ozeair Abessi
Phone: +989111146756
Address: Shariati Av., Babol, Mazandaran, Iran
Address: Shariati Av., Babol, Mazandaran, Iran
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Papers by ozeair Abessi
a high-dimensional state space. We also explain the relation between Taylor’s hypothesis and the comoving frame velocity Ud of the turbulent orbit in state space. In particular, in physical space we observe flow structures that deform as they advect downstream at a speed that differs significantly from Ud. Indeed, the symmetry-reduction analysis of planar dye concentration fields at Reynolds number Re = 3200 reveals that the speed u at which high-concentration peaks advect is
roughly 1.43 times Ud. In a physically meaningful symmetry-reduced frame, the excess speed u-Ud = 0.43 Ud can be explained in terms of the so-called geometric
phase velocity Ug associated with the orbit in state space. The ‘self-propulsion velocity’ Ug is induced by the shape-changing dynamics of passive scalar structures observed in the symmetry-reduced frame, in analogy with that of a swimmer at flow Reynolds numbers.
were conducted with nozzles oriented at 30°, 45°, and 60° to the horizontal and the spatial variations of tracer concentrations were measured by three-dimensional laser-induced fluorescence (3DLIF). Three flow regimes were identified: deep water, surface contact, and shallow water. The regimes depend on the value of dF=H, where d is the nozzle diameter, F the jet densimetric Froude number, and H the water depth; criteria were presented for the transitions between them. Flow images revealed complex three-dimensional interactions with the free surface, especially for steep nozzle angles in shallow water. Dilutions at critical points and their locations were measured. For deep water, all
results followed those previously reported for fully submerged jets. As the depth decreases (or dF=H increases) to the surface contact regime, dilutions begin to decrease. Tracer concentration profiles are truncated at the water surface and in shallow water resemble half-Gaussian profiles similar to those of wall jets. The jets can cling to the water surface, although the locations of the bottom impact point and near-field
length are not significantly affected by the water surface. In deep water and surface contact regimes, the impact point and near-field dilutions
are highest for 60° nozzles. As the depth decreases further, however, the dilutions for the three nozzle angles become approximately equal, until, for shallow water, the 30°-nozzle gives slightly higher dilution. The 30°-nozzle may be preferable for this case because there is less
surface interaction and, therefore, less visual impact on the water surface. Previous recommendations that dense jets be submerged so that the rise height to the jet’s upper boundary be less than 75% of the water depth to avoid surface effects appear to be overly conservative and the present results suggest that the rise can be as much as 90% of the water depth for all angles with no deleterious effect on dilution.
properties were measured by laser-induced fluorescence at the maximum rise height, impact point, and, for the first time, at the end of the near
field. The impact point dilution was insensitive to nozzle angle over the range of about 45–65°. Because the additional mixing that occurred in
the spreading layer beyond the impact point depended on nozzle angle, the near-field dilution was more sensitive to nozzle orientation and was highest for 60°, consistent with generally accepted design practice. Bottom boundary effects on dilution were also addressed. Along the jet centerline, time-average dilution first increased and then actually decreased in a thin layer up to the wall. The concentration increase near
the bed is due to an increase in turbulent intermittency and accumulation of more saline fluid elements at the bed. The presence of this layer may explain wide discrepancies in reported dilutions near the boundary and may be environmentally important due to exposure of benthic
organisms and sea grasses to high salinity. It may not persist, however, as it can be swept up by vortices that propagate radially away from the impact point. The vortices entrain ambient fluid leading to increased dilution, but they eventually collapse under their self-induced density stratification, marking the end of the near field.
results compared with simulations of the CORMIX model, an expert system for ocean outfall design. In CORMIX, the simulation module DHYDRO for dense discharges has been used. Finally the flow different patterns were arranged in a dimensionless diagram to propose a modified flowclassification system with new criteria
a high-dimensional state space. We also explain the relation between Taylor’s hypothesis and the comoving frame velocity Ud of the turbulent orbit in state space. In particular, in physical space we observe flow structures that deform as they advect downstream at a speed that differs significantly from Ud. Indeed, the symmetry-reduction analysis of planar dye concentration fields at Reynolds number Re = 3200 reveals that the speed u at which high-concentration peaks advect is
roughly 1.43 times Ud. In a physically meaningful symmetry-reduced frame, the excess speed u-Ud = 0.43 Ud can be explained in terms of the so-called geometric
phase velocity Ug associated with the orbit in state space. The ‘self-propulsion velocity’ Ug is induced by the shape-changing dynamics of passive scalar structures observed in the symmetry-reduced frame, in analogy with that of a swimmer at flow Reynolds numbers.
were conducted with nozzles oriented at 30°, 45°, and 60° to the horizontal and the spatial variations of tracer concentrations were measured by three-dimensional laser-induced fluorescence (3DLIF). Three flow regimes were identified: deep water, surface contact, and shallow water. The regimes depend on the value of dF=H, where d is the nozzle diameter, F the jet densimetric Froude number, and H the water depth; criteria were presented for the transitions between them. Flow images revealed complex three-dimensional interactions with the free surface, especially for steep nozzle angles in shallow water. Dilutions at critical points and their locations were measured. For deep water, all
results followed those previously reported for fully submerged jets. As the depth decreases (or dF=H increases) to the surface contact regime, dilutions begin to decrease. Tracer concentration profiles are truncated at the water surface and in shallow water resemble half-Gaussian profiles similar to those of wall jets. The jets can cling to the water surface, although the locations of the bottom impact point and near-field
length are not significantly affected by the water surface. In deep water and surface contact regimes, the impact point and near-field dilutions
are highest for 60° nozzles. As the depth decreases further, however, the dilutions for the three nozzle angles become approximately equal, until, for shallow water, the 30°-nozzle gives slightly higher dilution. The 30°-nozzle may be preferable for this case because there is less
surface interaction and, therefore, less visual impact on the water surface. Previous recommendations that dense jets be submerged so that the rise height to the jet’s upper boundary be less than 75% of the water depth to avoid surface effects appear to be overly conservative and the present results suggest that the rise can be as much as 90% of the water depth for all angles with no deleterious effect on dilution.
properties were measured by laser-induced fluorescence at the maximum rise height, impact point, and, for the first time, at the end of the near
field. The impact point dilution was insensitive to nozzle angle over the range of about 45–65°. Because the additional mixing that occurred in
the spreading layer beyond the impact point depended on nozzle angle, the near-field dilution was more sensitive to nozzle orientation and was highest for 60°, consistent with generally accepted design practice. Bottom boundary effects on dilution were also addressed. Along the jet centerline, time-average dilution first increased and then actually decreased in a thin layer up to the wall. The concentration increase near
the bed is due to an increase in turbulent intermittency and accumulation of more saline fluid elements at the bed. The presence of this layer may explain wide discrepancies in reported dilutions near the boundary and may be environmentally important due to exposure of benthic
organisms and sea grasses to high salinity. It may not persist, however, as it can be swept up by vortices that propagate radially away from the impact point. The vortices entrain ambient fluid leading to increased dilution, but they eventually collapse under their self-induced density stratification, marking the end of the near field.
results compared with simulations of the CORMIX model, an expert system for ocean outfall design. In CORMIX, the simulation module DHYDRO for dense discharges has been used. Finally the flow different patterns were arranged in a dimensionless diagram to propose a modified flowclassification system with new criteria