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Vacuum equipment, operational problems of, Vacuum operation, of reboilers, Valle, A, Valves: Vaned bends, single-phase flow and pressure drop in, Vapor blanketing, as mechanism of critical heat flux, Vapor injection, effect of on boiling heat transfer in tube bundles, Vapor-liquid disengagement, in kettle reboilers, Vapor-liquid separation, for evaporators, Vapor mixtures, condensation of, Vapor pressure, Vapor recompression, in evaporation, Vaporization, choice of evaporator type for, Vaporizer, double bundle, constructional features, Vapors, saturation properties of, Vapors, properties of superheated, Vasiliev, L, Vassilicos, J C, Velocity defect law: Velocity distribution: Velocity fluctuations, in turbulent pipe flow, Velocity ratio (slip ratio): Venting of condensers Vertical condensers: Vertical cylindrical fired heater, Vertical pipes: Vertical surfaces: Vertical thermosiphon reboilers: Vessels of non-circular cross section, design to ASME VIII code, Vessels of rectangular cross section, EN13445 guidance for, Vetere method, for enthalpy of vaporisation, Vibrated beds, heat transfer to, Vibration: Vinyl acetate: Vinyl benzene: Vinyl chloride: Virial equation: Virk equation for maximum drag reduction, Visco-elastic fluids, flow of, Viscometric functions (non-Newtonian flow), methods of determining, Viscosity: Viscosity number (Vi), Viscous dissipation, influence on heat transfer in non-Newtonian flows, Viscous heat generation, in scraped sauce heat exchangers, Viscous sublayer, in duct flow, Void fraction, Voidage, in fixed beds, definition, Volumetric heat transfer coefficient, Volumetric mass transfer coefficient, von Karman friction factor equation for fully rough surface, von Karman velocity defect law, Vortex flow, in helical coils of rectangular cross section, Vortex flow model, for twisted tube heat exchangers, Vortex shedding:
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General Introduction

DOI 10.1615/hedhme.a.000223

2.12.1 General introduction

A. Introduction

In many technological processes, which deal with heat and mass transfer, two-phase flows consisting of liquid and gas are exploited. These two phases may be in different states, which depend on the hydrodynamic state of whole the system.

The foam state is one of the possible forms of gas- liquid system. The foam is generated when gas and liquid comes into contact.

Let us consider the structure of a vertical upward two-phase flow generated from a detergent solution (Figure 1). A structure of this two-phase system varies depending on the height of the flow channel. Directly on the plate exists the bubble or so-called barbotage regime. Near the plate a regime of dynamically stable foam (DSF) exists, which consists of a turbulent mixture of the gas and liquid flows. Dynamically stable or turbulent foam is a very unstable two-phase system. It exists only with gas feed to the distributor plate. If the delivery of gas stops, the turbulent foam immediately decays into pure liquid and gas (in the case where a foam is generated from a pure liquid) or in the case of the detergent solution it turns into the statically stable foam (SSF). For pure liquid only dynamically stable foam can be generated. From a detergent solution, both dynamically stable and statically stable foams can be generated. Statically stable foam (cellular foam) consists of gas bubbles, which have the shape of regular polygons, separated each from other by the thin liquid films. Even in the absence of gas delivery, SSF can exist for quite long periods of time (from seconds to days or years).

Figure 1 Foam generation scheme

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