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Phase 1: Dry weather
level.
The V2B1 utilizes two round structures of varying
diameters (depths for both structures are typically equal). The two
structures are connected by a series of three pipes.
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Phase 2: First flush, two
month storm.
The first chamber (1) is designed to separate the
contaminated particulate (brown) from the drain water. The inlet
pipe is offset to introduce the influent tangentially into the first
structure. Floating pollutants (red) such as petroleum, litter and
organics are pushed through the center pipe into the floatable
containment chamber (2).
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Phase 3: Rising storm
flow intensity.
As the volume of flow through the inlet pipe
increases, a swirl begins to develop in the first chamber (1).
Liquid levels in the structures correspond with the intensity of the
storm event.
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Phase 4: Residual
floatable transport.
Residual floatables, which were not transferred to
the floatable containment chamber (2) during the initial storm flow,
rise to the point of overcoming the vertical portion of the bottom
pipe called the "Coriolus Intake". The residuals are then
drawn into the middle of swirl-chamber (1) and delivered to the
floatable containment chamber (2) in a low-flow circumstance.
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Phase 5: Peak flow,
floatable chamber bypass.
The corner stone of the V2B1 hydraulic design is
the top pipe connecting the vortex separator to the outlet chamber
(3). This "shunt", under peak storm design, carries the
majority of flow directly to the outlet chamber (3). By discouraging
peak flows from passing under the baffle wall, any Venturi effect on
or discharge of captured pollutants from the V2B1 system are
minimized.
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Phase 6: Dry weather
pump-out.
The frequency of pump-out is based on the site
loading, periodic monitoring and measurements of captured pollutant
levels in the swirl-chamber (1). If the V2B1 is maintained on a
regular schedule, the only chamber that requires pumping is the
swirl-chamber (1). This will remove both solid and floating
pollutants from the system.
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Take a look at the Animated
View!
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