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A B C D E F G H I J K L M N O P
Packaged units, specification of, Packing characteristic, in cooling towers, Packings, for cooling towers Packings, for fixed beds: Packinox heat exchanger, Paints, spectral characteristics of reflectance of surfaces treated with, Palen, J W Panchal, C B, Paraffins, normal and isonormal: Paraldehyde: Parallel channel instability, in condensers, Partial boiling in subcooled forced convective heat transfer, Participating media, radiation interaction in, Particle convective component, in heat transfer from fluidized beds, Particle emissivity, Particle Reynolds number in fixed beds, Particles: Particulate fluidization, Particulate fouling, Pass arrangements, in plate heat exchangers, Passes, tube side, Passive methods, for augmentation of heat transfer, passive systems for: PD5500 mechanical design of shell-and-tube heat exchangers to, Peacock, D K, Pearson number, Peclet number Peng-Robinson equation of state, application to hydrocarbons, Penner's rule, in absorption of radiation by gases, Pentachloroethane (Refrigerant 120): Pentadecane: Pentadecene: Pentadiene 1, 2: Pentadiene 1, trans 3: Pentadiene 1, 4: Pentadiene 2-3: Pentafluoroethane (Refrigerant 125) Pentamethylbenzene: Pentane: Pentanoic acid: 1-Pentanol: 1-Pentene: cis-2-Pentene: trans-2-Pentene: Pentylacetate: Pentylbenzene: Pentylcyclohexane: Pentylcyclopentane: Pentylcyclopropane, liquid properties, Perforated fins, in plate fin heat exchangers, Perforated plates, loss coefficients in, Periodic operation, of regenerator, Periodic variations in temperature, thermal conduction in bodies with, PFR correlation, for heat transfer in high fin tube banks, Pharmaceutical industry, fouling of heat exchangers in, Phase change materials, in augmentation of heat transfer, Phase change number, Phase equilibrium: Phase inversion Phase separation, as source of corrosion problems, Phenol: Phenols: Phenylhydrazine: Phonons, in thermal conductivity of solids, Phosgene: Physical properties: Pi theorum, in dimensional analysis, Pinch analysis, for heat exchanger network design, Pioro, I L Pioro, LS, Pipe leads, Piperidine: Pipes, circular: Pipes, noncircular: Piping components: Pitting corrosion, in stainless steels, Planck's constant, Planck's law, for spectral distribution of blackbody radiation, Plane shells, steady-state thermal conduction in, Plastic deformation Plate fin heat exchangers Plate fins, efficiency, Plate heat exchangers: Plate evaporator Plates: Plug flow: Plug flow model, for furnaces, Pneumatic conveyance, Pneumatic conveying dryer, P-NTU method: Polarization, of thermal radiation, Polyglycols, as heat transfer media, Polymers: Pool boiling, Porous surfaces: Port arrangements, in plate heat exchangers, Portable fouling unit, Poskas, P, Postdryout heat transfer: Powders: Power law fluid (non-Newtonian), Power plant: Prandtl number Precipitation (crystallization) fouling, Precipitation hardening, of stainless steels, Pressure coefficient: Pressure control of condensers, Pressure drop: Pressure gradient: Pressure, specification of in mechanical design to EN13445, Pressure testing, Pressure vessels, principle codes for, Pressurised water reactor, fouling in, Printed circuit heat exchanger, Problem table algorithm, in pinch analysis, Process heaters: Progressive plastic deformation Prolate spheroids, free convective heat transfer from, Promoters, in dropwise condensation, Propadiene: Propane: 1-Propanol: 2-Propanol: Propeller agitator, Property ratio method, for temperature dependent physical property Propionaldehyde: Propionic acid: Propionic anhydride: Proprionitrile: Propyl acetate: Propylamine: Propylbenzene: Propylcyclohexane: Propylcyclopentane: Propylene: 1,3-Propylene glycol: Propylene oxide: Propyl formate: Propyl propionate: Pseudo-boiling in supercritical fluids, Pseudo-film boiling in supercritical fluids, Pseudocritical pressure, Pseudocritical tempertaure, Pugh, S F Pulp and paper industry, fouling of heat exchangers in, Pulsations, use in augmentation of heat transfer, Pulverized fuel water-tube boiler, Pumping, lost work in, Pushkina and Sorokin correlation, for flooding in vertical tubes, Pyramid, free convective heat transfer from, Pyridine:
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Boiling of Binary and Multicomponent Mixtures: Pool Boiling

DOI 10.1615/hedhme.a.000197

2.7 BOILING AND EVAPORATION
2.7.7 Boiling of binary and multicomponent mixtures: Pool boiling

The pool boiling curve is considerably altered when the fluid being evaporated is a binary mixture rather than a pure single-component liquid. The principal changes are shown diagramatically in Figure 1. First, the onset of boiling is delayed to higher wall superheats as a result of the temperature gradients set up in the pool to accommodate the corresponding gradients in liquid composition. Heat transfer coefficients in the nucleate boiling region are sharply reduced. The critical heat flux may be increased or reduced depending on the extent of the contribution from convection in the pool. The minimum heat flux and the corresponding wall superheat are increased. Finally, heat transfer rates in the film boiling region are also somewhat higher.

A. Nucleate boiling

Even small amounts of a second component cause considerable reductions in the heat transfer rate under nucleate pool boiling conditions compared with that measured for the pure liquid. The reason for this reduction can be traced back to the influence of the second component on the bubble growth rate. The minimum bubble growth rate, the minimum heat transfer coefficient, and the occurrence of a maximum critical heat flux all occur at the same liquid composition corresponding to a maximum value of | - |. Starting with the early work of Bonilla and Perry (1941) and Cichelli and Bonilla (1944), many experimental studies of pool boiling of binary mixtures have been published. A good deal of useful experimental data for nucleate pool boiling of binary liquids have been presented by Sternling and Tichacek (1961). They used 14 binary systems with components ranging from water to light alcohols to heavy oils. All the mixtures had a wide boiling range, at least 90 °C. For all the systems the heat transfer coefficient for a given heat flux was less than would be expected for an "ideal" single-component fluid with the same physical properties. Extensive reviews on multicomponent pool boiling are given by Shock (1982) and Collier and Thome (1994). Here, the effects are illustrated by citing a few examples. It is helpful to define a heat transfer coefficient for nucleate pool boiling of a binary mixture as follows:

\[\label{eq1} \alpha=\dfrac{\dot{q}}{(T_{\rm{w}}-T_{\rm{bub}})}\tag{1}\]

where is the heal flux, Tw the wall temperature and Tbub the bubble point temperature. For a binary mixture, one may define an "ideal" heat transfer coefficient αid as follows:

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