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McKay, Donald. "Front matter" Multimedia Environmental Models ...

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ments of resuspension rates are particularly difficult, because the resuspension event<br />

may be triggered periodically by a storm or flood or by an especially energetic fish<br />

chasing prey at the bottom of the lake. Regrettably, the sediment-water interface is<br />

not easily accessible, thus measurements are few, difficult, and expensive.<br />

Measurement of diffusion D values usually involves setting up a system in which<br />

there is a known fugacity driving force (f 1 – f 2) and the capacity to measure N,<br />

leaving the overall transport D value as the only unknown in the flux equation. A<br />

difficulty arises because, for a two-resistance in series system, it is impossible to<br />

measure the concentrations or fugacity at the interface; therefore, it is not possible<br />

to deduce the individual D values that combine to give the overall D value. The<br />

subterfuge adopted is to select systems in which one of the resistances dominates<br />

and that resistance can be equated to the total resistance. Guidance on chemical<br />

selection can be obtained from the location of the substance on Figure 7.7.<br />

Air phase mass transfer coefficients (MTCs) can be determined directly by<br />

measuring the evaporation rate of a pool of pure liquid, or even the sublimation rate<br />

of a volatile solid. The interfacial partial pressure, fugacity, or concentration of the<br />

solute can be found from vapor pressure tables. The concentration some distance<br />

from the surface can be zero if an adequate air circulation is arranged, thus DC or<br />

Df is known. The pool can be weighed periodically to determine N, and area A can<br />

be measured directly, thus the MTC or evaporation D value is the only unknown.<br />

Worked Example 7.3<br />

A tray (50 ¥ 30 cm in area) contains benzene at 25°C (vapor pressure 12,700 Pa).<br />

The benzene is observed to evaporate into a brisk air stream at a rate of 585 g/h.<br />

What are D and k M, the mass transfer coefficient?<br />

Since the molecular mass is 78 g/mol, N is 585/78 or 7.5 mol/h.<br />

©2001 CRC Press LLC<br />

Df = (12700 – 0) Pa<br />

D = 7.5/12700 = 5.9 ¥ 10 –4 mol/Pa h<br />

A is 0.5 ¥ 0.3 or 0.15 m 2 . Z A is 1/RT or 4.04 ¥ 10 –4 . Since D is k MAZ, k M is 9.7 m/h.<br />

In conventional units, DC is 12,700/RT or 5.13 mol/m 3 .<br />

N = k MADC<br />

Thus, k M = 9.7 as before.<br />

Obviously, the two approaches are algebraically equivalent. Using an experimental<br />

system of this type, the dependence of k M on wind speed can be measured.<br />

Measurement of overall intermedia D values or MTCs is similar in principle, Df<br />

applying between two bulk phases. A convenient method of measuring water-to-air<br />

transfer is to dissolve the solute in a tank of water, blow air across the surface to<br />

simulate wind, and measure the evaporation rate indirectly by following the decrease<br />

in concentration in the water with time. If the water volume is V m 3 , area is A m 2 ,<br />

and depth is Y m, then

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