocs
...
that
...
describes
...
the
...
volume
...
of
...
dirt
...
in
...
the
...
floc
...
compared
...
to
...
the
...
volume
...
of
...
water.
...
A
...
value
...
of
...
3
...
indicates
...
that
...
the
...
floc
...
has
...
no
...
water
...
within
...
it.
...
ρ
...
floc.
...
0 (C
...
Alum,C
...
Clay)
...
-
...
density
...
of
...
floc
...
based
...
on
...
concentration
...
of
...
alum
...
and
...
clay,
...
respectively
...
ρ H20 - density of water
ν - kinematic viscosity of water
Φ - shape factor
An updated materials list and velocity gradient model can be found on the PSS Fall 2010 Velocity Gradients Experiments page.
Experimental Methods
Conclusions from the previous experiments (Exploring the Coupled Effects of Capture Velocity and Velocity Gradient on Settler Performance) showed that there was a problem with particles settling out in the turbidimeter at low flow rates. The team performed an experiment in which it found that to prevent this settling, a flow rate of at least 50 mL/min needs to be driven through the turbidimeter. Table 1 of the conclusions indicates that for the smaller tube, flow rates were considerably lower than this value. To address this, the team has decided to use bundles of tube joined by a manifold and a reservoir system. Equal flow distribution is ensured by placing small orifices in the manifold to provide 1 cm of headloss. The flow rate through the tube bundles is pumped into the reservoir continuously until a certain level is reached. This time is called the loading state. At that point, a pump begins to pull water from the reservoir to the turbidimeter at a flow rate higher than 50 mL/min, called the withdrawal state. The pump shuts down when a minimum water height is reached, allowing the reservoir to refill to the maximum specified height before repeating the cycle. The reservoir's sample is continuously stirred and mixed; this should provide an average turbidity reading the turbidimeter. A full analysis of residence times is still in progress.
Aside from the reservoir and bundled tubes, the system is the same as in the previous team's experiments. For data collection, the team plans to collect usable data for at least three residence times in the system, containing: tube settlers, connecting tubes, reservoir, and turbidimeter. With the reservoir system, usable data can only be collected in the withdrawal state. Data collected during the loading state is unusable and should be discarded.
Results
The experiments have not been performed, but the materials list in the introduction elaborates on the expected results. The following figure shows the inverse of the pi ratio plotted against the diameter of tube settler. For diameters at which the inverse is greater than one, roll-up is expected to occur.
