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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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Corrosion and Other Types of Damage

DOI 10.1615/hedhme.a.000433

4.5.3 Corrosion and other types of damage

Heat exchangers may be subject to various modes of deterioration associated with flow such as erosion- corrosion, fretting, and fatigue, and they may suffer stress corrosion cracking (SCC) due to preexisting or imposed stress. These mechanically induced problems will be discussed first, and then some of the fluids that give rise to corrosion in exchangers will be considered.

A. Mechanically induced damage

There are three main types of wastage directly associated with liquid flow, as illustrated in Figure 1: cavitation, impingement, and erosion-corrosion.

Figure 1 Wastage due to stress. (a) Cavitation: collaps of bubbles at metal surface sets up a stress oscillation transverse to the surface,causing localized fatigue failure. (b) Impingement: a similar effect produced by liquid drops impinging on a surface. (c) Erosion-corrosion: transverse stress due to fluid flow causes rupture or thinning of protective film

(a) Cavitation

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