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May 2009

Volume 21, Issue 5, Articles (05xxxx)

Issue Cover Spotlight Figure

Phys. Fluids 21, 056602 (2009); http://dx.doi.org/10.1063/1.3140002 (10 pages)

R. D. Wordsworth
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back to top Interfacial Flows

Evaporation of a thin droplet on a thin substrate with a high thermal resistance

G. J. Dunn, S. K. Wilson, B. R. Duffy, and K. Sefiane

Phys. Fluids 21, 052101 (2009); http://dx.doi.org/10.1063/1.3121214 (7 pages) | Cited 8 times

Online Publication Date: 6 May 2009

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A mathematical model for the quasisteady evaporation of a thin liquid droplet on a thin substrate that incorporates the dependence of the saturation concentration of vapor at the free surface of the droplet on temperature is used to examine an atypical situation in which the substrate has a high thermal resistance relative to the droplet (i.e., it is highly insulating and/or is thick relative to the droplet). In this situation diffusion of heat through the substrate is the rate-limiting evaporative process and at leading order the local mass flux is spatially uniform, the total evaporation rate is proportional to the surface area of the droplet, and the droplet is uniformly cooled. In particular, the qualitative differences between the predictions of the present model in this situation and those of the widely used “basic” model in which the saturation concentration is independent of temperature are highlighted.
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47.55.D- Drops and bubbles
64.70.fm Thermodynamics studies of evaporation and condensation
68.03.Fg Evaporation and condensation of liquids

Sloshing of a layered fluid with a free surface as a Hamiltonian system

G. Sciortino, C. Adduce, and M. La Rocca

Phys. Fluids 21, 052102 (2009); http://dx.doi.org/10.1063/1.3121304 (16 pages)

Online Publication Date: 6 May 2009

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The aim of this paper is the investigation of a layered sloshing fluid system using both a new Hamiltonian mathematical model and new laboratory experiments. The mathematical model is defined for a cylindrical tank with an arbitrary shape and subjected to an arbitrary rigid motion. The model consists of a pure evolution system of partial differential first order equations in the canonical four unknowns: water elevation at the upper free surface and at the separation surface and the gap in momentum potential density computed at each fluid surface. The system of equations is obtained by avoiding the construction of the Hamiltonian and its variational derivatives. An important advantage of this formulation, with respect to the Lagrangian formulation, is that the nonevolution constraint, which imposes for each fluid the same velocity component along the normal direction of the separation surface, is fulfilled by the model itself. The model implementation needs to define the so-called Neumann–Dirichlet operators, which are computed by an efficient algorithm, for any instantaneous configuration of the two fluid domains. A numerical integration of the model is performed by a suitable Galerkin projection of the evolution equations. New laboratory experiments, simulating the sloshing of a layered fluid system, inside a tank with a squared cross section, were performed. The experiments, with a two-dimensional sloshing, were carried out by varying the forcing frequency, the oscillation amplitude and the ratio of the two fluids’ depths. In some experiments, a traveling wave, with a shape similar to a moving hydraulic jump, was observed at the separation surface. Measurements of the space-time evolution of both the free and the separation surfaces were performed and compared with the model’s predictions. A good agreement between the model predictions and laboratory measurements is found, even for strong nonlinear cases such as the traveling wave.
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47.15.Rq Laminar flows in cavities, channels, ducts, and conduits
47.11.-j Computational methods in fluid dynamics
47.35.-i Hydrodynamic waves

Inertia dominated drop collisions. I. On the universal flow in the lamella

Ilia V. Roisman, Edin Berberović, and Cam Tropea

Phys. Fluids 21, 052103 (2009); http://dx.doi.org/10.1063/1.3129282 (10 pages) | Cited 22 times

Online Publication Date: 11 May 2009

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This study is devoted to the analysis of inertia dominated axisymmetric drop collisions with a dry substrate or with another liquid drop. All the previous theoretical and semiempirical models of drop collisions are based on the assumption that the flow in the lamella and its thickness are determined by the impact conditions, mainly by the Reynolds and Weber numbers. In this study the existing experimental data are compared to existing and new numerical simulations for the shape of the lamella generated at the early times of drop impact for various impact conditions. The results show that if the Reynolds and Weber numbers are high enough, the evolution of the lamella thickness almost does not depend on the viscosity and surface tension. Therefore these results completely change our understanding of the flow generated by drop collisions. Moreover, we demonstrate that the theoretical models based on the approximation of the shape of the deforming drop by a disk and the models based on the energy balance approach are not correct. Finally, universal dimensionless distributions for the lamella thickness, velocity, and pressure are obtained from the numerical simulations of drop impact onto a symmetry plane (associated with the binary drop collisions). These universal distributions are valid for high impact Weber and Reynolds numbers.
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47.55.dr Interactions with surfaces
47.15.Cb Laminar boundary layers
47.11.-j Computational methods in fluid dynamics
68.05.-n Liquid-liquid interfaces
68.08.-p Liquid-solid interfaces

Inertia dominated drop collisions. II. An analytical solution of the Navier–Stokes equations for a spreading viscous film

Ilia V. Roisman

Phys. Fluids 21, 052104 (2009); http://dx.doi.org/10.1063/1.3129283 (11 pages) | Cited 20 times

Online Publication Date: 11 May 2009

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This study is devoted to a theoretical description of an unsteady laminar viscous flow in a spreading film of a Newtonian fluid. Such flow is generated by normal drop impact onto a dry substrate with high Weber and Reynolds numbers. An analytical self-similar solution for the viscous flow in the spreading drop is obtained which satisfies the full Navier–Stokes equations. The characteristic thickness of a boundary layer developed near the wall uniformly increases as a square root of time. An expression for the thickness of the boundary layer is used for the estimation of the residual film thickness formed by normal drop impact and the maximum spreading diameter. The theoretical predictions agree well with the existing experimental data. A possible explanation of the mechanism of formation of an uprising liquid sheet leading to splash is also proposed.
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47.55.dr Interactions with surfaces
47.10.ad Navier-Stokes equations
47.15.Cb Laminar boundary layers
47.55.nd Spreading films

The effective slip length and vortex formation in laminar flow over a rough surface

Anoosheh Niavarani and Nikolai V. Priezjev

Phys. Fluids 21, 052105 (2009); http://dx.doi.org/10.1063/1.3121305 (10 pages) | Cited 5 times

Online Publication Date: 11 May 2009

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The flow of viscous incompressible fluid over a periodically corrugated surface is investigated numerically by solving the Navier–Stokes equation with the local slip and no-slip boundary conditions. We consider the effective slip length which is defined with respect to the level of the mean height of the surface roughness. With increasing corrugation amplitude the effective no-slip boundary plane is shifted toward the bulk of the fluid, which implies a negative effective slip length. The analysis of the wall shear stress indicates that a flow circulation is developed in the grooves of the rough surface provided that the local boundary condition is no-slip. By applying a local slip boundary condition, the center of the vortex is displaced toward the bottom of the grooves and the effective slip length increases. When the intrinsic slip length is larger than the corrugation amplitude, the flow streamlines near the surface are deformed to follow the boundary curvature, the vortex vanishes, and the effective slip length saturates to a constant value. Inertial effects promote vortex flow formation in the grooves and reduce the effective slip length.
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47.45.Gx Slip flows and accommodation
47.15.Rq Laminar flows in cavities, channels, ducts, and conduits
47.32.-y Vortex dynamics; rotating fluids
83.50.Rp Wall slip and apparent slip
47.10.ad Navier-Stokes equations

Nonlinear regimes of anticonvection, thermocapillarity, and Rayleigh–Benard convection in two-layer systems

Ilya B. Simanovskii, Antonio Viviani, Frank Dubois, and Jean–Claude Legros

Phys. Fluids 21, 052106 (2009); http://dx.doi.org/10.1063/1.3139264 (11 pages) | Cited 1 time

Online Publication Date: 18 May 2009

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The nonlinear regimes of anticonvection and Rayleigh–Benard convection in a two-layer system with periodic boundary conditions on lateral walls in the presence of the interfacial heat release are studied. The region where anticonvective and the Rayleigh–Benard instability mechanisms act simultaneously is considered. The influence of the thermocapillary effect on anticonvective and Rayleigh–Benard flows, is investigated. New types of nonlinear traveling waves and modulated traveling waves are found.
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47.20.Bp Buoyancy-driven instabilities (e.g., Rayleigh-Benard)
47.55.N- Interfacial flows

Characterization of string cavitation in large-scale Diesel nozzles with tapered holes

M. Gavaises, A. Andriotis, D. Papoulias, N. Mitroglou, and A. Theodorakakos

Phys. Fluids 21, 052107 (2009); http://dx.doi.org/10.1063/1.3140940 (9 pages) | Cited 1 time

Online Publication Date: 21 May 2009

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The cavitation structures formed inside enlarged transparent replicas of tapered Diesel valve covered orifice nozzles have been characterized using high speed imaging visualization. Cavitation images obtained at fixed needle lift and flow rate conditions have revealed that although the conical shape of the converging tapered holes suppresses the formation of geometric cavitation, forming at the entry to the cylindrical injection hole, string cavitation has been found to prevail, particularly at low needle lifts. Computational fluid dynamics simulations have shown that cavitation strings appear in areas where large-scale vortices develop. The vortical structures are mainly formed upstream of the injection holes due to the nonuniform flow distribution and persist also inside them. Cavitation strings have been frequently observed to link adjacent holes while inspection of identical real-size injectors has revealed cavitation erosion sites in the area of string cavitation development. Image postprocessing has allowed estimation of their frequency of appearance, lifetime, and size along the injection hole length, as function of cavitation and Reynolds numbers and needle lift.
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47.55.D- Drops and bubbles
47.60.Kz Flows and jets through nozzles
47.32.-y Vortex dynamics; rotating fluids
47.80.Jk Flow visualization and imaging
47.11.-j Computational methods in fluid dynamics
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