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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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7.2 Bubbles dynamics and boiling 381<br />

Figure 7.2.18. Growth <strong>of</strong> vapor bubbles on the heating surface at high (a) and low (b) pressures. [Reprinted from<br />

S.P. Levitsky, B.M. Khusid and Z.P. Shulman, Int. J. Heat Mass Transfer, 39, 639, Copyright 1996, the reference<br />

66, with permission from Elsevier Science]<br />

with manifestation <strong>of</strong> elastic properties <strong>of</strong> the solution at vapor bubble growth on the heating<br />

surface. 66<br />

The general character <strong>of</strong> the bubbles evolution at boiling under atmospheric and<br />

subatmospheric pressures, respectively, is clarified schematically in Figure 7.2.18. In the<br />

first case (at high pressures) the base <strong>of</strong> a bubble does not “spread” 67 but stays at the place <strong>of</strong><br />

its nucleation. Under such conditions the decrease in the curvature <strong>of</strong> the bubble surface<br />

with time, resulting from the increase in bubble radius, R, leads to liquid displacement from<br />

the zone between the lower part <strong>of</strong> the microbubble and the heating surface. This gives rise<br />

to the local shear in a thin layer <strong>of</strong> a polymer solution. A similar shear flow is developed also<br />

in the second case (at low pressures), when a microlayer <strong>of</strong> liquid is formed under a<br />

semi-spherical bubble. As known, at shear <strong>of</strong> a viscoelastic fluid appear not only tangential<br />

but also normal stresses, reflecting accumulation <strong>of</strong> elastic energy in the strained layer (the<br />

Weissenberg effect 3 ). The appearance <strong>of</strong> these stresses and elastic return <strong>of</strong> the liquid to the<br />

bubble nucleation center is the reason for more early detachment <strong>of</strong> the bubble from the<br />

heating surface, reduction in its size and growth in the nucleation frequency. All this ultimately<br />

leads to enhancement <strong>of</strong> the heat transfer.<br />

The above discussion permits to explain the experimental results. 61 Their reasons are<br />

associated with substantial differences in the conditions <strong>of</strong> boiling on a thin wire and a plate<br />

or a tube. Steam bubbles growing on a wire have a size commensurable with the wire diameter<br />

(the growing bubble enveloped the wire 61 ). This results in sharp reduction <strong>of</strong> the boundary<br />

layer role, the same as the role <strong>of</strong> the normal stresses. Besides, the bubble growth rate on<br />

a wire is smaller than on a plane (for a wire R~t n where n < 1/4). 67<br />

The elastic properties <strong>of</strong> the solution are responsible also for stabilization <strong>of</strong> the spherical<br />

shape <strong>of</strong> bubbles observed in experiments on boiling and cavitation. Finally, the observed<br />

reduction in a coalescence tendency and an increase in the bubble sizes uniformity<br />

can also be attributed to the effects <strong>of</strong> normal stresses and longitudinal viscosity in thin<br />

films separating the drawing together bubbles.<br />

The linkage between the enhancement <strong>of</strong> heat transfer at boiling <strong>of</strong> dilute polymer solutions<br />

and the elastic properties <strong>of</strong> the system is confirmed by the existence <strong>of</strong> the optimal<br />

concentration corresponding to α max (Figure 7.2.14). Similar optimal concentration was established<br />

in addition <strong>of</strong> polymers to water to suppress turbulence - the phenomenon that also<br />

owes its origin to elasticity <strong>of</strong> macromolecules. 1,3,9 Therefore, it is possible to expect that the<br />

factors favoring the chain flexibility and increase in the molecular mass, should lead to<br />

strengthening <strong>of</strong> the effect.<br />

The data on boiling <strong>of</strong> concentrated polymeric solutions 20 demonstrate that in such<br />

systems thermodynamic, diffusional, and rheological factors are <strong>of</strong> primary importance.

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