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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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7.2 Bubbles dynamics and boiling 379<br />

In view <strong>of</strong> the discussed results, the work 61 attracts special attention since it contains<br />

data on boiling <strong>of</strong> dilute solutions, opposite to those reported earlier. 56-60 The addition <strong>of</strong><br />

PAA, PEO and HEC to water in concentrations, corresponding to the viscosity increase up<br />

toηp= 1.32×10 -3 Pas, has brought about reduction in heat transfer. The boiling curve in coordinates<br />

q (heat flux) vs. ΔT displaced almost congruently to the region <strong>of</strong> larger ΔT values<br />

with c (Figure 7.2.17a). It was demonstrated 61 that the observed decrease in α with addition<br />

<strong>of</strong> polymer to water can be both qualitatively and quantitatively (with the Rohsenow pool<br />

boiling correlation for the heat transfer coefficient 62 ) associated with the increase in the solution<br />

viscosity (Figure 7.2.17, b). The experiments 61 were performed using a thin platinum<br />

wire with diameter 0.3 mm.<br />

Explanation <strong>of</strong> experimental data needs more detailed discussion <strong>of</strong> physical factors<br />

that can reveal themselves in boiling <strong>of</strong> polymeric solutions. They include possible changes<br />

in capillary forces on interfaces in the presence <strong>of</strong> polymeric additives; absorption <strong>of</strong><br />

macromolecules on the heating surface; increase in the number <strong>of</strong> weak points in the solution,<br />

which facilitates increase in the number <strong>of</strong> nuclei; thermodynamic peculiarities <strong>of</strong> the<br />

polymer-solvent system; the effect <strong>of</strong> macromolecules on the diffusion mass transfer in<br />

evaporation <strong>of</strong> solvent; hydrodynamics <strong>of</strong><br />

convective flows in a boiling layer and the<br />

motion <strong>of</strong> bubbles; manifestation <strong>of</strong> rheological<br />

properties <strong>of</strong> solution.<br />

The capillary effects were indicated as<br />

one <strong>of</strong> the reasons for the intensification <strong>of</strong><br />

heat transfer, since many polymers (in particular,<br />

HEC, PEO, etc.), 63<br />

similar to<br />

Figure 7.2.16. Heat transfer coefficient for nucleate pool<br />

boiling <strong>of</strong> PEO aqueous solutions. (p f0 = 9.8×10 3 Pa).<br />

Curve 1 corresponds to pure water, for curves2-7, c=<br />

0.01, 0.02, 0.04, 0.08, 0.16 and 1.28%, respectively.<br />

[Adapted, from S.P. Levitsky, and Z.P. Shulman, Bubbles<br />

in polymeric liquids, Technomic Publish. Co.,<br />

Lancaster, 1995, with permission from Technomic Publishing<br />

Co., Inc., copyright 1995]<br />

low-molecular surfactants, 64 are capable <strong>of</strong><br />

decreasing the surface tension. As a result,<br />

they decrease both the work <strong>of</strong> the nucleus<br />

formation, W cr, and the critical size <strong>of</strong> bubble,<br />

R cr:<br />

Figure 7.2.17. Boiling curves for aqueous solutions <strong>of</strong> PAA Separan AP-30. (a) experimental data; for curves1-6<br />

η r = 1.00, 1.01, 1.04, 1.08, 1.16 and 1.32, correspondingly; (b) calculations made with the use <strong>of</strong> the Rohsenow<br />

pool boiling correlation; for curves1-5,η r= 1.00, 1.01, 1.04, 1.16 and 1.32, respectively (η r = η p/η s). [By permission<br />

from D.D. Paul, and S.I. Abdel-Khalik, J. Rheol., 27, 59, 1983, reference 61]

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