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Transport Phenomena.pdf

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§1.6 Viscosity of Suspensions and Emulsions 31<br />

fluid and are simply related to the internal energy of vaporization at the normal boiling<br />

point, as follows: 3 AGj « 0.408 AU vap<br />

(1.5-8)<br />

By using this empiricism and setting 8/a = 1, Eq. 1.5-7 becomes<br />

11 = Щехр 0.408 ALZ vap<br />

/RT) (1.5-9)<br />

The energy of vaporization at the normal boiling point can be estimated roughly from<br />

Trouton's rule<br />

AL/ vap<br />

- AH vap<br />

- RT b<br />

= 9ART b<br />

With this further approximation, Eq. 1.5-9 becomes<br />

(1.5-10)<br />

p V D (1.5-11)<br />

Equations 1.5-9 and 11 are in agreement with the long-used and apparently successful<br />

empiricism jx = Л ехр(В/Т). The theory, although only approximate in nature, does give<br />

the observed decrease of viscosity with temperature, but errors of as much as 30% are<br />

common when Eqs. 1.5-9 and 11 are used. They should not be used for very long slender<br />

molecules, such as n-C 2<br />

oH 4<br />

2.<br />

There are, in addition, many empirical formulas available for predicting the viscosity<br />

of liquids and liquid mixtures. For these, physical chemistry and chemical engineering<br />

textbooks should be consulted. 4<br />

EXAMPLE 1.5-1<br />

Estimation of the<br />

Viscosity of a Pure<br />

Liquid<br />

Estimate the viscosity of liquid benzene, QH 6<br />

, at 20°C (293.2K).<br />

SOLUTION<br />

Use Eq. 1.5-11 with the following information:<br />

V = 89.0cm 3 /g-mole<br />

T b<br />

= 80.1 °C<br />

Since this information is given in c.g.s. units, we use the values of Avogadro's number and<br />

Planck's constant in the same set of units. Substituting into Eq. 1.5-11 gives:<br />

(6.023 X 10 23 )(6.624 X 10" 27 ) /3.8 X (273.2 + 80.1))<br />

(89.0) ~ r V 293.2<br />

= 4.5 X 10" 3 g/cm-s or 4.5 X 10~ 4 Pa • s or 0.45 mPa • s<br />

§1.6 VISCOSITY OF SUSPENSIONS AND EMULSIONS<br />

Up to this point we have been discussing fluids that consist of a single homogeneous<br />

phase. We now turn our attention briefly to two-phase systems. The complete description<br />

of such systems is, of course, quite complex, but it is often useful to replace the suspension<br />

or emulsion by a hypothetical one-phase system, which we then describe by<br />

3<br />

J. F. Kincaid, H. Eyring, and A. E. Stearn, Chem. Revs., 28, 301-365 (1941).<br />

4<br />

See, for example, J. R. Partington, Treatise on Physical Chemistry, Longmans, Green (1949); or R. C.<br />

Reid, J. M. Prausnitz, and В. Е. Poling, The Properties of Gases and Liquids, McGraw-Hill, New York, 4th<br />

edition (1987). See also P. A. Egelstaff, An Introduction to the Liquid State, Oxford University Press, 2nd<br />

edition (1994), Chapter 13; and J. P. Hansen and I. R. McDonald, Theory of Simple Liquids, Academic Press,<br />

London (1986), Chapter 8.

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