Academia.edu no longer supports Internet Explorer.
To browse Academia.edu and the wider internet faster and more securely, please take a few seconds to upgrade your browser.
2016, International Journal of Multiphase Flow
An experimental investigation is reported for the flow structures in the wake of an air bubble sliding under an inclined surface in quiescent water. Time-resolved particle image velocimetry (PIV) is used to study the wakes of sliding bubbles for a range of measurement planes, bubble diameters and surface inclination angles. Additionally, key aspects of the bubble's motion are measured simultaneously using a novel method that accounts for the motion of the bubble's interface. Thus, vortex shedding may be linked to changes in the bubble shape and path. Analysis of the measured velocity and vorticity fields reveals a wake structure consisting of a near wake that moves in close proximity to the bubble, shedding vorticity at the inversion points of the bubble path. Downstream of the bubble in the far wake, these structures evolve into asymmetrical, oppositelyoriented hairpin vortices that are generated in the near wake. These hairpin vortices bear similarities to those observed behind freely rising bubbles and near-wall bluff bodies and are found to cause significant motion of the bulk fluid. This bulk fluid motion has the potential to offer significant convective cooling of adjacent heated surfaces, such as submerged electronics components.
Physical Review Fluids, 2017
In this work, Schlieren measurements are presented for the wake of an air bubble sliding under a heated, inclined surface in quiescent water to provide new insights into the intricate sliding bubble wake structure and the associated convective cooling process. This is a two-phase flow configuration that is pertinent to thermal management solutions, where the fundamental flow physics have yet to be fully described. In this work, we present an experimental apparatus that enables high-quality Schlieren images for different bubble sizes and measurement planes. By combining these visualizations with an advanced bubble tracking technique, we can simultaneously quantify the symbiotic relationship that exists between the sliding bubble dynamics and its associated wake. An unstable, dynamic wake structure is revealed, consisting of multiple hairpin-shaped vortex structures interacting within the macroscopic area affected by the bubble. As vorticity is generated in the near wake, the bubble shape is observed to recoil and rebound. This also occurs normal to the surface and is particularly noticeable for larger bubble sizes, with a periodic ejection of material from the near wake corresponding to significant shape changes. These findings, along with their implications from a thermal management perspective, provide information on the rich dynamics of this natural flow that cannot be obtained using alternate experimental techniques.
World Academy of Science, Engineering and Technology, International Journal of Mechanical, Aerospace, Industrial, Mechatronic and Manufacturing Engineering, 2016
The dynamics of bubbly flows are rich and varied, with the understanding of these flows a major issue for many engineering applications. Although a large body of work exists for bubbles rising in an unbounded medium, that of bubbles rising in constricted geometries has received less attention. The particular case of a bubble sliding underneath an inclined surface is common to two-phase flow systems such as shell and tube heat exchangers, mineral flotation and oxidation in water treatment. Prior work by the authors has quantified the surface heat transfer of a single air bubble sliding under a heated surface, showing that enhanced heat transfer is achievable for gas bubbles, even at low wall superheats. The current study intends to expand this knowledge by performing experiments to quantify the streamwise flow structures associated with a single sliding air bubble under an inclined surface in quiescent water and adiabatic conditions. This is achieved by means of two-dimensional, two-component particle image velocimetry (PIV), performed with a continuous wave laser and high-speed camera. PIV velocity and vorticity fields obtained in a plane perpendicular to the sliding surface show that there is significant bulk fluid motion away from the surface, likely contributing to the aforementioned heat transfer enhancement. Additionally, the associated momentum of the bubble means that this wake motion persists for a significant time before viscous dissipation. Bubbles in the shape regime defined by the Reynolds, Morton and Weber numbers are ellipsoidal and experience path oscillations. The magnitude and direction of the flow structures in the streamwise measurement plane are found to depend on the point on its path through which the bubble enters the plane. This entry point, represented by a phase angle, affects the nature and strength of the vortical structures. Previous work has shown that streamwise vorticity downstream of the bubble is key to understanding these flow structures and their effects on fluid mixing. The current study reconstructs the vorticity field in the wake of the bubble, converting the field at different instances in time to slices of a large-scale wake structure. This is, in essence, Taylor's "frozen turbulence" hypothesis. Applying this to the obtained vorticity fields provides a pseudo three-dimensional representation from 2-D data, allowing for a more intuitive understanding of the bubble wake. This study provides insights into bubble behaviour for a configuration that is ubiquitous to engineering applications, and will aid in the interpretation of previously obtained surface heat transfer measurements.
Chinese Journal of Chemical Engineering, 2018
An experimental study was conducted to investigate the 2D bubbly flow downstream of a cylinder. Sparsely distributed bubbles were produced using the ventilation method. The carrier flow was measured using the particle image velocimetry (PIV) technique. The shadow imaging technique was used to capture instantaneous bubbly flow images. An image-processing code was compiled to identify bubbles in acquired image, calculate the bubble equivalent diameter and the bubble velocity. The effects of Reynolds number and the flow rate of the injected air were considered. The result indicates that the carrier flow is featured by distinct flow structures and the wake region is suppressed as the upstream velocity increases. Regarding the bubbles trapped in the wake flow, the number of small bubbles increases with the upstream velocity. On the whole, the bubble velocity is slightly lower than that of the carrier flow. The consistency between small bubbles and the carrier flow is high in terms of velocity magnitude, which is justified near the wake edge. The difference between the bubble velocity and the carrier flow velocity is remarkable near the wake centerline. For certain Reynolds number, with the increase in the air flow rate, the bubble equivalent diameter increases and the bubble void fraction is elevated.
International Journal of Multiphase Flow, 2009
International Journal of Heat and Mass Transfer, 2017
An experimental investigation is reported for the bubble-wake interactions that occur between an in-line air bubble pair sliding under an inclined surface in quiescent water. Three experimental techniques are utilised to study this flow: time-resolved particle image velocimetry (PIV), a new edge-based bubble tracking algorithm incorporating high speed video and high speed infrared thermography. These techniques allow for a novel characterisation of sliding bubble-wake interactions in terms of their associated fluid motion, the fluid-induced changes in the trailing bubble interface and the resulting surface convective heat transfer. As these interactions are ubiquitous to multiphase flows, such knowledge is pertinent to many industrial applications, including the optimisation of two-phase cooling systems. This work has revealed that for an intermediate bubble size, in-line bubble pairs adopt a configuration in which their paths are 180°out of phase. Upon entering the fluid shed from the near wake of the leading bubble at each local extremum, the trailing bubble is accelerated both in the direction of buoyancy and in the spanwise direction corresponding to that of the shed fluid structure. This causes significant, high-frequency changes in the interface of the trailing bubble, which recoils and rebounds during this interaction. Surface heating adds further complexity to the bubble-wake interaction process due to the disruption of the thermal boundary layer at the surface. It is found that the trailing bubble can momentarily decrease local convective heat transfer levels by displacing the cool fluid introduced to the surface by the leading bubble. However, the amplified fluid mixing and local heat transfer enhancement of 7-8 times natural convection levels observed at the trailing bubbles mean that the net effect of the trailing bubble is to enhance convective heat transfer.
Journal of Visualization, 2005
A study on flow field measurement around growing and rising vapour bubbles by use of PIV technique is presented. Bubbles were generated from single artificial cavities. Experiments have been conducted with saturated boiling of distilled water at atmospheric pressure. In the experiment fluid velocity field surrounding the bubbles was visualized by use of polyamide tracer particles and a sheet of a YAG pulse laser beam. The images were recorded with a cross-correlation CCD-camera. It has been shown that for lower heat flux density bubble growths in an almost quiescent bulk of liquid. For higher heat flux density the train of bubbles creates a vapour column with strong wake effect. Maximum liquid velocity recorded is approximately equal to the terminal velocity of bubble rising in a stagnant liquid.
Volume 2: Symposia and General Papers, Parts A and B, 2002
The effect of bubbles on the evolution of vortical flows near a wall are studied by direct numerical simulations, using a finite volume/front tracking technique that accounts fully for the effect of fluid inertia, viscosity, bubble deformability, and surface tension. Two problems have been studied. In one, the interaction of bubbles with a welldefined vortical flow, consisting of a parabolic velocity profile and a pair of counter-rotating straight vortex filaments near a wall, parallel to the flow direction, is followed. For a wide range of injection sites and bubble sizes, as well as for different number of bubbles, the motion of the bubbles into the vortex core leads to a cancellation of the original vorticity with secondary wall vorticity, resulting in a small transient reduction of the wall shear. In the other study, bubbles are injected near the wall in a turbulent channel flow. The evolution of the bubbles and the modification of the flow is followed as the bubbles migrate away from the wall.
2014
The microbubble content in the wake of a cavitating hydrofoil is investigated in a variable pressure water tunnel using longrange microscopy shadowgraphy. A 200 mm span, 120 mm base-chord NACA 63A015 section elliptical planform hydrofoil was mounted at 3.5 • incidence in a 0.6 m square tunnel test section. The microbubbles generated by the cavitation in the hydrofoil wake at a Reynolds number of 0.5×10 6 and a cavitation number of 0.37 were characterised at several locations. The bubble content was photographed at three locations downstream of the trailing edge, and five spanwise and three transverse locations. Measurements were made downstream of the region where shed vortices from the cavity trailing edge are still visible. The bubbles were back-lit using diffused laser lighting and images captured with a CCD camera. The image resolution was approximately 2 µm/pixel. The dominant bubble size in the wake was found to range between 25 and 40 µm depending on location. Bubbles larger than 200 µm are evident in the wake but not well captured with these tests. Additional tests with a higher magnification are required to image bubbles below 20 µm.
Journal of Fluid Mechanics, 2004
A simultaneous technique employing particle image velocimetry (PIV) and shadowgraphy was used to study vertical slug flow in non-Newtonian fluids. Two aqueous solutions of 0.8 and 1.0 wt% carboxymethylcellulose (CMC) were studied and the flow field around individual Taylor bubbles fully characterized. The rheological fluid properties and pipe dimension yielded Reynolds numbers of 8 and 4 and Deborah numbers of 0.2 and 0.4. A negative wake was found downstream of the Taylor bubbles in both fluids. Below the bubble trailing edge, along the axis region, the fluid flows in the opposite direction to the bubble (negative wake), originating rotational liquid movements in adjacent regions. Even far downward from the bubble, rotational liquid movements are clearly seen and measured. In the 1.0 wt% CMC solution, the bubble trailing edge has the shape of a two-dimensional cusp. This two-dimensional cusp, of small dimensions, is seen in different orientations during the bubble riseindicating a fast rotational movement. The asymmetrical shape of the trailing edge is responsible for small asymmetries in the flow in the wake region (three-dimensional flow). The asymmetrical shape associated with the rotational movement is responsible for an unsteady flow of small amplitude. In the 0.8 wt% CMC solution, the shape of the trailing edge changes during the bubble rise. An axisymmetric axial oscillation a continuous expansion and contraction of the trailing edge, is the origin of this behaviour. This oscillatory movement is responsible for an unsteady flow of small amplitude in the wake region.
Journal of Mechanical Science and Technology, 2010
The spatial and temporal structures of turbulent water flows driven by air bubbles in a rectangular water tank were investigated. The time-resolved particle image velocimetry (PIV) technique was adopted for quantitative visualization. Flow rates of compressed air were changed from 2 to 4 ℓ/min at 0.5 MPa, and the corresponding range of bubble-based Reynolds number ranged from 6,740 to 13,220. The dynamics of flow structures was further investigated by the time-resolved proper orthogonal decomposition (POD) analysis technique. When the flow rate was increased, the main vortex core moved to the side and bottom wall. Locations of peak turbulent kinetic energy regions depended on the bubble Reynolds number. Both spatial and temporal modes were quite different with respect to the flow rates. The first temporal mode was harmonized with the second temporal mode, with small oscillations in the case of the lowest Reynolds number. However, temporal modes oscillate with higher frequencies when the Reynolds number increases. Based on the result of the FFT analysis of each temporal mode, we conjectured that low-frequency oscillation was attributed to the recirculating flow, whereas a higher dominant frequency was related to the vibration of the free surface that interacts with the rising bubbles.
Experiments in Fluids, 2000
The particle tracking velocimetry measurement technique was used to measure the whole-volume, threedimensional, transient velocity ®eld generated by a single air bubble rising in stagnant water in a small diameter pipe. The three-dimensional¯ow ®eld was reconstructed using a stereoscopic technique. Conditional averages of the velocity ®elds for the situations when the bubble rises at the center of the pipe, and close to the pipe wall, were determined. The turbulent motion generated in the continuous liquid phase for both situations was studied.
Heat and Mass Transfer, 2017
Both vapour and gas bubbles are known to significantly increase heat transfer rates between a heated surface and the surrounding fluid, even with no phase change. The cooling structures observed are highly temporal, intricate and complex, with a full description of the surface cooling phenomena not yet available. The current study uses high speed infrared thermography to measure the surface temperature and determine the convective heat flux enhancement associated with the interaction of a single air bubble with a heated, inclined surface. This process can be discretised into the initial impact, in which enhancement levels in excess of 20 times natural convection are observed, and the subsequent sliding behaviour, with more moderate maximum enhancement levels of 8 times natural convection. In both cases, localised regions of suppressed heat transfer are also observed due to the recirculation of warm fluid displaced from the thermal boundary layer with the surface. The cooling patterns observed herein are consistent with the interaction between an undulating wake containing multiple hairpin vortex loops and the thermal boundary layer that exists under the surface, with the initial nature of this enhancement and suppression dependent on the particular point on its rising path at which the bubble impacts the surface.
Computers & Fluids, 2005
The results of large eddy simulations (LES) of turbulent bubbly wake flows are presented. The LES technique was applied together with the Lagrangian particle dynamics method and a random flow generation (RFG) technique to the cases of a two-phase bubbly mixing layer and the high-Reynolds number bubbly ship-wake flows. The validation was performed on the experimental data for the bubbly mixing layer. Instantaneous distributions and probability density functions of bubbles in the wake were obtained using a joint LES/RFG approach. Separate estimates of bubble decay due to dissolution and buoyancy effects were obtained. The analysis of bubble agglomeration effects was done on the basis of experimental data for a turbulent vortex to satisfy one-way coupling that is used in this study.
Journal of Fluid Mechanics, 1997
A novel wake structure, observed as penny-shaped air bubbles rise at moderate Reynolds number through a thin layer of water bound between parallel glass plates inclined at a shallow angle relative to the horizontal, is reported. The structure of the wake is revealed through tracking particles suspended in the water. The wake completely encircles the rising bubble, and is characterized by a reverse surface flow or ‘edge jet’ which transports fluid in a thin boundary layer along the bubble surface from the tail to the nose at speeds which are typically an order of magnitude larger than the bubble rise speed. A consistent physical explanation for the wake structure is proposed. The wake is revealed to be a manifestation of the three-dimensionality of the flow in the suspending fluid. The bubble surface advances through a rolling motion, thus generating regions of surface divergence and convergence at, respectively, the leading and trailing edges of the bubble. A nose-to-tail gradient i...
Journal of physics, 2016
Home Search Collections Journals About Contact us My IOPscience You may also be interested in: Influence of forced convection on solidification and remelting in the developing mushy zone M Wu, A Vakhrushev, A Ludwig et al. Numerical investigation of forced convection of nano fluid flow in horizontal U-longitudinal finned tube heat exchanger S M Qasim, A F A Sahar and A A Firas Analytic study of the temperature profile in a copper bromide laser I P Iliev, S G Gocheva-Ilieva and N V Sabotinov Kinetics modeling of the drying of sunflower stem (Helianthus annuus L.) in a forced convection tunnel R López, M Vaca, H Terres et al. Between inertia and viscous effects: Sliding bubbles beneath an inclined plane C. Dubois, A. Duchesne and H. Caps Sliding bubble dynamics and the effects on surface heat transfer B Donnelly, A J Robinson, Y M C Delauré et al. Experiment on nucleate pool boiling in microgravity by using transparent heating surface-Analysis of surface heat transfer coefficients C Kubota, O Kawanami, Y Asada et al.
International Journal of Heat and Mass Transfer, 2015
Freely rising and sliding bubbles have been found to increase local heat transfer coefficients from adjacent heated surfaces. The latter have been exploited in various industrial applications, such as shell and tube heat exchangers and chemical reactors. Although there is a relatively large body of work on bubbles, only a very small portion of this focuses on sliding bubbles. The current study intends to expand this by understanding both the motion and surface heat transfer characteristics of sliding bubbles. Herein, results are presented on bubbles of 4.75-9.14 mm equivalent spherical diameter sliding under both a heated and unheated surface, inclined at 30 relative to the horizontal. The sliding bubble path and shape oscillations are observed by a pair of high speed cameras. The frequency and amplitude of these oscillations are derived from analysis of the acquired images. Heat transfer is measured using a high speed infra-red camera synchronised to the video cameras, which is spatially and temporally aligned with the high speed images, allowing for the relationship between bubble motion and heat transfer to be observed. It has been found that bubbles in the range tested exhibit a sinusoidal motion. This motion is likely linked to the asymmetrical generation and shedding of vortices, with one vortex shed for each half period of path oscillation. It was observed that the bubble shape fluctuations were closely linked to the path oscillations and therefore vortex shedding. At higher bubble volumes, the bubble interface was found to recoil after a vortex is shed. There is little difference between bubble motion on a heated and unheated surface at lower bubble volumes, but at higher volumes a thinning of the bubble tips is observed along with a less-smooth interface, both of which are attributed to the thermal boundary layer at the surface. The bubble drag coefficient is also decreased when the surface is heated. Two-dimensional, time-varying surface heat transfer patterns reveal local heat transfer coefficient enhancements of up to 8 times that corresponding to natural convection levels, while the global surface-averaged heat transfer coefficient was up to twice that of natural convection. The mechanism of this heat transfer enhancement is a combination of forced convection by the sliding bubble and vortices shed at half the bubble path oscillation frequency that draw cool fluid from the bulk towards the surface. In the far wake, these vortices form isolated, elliptical regions of cooling that remain for many seconds after the bubble has passed. Interestingly, there are regions of the bubble wake where the heat transfer coefficient briefly drops below natural convection levels, highlighting the complexities of the fluid mechanics behind multiphase cooling.
2015
Two-phase bubbly flows are widely applied in engineering and environmental processes. The interaction of the dispersed phase with the continuous phase has a great effect on transfer processes between the phases. The interstitial relative velocities between the phases and the interfacial area and the shape of the dispersed phase are the key dependent parameters in the drag, heat and mass transfer between the phases. Although the physical understanding of bubbles rise in a liquid is a significant practical importance in many areas of engineering, neither the interactions between bubbles in clusters nor the bubble-induced pseudo-turbulence (i.e., the generation of velocity fluctuations by bubbles and their wakes in a laminar flow) are fully understood. The modeling of bubbly flows with the Computational Fluid Dynamics (CFD) codes requires detailed information about the full field velocity close to the bubble and its wake. Such information is not widely available. Experimental data exis...
A hybrid scheme combining Particle Image Velocimetry and Shadow Image Velocimetry has been used for a full-volume, three-dimensional, transient study of the shape, trajectory and forces acting on air bubbles rising in stagnant tap water in restricted media. The bubble Reynolds number ranged from 400 to 650. The three-dimensional reconstruction of the bubble was accomplished by combining images from two orthogonal views. This reconstruction process allowed for measurement of dimensions, orientation, trajectory, rotation, velocity and acceleration of an individual rising bubble. These parameters were then used to compute drag and lift forces acting on the bubble. Instantaneous values of drag and lift coefficients were then determined. These experimental results were compared to known experimental data and values obtained from correlations found in scientific literature. It was found that correlations intended for determining drag coefficient values should be adequately modified when necessary to account for wall impact, since the drag coefficient magnitude is considerably higher than that predicted by such correlations at Re below 550. Regarding the bubble lift coefficient, instantaneous data scatter noticeably as a function of Re, but average values agree within the range of known data. The major contributors to the uncertainty in this experiment were the capability of accurately reconstructing the 2D shape of the bubbles from distorted and/or incomplete PIV images and determining the bubble centroid. An overall error of 7% was computed for the drag coefficient, but it rises up to 44% for the lift coefficient.
Journal of physics, 2012
An investigation into the effects of a single sliding air bubble on heat transfer from a submerged, inclined surface has been undertaken. Existing literature has shown that both vapour and gas bubbles can increase heat transfer rates from adjacent heated surfaces. However, the mechanisms involved are complex and dynamic and in some cases poorly understood. The present study utilises high speed, high resolution, infrared thermography and video photography to measure two dimensional surface heat transfer and three dimensional bubble position and shape. This provides a unique insight into the complex interactions at the heated surface. Bubbles of volume 0.05, 0.1, 0.2 and 0.4 ml were released onto a surface inclined at 30 degrees to horizontal. Results confirmed that sliding bubbles can enhance heat transfer rates up to a factor of 9 and further insight was gained about the mechanisms behind this phenomenon. The enhancement effects were observed over large areas and persisted for a long duration with the bubble exhibiting complex shape and path oscillations. It is believed that the periodic wake structure present behind the sliding bubble affects the bubble motion and is responsible for the heat transfer effects observed. The nature of this wake is proposed to be that of a chain of horseshoe vortices. 2 The work presented in this paper was performed by the author during his time in Trinity College Dublin under the supervision of Prof. D B Murray as part of his Ph.D research.
Loading Preview
Sorry, preview is currently unavailable. You can download the paper by clicking the button above.