Abstract:Unsteady turbulent swirled water flow in a channel in the presence of cavitation is calculated. It is shown that in the near-axial channel zone a fluctuating vapor region, or cavity, arises and variations in the cavity shape and dimensions lead to the onset of undamped pressure fluctuations. The amplitude-frequency characteristics of the oscillations are obtained in different channel cross-sections. The amplitude maximum position in the channel expansion zone is in agreement with the available experimental dat… Show more
“…Several mechanisms of the pressure fluctuation generation in hydrodynamic generators were established. These are the separation of toroidal vortices formed in the generator channel [3], separation and downstream convection of vapor regions in the presence of cavitation [6], the precessional rotation of a curved vortex core around the axis of symmetry of the chamber leading to the violation of the flow axial symmetry [7,8], and periodic variations of the shape and dimensions of the cavity formed in the lowpressure zone in the axial region of the channel [9,10]. One or another oscillation generation mechanism can be predominant depending on the hydrodynamic generator geometry and the operating regime.…”
Section: Operating Principle Of the Wave Disperser Of A Gas In A Liquidmentioning
confidence: 99%
“…For all gas flow rates considered the disperser with the channel diameter D = 5 mm showed better results than that with D = 7 mm. Apparently, this is due to the fact that in the channel having the smaller diameter fluctuations in the cavitation cavity lead to the more considerable variation in the effective duct cross-section [10] which enhances the pressure fluctuations and improves the dispersion fineness.…”
Section: Effect Of the Generator Channel Length On The Bubble Sizesmentioning
The influence of the channel diameter and length of the hydrodynamic oscillation generator on gas bubble dimensions in the case of wave dispersion of a gas in a liquid is experimentally investigated. The technique of measuring the bubble diameters based upon the computer analysis of the gas-liquid jet photos is presented. It is shown that on the gas flow rate range from 0.5 to 32 dm 3 /min the mean diameter of the gas bubbles produced by wave dispersers in water is estimated by an interval from 0.45 to 0.75 mm in optimum performance regimes.
“…Several mechanisms of the pressure fluctuation generation in hydrodynamic generators were established. These are the separation of toroidal vortices formed in the generator channel [3], separation and downstream convection of vapor regions in the presence of cavitation [6], the precessional rotation of a curved vortex core around the axis of symmetry of the chamber leading to the violation of the flow axial symmetry [7,8], and periodic variations of the shape and dimensions of the cavity formed in the lowpressure zone in the axial region of the channel [9,10]. One or another oscillation generation mechanism can be predominant depending on the hydrodynamic generator geometry and the operating regime.…”
Section: Operating Principle Of the Wave Disperser Of A Gas In A Liquidmentioning
confidence: 99%
“…For all gas flow rates considered the disperser with the channel diameter D = 5 mm showed better results than that with D = 7 mm. Apparently, this is due to the fact that in the channel having the smaller diameter fluctuations in the cavitation cavity lead to the more considerable variation in the effective duct cross-section [10] which enhances the pressure fluctuations and improves the dispersion fineness.…”
Section: Effect Of the Generator Channel Length On The Bubble Sizesmentioning
The influence of the channel diameter and length of the hydrodynamic oscillation generator on gas bubble dimensions in the case of wave dispersion of a gas in a liquid is experimentally investigated. The technique of measuring the bubble diameters based upon the computer analysis of the gas-liquid jet photos is presented. It is shown that on the gas flow rate range from 0.5 to 32 dm 3 /min the mean diameter of the gas bubbles produced by wave dispersers in water is estimated by an interval from 0.45 to 0.75 mm in optimum performance regimes.
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