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1993, Journal of Fluid Mechanics
Bubble plumes in a linearly stratified ambient fluid are studied. Four well-defined flow regions were observed: an upward-moving bubble core, an inner plume consisting of a mixture of bubbles and relatively dense fluid, an annular downdraught and beyond that a horizontal intrusion flow. Depending on the gas flow rate with respect to the stratification, three types of intrusions were documented. At large gas flow rates a single intrusion was observed. As the gas flow rate was decreased, the buoyancy flux was insufficient to carry the lower fluid to the surface and a stack of intrusions were formed. At very low gas flow rates the intrusions became unsteady. The transition between these three regimes was observed to occur at critical values of the pararnetersN3H4/(QBg), Q B g / (4~a~u~ H) , and H/H,, where N is the buoyancy frequency, H is the water depth, HT is equal to H+H,, H A being the atmospheric pressure head, Q B is the gas flow rate at the bottom, g the acceleration due to gravity, a the entrainment coefficient and us the differential between the bubble and the average water velocity commonly called the slip velocity. The height between intrusions was found to scale with the Ozmidov length (QBg/P)i, the plunge point entrainment with the inner plume volume flux (Q, g)gN-f and the radial distance to the plunge point with (Qog/Ns)i, where Q, is the gas flow rate at the free surface. These results were used to construct a double annular plume model which was used to investigate the efficiency of conversion of the input bubble energy to potential energy of the stratification; the efficiency was found to first increase, reach a maximum, then decrease with decreasing gas flow rate. This agreed well with the results from the laboratory experiments.
Physical Review Fluids, 2017
A cross-sectionally averaged model is used to study several aspects of the physics of a bubble plume rising in a stratified quiescent liquid. Scaling analyses for the peel height, at which the plume momentum vanishes, and the neutral height, at which its average density equals the ambient density, are presented. Contrary to a widespread practice in the literature, it is argued that the neutral height cannot be identified with the experimentally reported intrusion height. Recognizing this difference provides an explanation of the reason why the intrusion height is found so frequently to be much above predictions and brings the theoretical results in line with observations. The mathematical model depends on three dimensionless parameters, some of which are related to the inlet conditions at the plume source. Their influence on the peel and neutral heights is illustrated by means of physical considerations, scaling analyses, and numerical results.
Models are developed to describe the gross behavior of air-bubble plumes generated by point and line sources of air-bubbles released in stagnant water bodies of uniform density. The models predict plume width, velocities, and induced flow rates as a function of elevation above the source. The analysis is confined to the plume mechanics and does not include the horizontal flow created at the surface by the plume. An integral similarity approach, similar to that used for single-phase buoyant plumes, is employed. Governing equations are found by applying conservation of mass, momentum, and buoyancy. The compressibility of the air and the differential velocity between the rising air bubbles and water are introduced in the buoyancy flux equation. Generalized solutions to the normalized governing equations are presented for both point and line sources of air-bubbles. The results of the analyses are compared with existing large-scale experimental data. The comparisons indicate that the models predict the gross behavior of plumes well and yield estimates of the entrain-ment coefficients and lateral spreading ratios.
Physical Review Fluids
Characteristics and material transport of a bubble-driven plume in stably stratified water with uniform crossflow are studied using an Eulerian-Eulerian large-eddy simulation model. Four laboratory-scale plume conditions with different bubble rise velocities (w r = 3, 6, 12, and 20 cm/s) are considered, and their characteristics under three weak crossflow conditions (U c = 0.5, 1, and 2 cm/s) are studied. The interaction between the rising bubbles and the stratified water generates a double-plume structure, consisting of a rising plume of bubble/water mixture and a falling plume of dense water peeled from the rising plume due to the stratification effect. The presence of crossflow forces the rising plume to incline and causes the falling plume to form on the downstream side (with respect to the crossflow direction) of the rising plume, resulting in reduced contact area between the two plumes. Consequently, the turbulent mixing of the vertical momentum between the rising and falling plumes is reduced, causing the magnitude of the vertical velocity in both plumes to increase when the crossflow velocity is increased. The material transport from the plume to the horizontal intrusion layer (traced using dye) also exhibits strong dependence on the crossflow velocity. Faster crossflow results in narrower lateral extension and wider vertical extension of the intrusion layer due to the interaction between the peeling process and the crossflow. For cases with the two smaller w r (3 and 6 cm/s), the plume can form a distinct peeling event that dominates the material transport process. As a result, the mean intrusion layer height h t shows only small variation for these two plume conditions when U c is increased. In contrast, the plumes with w r = 12 and 20 cm/s exhibit noticeable decrease of h t (9% and 24%, respectively) when U c is increased from 0.5 to 2 cm/s. Statistical analysis of the streamwise dye flux shows that the decrease of h t with increased U c for the cases with w r = 12 and 20 cm/s is mainly due to the crossflow-enhanced mean flux of dye from the rising plume at the low elevation.
International Journal of Multiphase Flow, 2002
1) A short review is given of some of the important publications on air-bubble plumes. Two main ways of modelling, using either the entrainment assumption, or the energy balance principle, are presented and briefly compared.
International Journal of Multiphase Flow, 2006
An extensive study of the most important hydrodynamic characteristics of fairly large-scale bubble plumes was conducted using several measurement techniques and a variety of tools to analyze the data. Particle image velocimetry (PIV), double-tip optical probes (OP) and photographic techniques were extensively applied to measure bubble and liquid velocities, void-fraction and bubble sizes. PIV measurements in a vertical plane crossing the centre of the injector provided the instantaneous velocity fields for both phases, as well as hydrodynamic parameters, such as the movement of the axis of the plume and its instantaneous shape. Statistical studies were performed using image processing to determine the distribution of the apparent instantaneous plume diameter and centreline position. An important finding was that there is little instantaneous spreading of the bubble plume core; the spreading of the time-averaged plume width (as measured from the time-averaged void-fraction and time-averaged liquid velocity fields) is largely due to plume meandering and oscillations. The liquid-phase stress tensor distributions obtained from the instantaneous velocity data indicate that, for the continuous phase, these stresses scale linearly with the local void-fraction in the range of 0.5% < a < 2.5%. The bubbles were found to be ellipsoidal, with shape factor e % 0.5.
Journal of Fluid Mechanics, 1989
A method has been devised for measuring the volume flux in a bubble plume in a homogeneous liquid. Laboratory experiments on weak bubble plumes using the method determined the flux as a function of height and gas flow rate for air flow rates between 0.41 and 6.25 cc/s. It was found that volume flux was proportional to the square-root of air flow and increased linearly with height. From measurement of bubble velocity it is concluded that the individual bubble wakes make an important contribution to the entrainment.
In bubbly flow, bubbles and the surrounding fluid interact through both force and turbulence coupling. The effects of flow turbulence on bubble trajectory are reflected in turbulent dispersion. Bubbles will introduce extra turbulence into the fluid through wake effects (so-called pseudo turbulence). The single phase k-epsilon model does not incorporate the bubble-induced turbulence [1]. This study aimed to develop and implement a model to account for these effects. The gas-stirred-ladle experiments of [10] and [1] were employed for validation. The model framework combines a volume of fluid (VOF) and discrete phase model (DPM). VOF is used to capture the fountain shape formed by the bubble plume reaching the surface, while DPM is a parcel-based Lagrangian approach to track bubbles.
Journal of Hydraulic Research, 2007
In this paper, we focus on bubble plumes aimed at providing oxygen to, and at mixing unstratified water bodies. First, we discuss scaling relations obtained from a three-dimensional (3D) theoretical model for multi-component fluids. An expression for a length scale that represents a balance between inertia and buoyancy is derived, and it is used to scale vertical as well as horizontal (radial) distances. This length scale is then analyzed in terms of previous bubble-plume non-dimensional numbers. For the practical case in which the bubble diameter remains almost constant throughout the bubble plume, a one-dimensional theoretical model-which can be derived by integrating the 3D model in a horizontal plane-is used to show that the length scale (D) is well suited for defining zones in bubble plumes. These zones include a region near the diffuser where the size of the diffuser is important, an intermediate zone where the diffuser size and D determine the flow features, and an asymptotic region where plume variables approach a universal behavior. Procedures for scaling entire reservoirs and portions of reservoirs are developed. These procedures are evaluated with results from previous experiments and new observations in a large tank and a scaled physical model. Scaling of turbulence statistics in bubble plumes is also investigated.
2000
In this paper, we focus on bubble plumes aimed at providing oxygen to, and at mixing unstratified water bodies. First, we discuss scaling relations obtained from a three-dimensional (3D) theoretical model for multi-component fluids. An expression for a length scale that represents a balance betw een inertia and buoyancy is derived, and it is used to scale vertical as well
1990
The goal of the research presented in this report is to analyze, understand, and simulate the flow field induced by a bubble plume in a lake or reservoir. This is useful and necessary for the design of lake or reservoir aeration and destratification projects.
Annals of the New York Academy of Sciences, 2002
This paper presents an integral model to evaluate the impact of gas transfer on the hydrodynamics of bubble plumes. The model is based on the Gaussian type self-similarity and functional relationships for the entrainment coeffi cient and factor of momentum amplifi cation due to turbulence. The impact of mass transfer on bubble plume hydrodynamics is investigated considering different bubble sizes, gas fl ow rates and water depths. The results revealed a relevant impact when fi ne bubbles are considered, even for moderate water depths. Additionally, model simulations indicate that for weak bubble plumes (i.e., with relatively low fl ow rates and large depths and slip velocities), both dissolution and turbulence can affect plume hydrodynamics, which demonstrates the importance of taking the momentum amplifi cation factor relationship into account. For deeper water conditions, simulations of bubble dissolution/decompression using the present model and classical models available in the literature resulted in a very good agreement for both aeration and oxygenation processes. Sensitivity analysis showed that the water depth, followed by the bubble size and the fl ow rate are the most important parameters that affect plume hydrodynamics. Lastly, dimensionless correlations are proposed to assess the impact of mass transfer on plume hydrodynamics, including both the aeration and oxygenation modes.
International Journal of Multiphase Flow, 1996
The axisymmetric air-bubble plume in water may be thought of as emanating from a virtual point source located at some distance below the real source. To give a phenomenological description of this system one has at one's disposal the equation of continuity, the balance equation for momentum, and the balance equation for kinetic energy. The most common way of approach so far has been to make use of the first two of these equations, together with the assumption that the rate of entrainment be proportional to the vertical centerline velocity. This is the theory developed, in particular, by . The present paper presents an alternative theory, in which the rate-of-entrainment assumption is abandoned and use is made of the kinetic energy equation together with the assumption that the most dominant component of the Reynolds stress be self-preserved. Very good agreement is found in this way with the large scale experiments of Kobus 0968) and . The agreement is somewhat better than that found for the plane plume; the analogous theory for this case was developed by one of the present authors (I.B.). The conclusion of our analysis is that the kinetic energy approach stands out as a quite viable alternative for engineering applications in the axisymmetric case. Copyright
Environmental Fluid Mechanics, 2018
We present the development and validation of a numerical modeling suite for bubble and droplet dynamics of multiphase plumes in the environment. This modeling suite includes real-fluid equations of state, Lagrangian particle tracking, and two different integral plume models: an Eulerian model for a double-plume integral model in quiescent stratification and a Lagrangian integral model for multiphase plumes in stratified crossflows. Here, we report a particle tracking algorithm for dispersed-phase particles within the Lagrangian integral plume model and a comprehensive validation of the Lagrangian plume model for single-and multiphase buoyant jets. The model utilizes literature values for all entrainment and spreading coefficients and has one remaining calibration parameter j, which reduces the buoyant force of dispersed phase particles as they approach the edge of a Lagrangian plume element, eventually separating from the plume as it bends over in a crossflow. We report the calibrated form j ¼ ½ðb À rÞ=b 4 , where b is the plume halfwidth, and r is the distance of a particle from the plume centerline. We apply the validated modeling suite to simulate two test cases of a subsea oil well blowout in a stratificationdominated crossflow. These tests confirm that errors from overlapping plume elements in the Lagrangian integral model during intrusion formation for a weak crossflow are negligible for predicting intrusion depth and the fate of oil droplets in the plume. The Lagrangian integral model has the added advantages of being able to account for
Nuclear Engineering and Design, 2011
The current paper presents the prediction results of a bubbly flow under plunging jet conditions using multiphase mono-and poly-dispersed approaches. The models consider interfacial momentum transfer terms arising from drag, lift, and turbulent dispersion force for the different bubble sizes. The turbulence is modeled by an extended k-ε model which accounts for bubble induced turbulence. Furthermore in case of a poly-dispersed air-water flow the bubble size distribution, bubble break-up and coalescence processes as well as different gas velocities in dependency on the bubble diameter are taken into account using the Inhomogeneous MUSIG model. This model is a generalized inhomogeneous multiple size group model based on the Eulerian modeling framework which was developed in the framework of a cooperative work between ANSYS-CFX and Forschungszentrum Dresden-Rossendorf (FZD). The latter is now implemented into the CFD code CFX.
Chemical Engineering Science, 2021
h i g h l i g h t s An enhanced turbulence model has been developed and validated, which is generally applicable to bubble plumes. The model accounts for the extra turbulence agitation introduced by bubble wakes. The model also considers the turbulence modulations due to bubble-induced stratification and free surface damping effects. The implications of each physical process in turbulence modelling are investigated.
Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences, 2020
Weak bubble plumes carry liquid from the environment upwards and release it at multiple intermediate levels in the form of radial intrusive currents. In this study, laboratory experiments are performed to explore the spreading of turbulent axisymmetric bubble plumes in a liquid with linear density stratification. The thickness, volumetric flowrate and spreading rates of multiple radial intrusions of plume fluid were measured by tracking the movement of dye injected at the source of bubbles. The experimental results are compared with scaling predictions. Our findings suggest that the presence of multiple intrusions reduces their spreading rate, compared to that of a single intrusion. This work is of relevance to the spreading of methane plumes issuing from the seabed in the Arctic Ocean, above methane-hydrate deposits. The slower, multiple spreading favours the presence of methane-rich seawater close to the plume, which may reduce the dissolution of methane in the bubbles, and thus p...
It is well known that the environment degradation has come along the time positioning as one of the main problems from modern world. Among several questions of the environmental interest the methane bubble rise in the lakes can be emphasized, from the anoxic sediment in the bottom of lake until water interface atmosphere. In particular, the present academic work has come to treat mathematic modeling of the bubble rise through sediment viscous fluid near the bottom lake and present results, via Mathematics and Computing-Numeric Simulation, about the terminal velocity ascent of the bubble.
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