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Handbook of Solvents - George Wypych - ChemTech - Ventech!

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370 Semyon Levitsky, Zinoviy Shulman<br />

Figure 7.2.6. Expansion <strong>of</strong> bubbles in water and POE<br />

aqueous solution at a pressure drop. (a) - water, (b) -<br />

solution <strong>of</strong> POE with c = 420 ppm. [By permission <strong>of</strong><br />

the American Institute <strong>of</strong> Physics from R.Y. Ting, and<br />

A.T. Ellis, Phys. Fluids., 17, 1461, 1974, the reference<br />

36]<br />

tively different from the concentration dependence<br />

<strong>of</strong> μ for a bubble in a pure viscous<br />

fluid with the same Newtonian viscosity as<br />

the solution (curve 7 in Figure 7.2.5).<br />

The rheological properties <strong>of</strong> polymeric<br />

solution highly depend on temperature.<br />

Therefore, its variation affects the<br />

bubble pulsations. Thermorheological features<br />

in bubble dynamics have been studied 35<br />

on the basis <strong>of</strong> temperature superposition<br />

principle, using relations [7.2.30], [7.2.31].<br />

It was shown that the temperature rise leads<br />

to decrease <strong>of</strong> the decrement Λ 3, and this effect<br />

is enhanced with the increase <strong>of</strong> n 1. Note<br />

that the higher is the equilibrium temperature<br />

<strong>of</strong> the liquid, the less sensitive are the Λ 3<br />

values to variations in n 1. It is explained by<br />

narrowing <strong>of</strong> the relaxation spectrum <strong>of</strong> the<br />

solution. 25<br />

Experimental results on bubble dynamics<br />

in solution <strong>of</strong> polymers are not numerous.<br />

Existing data characterize mainly the integral<br />

effects <strong>of</strong> polymeric additives on bulk<br />

phenomena associated with bubbles while<br />

only few works are devoted to studying the<br />

dynamics <strong>of</strong> an individual bubble. The observations<br />

<strong>of</strong> the bubble growth in water at a<br />

sudden pressure drop were compared with<br />

those for aqueous solution <strong>of</strong> POE. 36 The results are represented in Figure 7.2.6. It is seen<br />

that the effect <strong>of</strong> polymeric additives is small. This result is explained by rather large value<br />

<strong>of</strong> Reynolds number Re p =t 0/t p corresponding to experimental conditions. 36 Therefore, the<br />

inertial effects rather than the rheological ones play a dominant role in bubble dynamics.<br />

The conclusions 36 were confirmed later 37 when studying the bubbles behavior in aqueous<br />

solution <strong>of</strong> POE (trade mark Polyox WS 301) with the concentration <strong>of</strong> 250 ppm (for water<br />

1 ppm = 1 g/m 3 ). A similar result was received also in studies 38 <strong>of</strong> nucleate cavitation in the<br />

PAA aqueous solution with c = 0.1 kg/m 3 . The solution viscosity 38 only slightly (by 10%)<br />

exceeded that <strong>of</strong> water.<br />

When the polymer concentration (or molecular mass) is sufficiently high and viscosity<br />

<strong>of</strong> solution exceeds essentially that <strong>of</strong> solvent, the rheological effects in bubble dynamics<br />

become much more pronounced. In Figure 7.2.7, data 39 are presented for the relative damping<br />

decrement <strong>of</strong> free oscillations <strong>of</strong> air bubble with R 0 = 2.8 mm in aqueous solution <strong>of</strong><br />

POE via concentration. The dashed line represents theoretical values <strong>of</strong> the decrement, corresponding<br />

to Newtonian liquid with η = η p. The actual energy losses, characterized by experimental<br />

points, remained almost unchanged, despite the sharp rise in the “Newtonian”<br />

decrement, Λ p, with c. This result correlates well with the above theoretical predictions and<br />

it is explained by viscoelastic properties <strong>of</strong> the solution. The same explanation has the phe-

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