1996
DOI: 10.1017/s0022112096007239
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Bubble shapes in rotating two-phase fluid systems: a thermodynamic approach

Abstract: A method is reported for predicting the shape of the phase boundary in two-phase isothermal constant-volume constant-mass rotating fluid systems. In contrast to previous methods that have employed the continuum concept of pressure, the proposed method uses the thermodynamic concept. The latter requires, in addition to the usual condition of a force balance existing at the boundary, that the equilibrium phase boundary shape be such that there is no net mass flux. The latter condition is imposed by requiring tha… Show more

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Cited by 7 publications
(4 citation statements)
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“…The Bashforth and Adams procedure is modified to impose the necessary conditions for thermodynamic equilibrium at the droplet apex. ,− The turning angle, ϕ, the radial position on the liquidvapor interface, y (ϕ), and the height of the liquid−vapor interface above the Cu substrate, z (ϕ) − z b , are indicated in Figure . We assume the liquid phase is axisymmetric.…”
Section: System Definitionmentioning
confidence: 99%
“…The Bashforth and Adams procedure is modified to impose the necessary conditions for thermodynamic equilibrium at the droplet apex. ,− The turning angle, ϕ, the radial position on the liquidvapor interface, y (ϕ), and the height of the liquid−vapor interface above the Cu substrate, z (ϕ) − z b , are indicated in Figure . We assume the liquid phase is axisymmetric.…”
Section: System Definitionmentioning
confidence: 99%
“…If the chemical potential in phase j is denoted as µ j , the potential energy per unit mass as ξ, a second condition for equilibrium may be written 28,29 where λ is a constant. For a system exposed to a gravitational field of intensity g and to a centrifugal field corresponding to an angular speed of ω, at a height z and radial position y, ξ may be written When eq 2 is applied at a position on a liquid-vapor interface, z and y have the same values in each phase; thus If the molar specific volume of the liquid at saturation is denoted as V f , the saturation vapor pressure as P s (T), the ratio of the liquid-phase pressure to the saturation vapor pressure as x L (y, z), and the isothermal compressibility as κ T , then provided |κ T P s [x L (y, z) -1]| , 1, the chemical potential in the liquid may be expressed If the vapor phase is approximated as an ideal gas:…”
Section: Contact Angle Dependence On the Pressure At The Three-phase ...mentioning
confidence: 99%
“…Each of the cylinders is assumed to be maintained isothermal while exposed to gravitational and centrifugal fields. A modified turning-angle method 28,31,32 was used to determine the functional relation between x 3 L and θ. The turning angle, φ, is indicated in Figure 1.…”
Section: Functional Relation Between X 3 L and θmentioning
confidence: 99%
“…Thus, the total Helmholtz function for this phase must be written as an integral over the solid volume, V s . Following the treatment of systems exposed to an external field, , one finds: where f s is the Helmholtz function of the solid per unit volume and may be written where u s and s s are the internal energy and entropy of the solid, respectively, each per unit volume, T is the temperature, and φ is the potential energy of a unit volume of solid arising from the field generated by the adsorbed molecules. The potential energy is assumed to be a function of the number of adsorbed molecules, N σ , and the distance of the solid volume element from the surface, z…”
Section: System Descriptionmentioning
confidence: 99%