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Ideal gas: Ilexan, heat transfer medium, Illingworth, A, Imbedded fins, Immersed bodies: Immersed tubes, in fluidized beds, heat transfer to, Immiscible liquids, condensation of vapors producing Impairment of heat transfer in combined free and forced convection in a vertical pipe, Imperfectly diffuse surfaces: Impingement damage in heat exchangers, Impingement plate: Impingement protection, in shell-and-tube heat exchangers, Impinging jets: Implicit equations, solution of Inclined enclosures, free convective heat transfer in, Inclined flow, effect of on heat transfer to cylinders, Inclined pipes: Inclined surfaces, free convective heat transfer from, Inconel, spectral characteristics of reflectance from oxidized surface of, Induced flow instabilities, in augmentation of heat transfer, Injection: Inlet effects in shell-and-tube heat exchangers, In-line tube banks: Inorganic compounds, solutions of, as heat transfer media, Inorganic substances: Instability, parallel channel, in condensers, Insulators, thermal conductivity of, Integral condensation: Integral finned tubes: Interaction coefficients in heat exchangers, Interaction parameters for binary systems, tables, Interfacial friction, in three-phase (liquid-liquid-gas) stratified flows, Interfacial resistance, in condensation, Interfacial roughness, relationships for, in annular gas-liquid flow, Interfacial shear stress, effect on filmwise condensation, on vertical surface, Intergrannular corrosion, of Intermating troughs, as corrugation design in plate heat exchangers, Intermittent flows: Internal heat sources, temperature distribution in bodies with, Internal heat transfer coefficient, use in transient conduction calculations, Internal reboilers (in distillation columns), characteristics advantages and disadvantages of, Internally finned tubes: International codes for pressure vessels, Interpenetrating continua (as representation of heat exchangers): Intertube velocity, in tube banks, Inviscid flow, compressible, with heat addition, Iodine: Iodobenzene: Iodoethane: Iodomethane: ISO codes for mechanical design of heat exchangers, Isobutane: Isobutanol: Isobutylamine: Isobutylformate: Isobutyric acid: Isoparaffins: Isopentane: Isopentanol: Isopropanol: Isopropylacetate: Isopropylamine: Isopropylbenzene: Isopropylcyclohexane: Isothermal flow, compressible, in ducts, Isothermal gas, radiation heat transfer to walls from, Isotropic materials, elastic properties, Isotropic scattering, Italy, guide to national practice for heat exchanger mechanical design,
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Liquid-Liquid-Gas Flow

DOI 10.1615/hedhme.a.000158

2.3.6 Three-phase liquid-liquid-gas flow

A. General description of three-phase flows: Flow patterns

This section discusses three-phase flows comprising a gas phase and two liquid phases. More specifically, the important case of gas, oil and water is described. Such flows relate to both gas-liquid and oil-water flows since these are limiting cases of the more-general three-phase flow. However, the inclusion of the third phase leads to a further degree of freedom and the interactions between the phases, already complex in two-phase flows, become even more complex.

Two-phase, gas-liquid and liquid-liquid flows are described in Section 154 and Section 157. In this section two-phase, gas-liquid and liquid-liquid flows will only be described as necessary for the three-phase flow descriptions.

In contrast to two-phase, gas-liquid flow, where many different kinds of models and semi-empirical relations have been presented over the last 40 years, the prediction models for three-phase, gas-liquid flow are very limited in number. The early investigators predicted three phase flow by modification of the liquid properties combined with the two-phase, gas-liquid models. Based on the experimental findings reviewed by Valle (1998) this approach to describing three phase flow is not sufficient on a general basis. In this section models and modified closure relations for three phase flow will be discussed for stratified flow and the extension to more complex flow patterns will be discussed.

For horizontal and slightly inclined pipes, four distinct gas-liquid flow patterns can be defined namely: stratified, annular, slug and bubbly flow.

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