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Baffle leakage in shell-and-tube heat exchangers: Baffles in shell-and-tube heat exchangers: Baker flow regime map for horizontal gas-liquid flow, Balance equation (applied to complete equipment), Band dryer: Bandel and Schlunder correlations, for boiling in horizontal tubes, Basket-type evaporator, Barbosa, J R Jr, Bateman, G, Bayonet tube heat exchangers, constructional features of, Bayonet tube evaporators, Beaton, C F, Beer-Lambert law, Bejan, A, Bell-Delaware method for shell-side heat transfer and pressure drop in shell-and-tube heat exchangers, Bell and Ghaly method for calculation of multicomponent condensation, Benard cells in free convection in horizontal fluid layers, Bends: Benzaldehyde: Benzene: Benzoic acid: Benzonitrile: Benzophenone: Benzyl alcohol: Benzyl chloride: Berenson equation for pool film boiling from a horizontal surface, Bergles, Arthur E, Bernoulli equation, application to flow across cylinders, Bimetallic tubes: Binary mixtures: Bingham fluid (non-Newtonian), Biofouling, Biot number: Biphenyl: Bismarck A, Black liquor, in pulp and paper industry, fouling of heat exchangers by, Black surface: Blackbody radiation, Blades, in scraped surface heat exchangers, Blake-Carmen-Kozeny equation, Blasius equation for friction factor, Blenkin, R, Blunt bodies, drag coefficients for, Boilers: Boiling: Boiling curve: Boiling length: Boiling number, definition, Boiling point, normal, Boiling range (in multicomponent mixtures): Boiling surface in boiling in vertical tubes, Boiling Water Reactor (BWR), fouling problems in, Bolted channel head in shell-and-tube exchanger, Bolted cone head in shell-and-tube heat exchanger, Bolted joints, thermal contact resistance in, Bolting, Bolting of flanges in shell-and-tube heat exchangers, Boltzmann's constant, Bonnet head, in shell-and-tube heat exchanger, Borishanski, V M, Borishanski correlation for nucleate pool boiling, Bott, T R, Boundary layer: Boussinesq approximations: Boussinesq number, definition, Bowring correlations for critical heat flux, Bracket supports for heat exchangers: Brauner, N, Brazed plate exchanger, Brazing in plate fin heat exchanger construction, Bricks, drying of, Brine recirculation, in multistage flash-evaporation, Brinkman number, Brittle fracture, Bromine: Bromley equation for film boiling from horizontal cylinders, Bromobenzene: Bromoethane: Bromomethane: Bromotrifluoromethane (Refrigerant 13B1): Brush and cage system, for fouling mitigation, BS 5500 code for mechanical design of shell-and-tube heat exchangers (see also PD 5500), Bubble crowding as mechanism of critical heat flux, Bubble flow: Bubbles: Bulk viscosity, Bundle-induced convection in kettle reboilers, Bundle layout, in condensers Buoyancy effects: Buoyancy-induced flow in channels, free convective heat transfer with, Busemann-Crocco integral, application in boundary layer equations, 1,2-Butadiene: 1,3-Butadiene: Butane: 1-Butanol: 2-Butanol: Butene-1: cis-2-Butene: trans-2-Butene: Butterworth, D, Butyl acetate: t-Butyl alcohol: Butylamine: Butylbenzene: n-Butylbenzene: n-Butylcyclohexane: Butylcyclopentane: Butylene oxide: Butyr-aldehyde: Butyric acid: Butyronitrile: Bypass (shell-and-tube bundle):
C D E F G H I J K L M N O P Q R S T U V W X Y Z

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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