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

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misuse) these “over-maximum” fugacities. For example, a chemical may be spilled<br />

into a lake. The fugacity can be calculated as the amount spilled divided by VZ for<br />

water. If the resulting fugacity exceeds the vapor pressure, the water has insufficient<br />

capacity to dissolve all the chemical, and a separate pure chemical phase must be<br />

present. A similar situation can apply when a pesticide is applied to soils.<br />

It is likely that the maximum Z value that a solute can ever achieve is that of<br />

the pure phase Z p. It may be useful to calculate Z P to ensure that no mistakes have<br />

been made by grossly overestimating other Z values.<br />

5.6.6 Solutes of Negligible Volatility<br />

A problem arises when calculating values of the fugacity and fugacity capacity<br />

of solutes that have a negligible or zero vapor pressure. Thermodynamically, the<br />

problem is that of determining the reference fugacity. The practical problem may<br />

be that no values of vapor pressure or air-water partition coefficients are published<br />

or even exist. Examples are ionic substances, inorganic materials such as calcium<br />

carbonate or silica and polymeric, or high-molecular-weight substances including<br />

carbohydrates and proteins. Intuitively, no vapor pressure determination is needed<br />

(or may be possible), because the substance does not partition into the atmosphere,<br />

i.e., its “solubility” in air is effectively zero. Ironically, its air fugacity capacity can<br />

still be calculated as (1/RT), but all the other (and the only useful) Z values cannot<br />

be calculated, since H cannot be determined and indeed may be zero. Apparently,<br />

the other Z values are infinite or at least are indeterminably large.<br />

This difficulty is more apparent than real and is a consequence of the selection<br />

of fugacity rather than activity as an equilibrium criterion. There are two remedies.<br />

The first method, which is convenient but somewhat dishonest, is to assume a<br />

fictitious and reasonable, but small, value for vapor pressure (such as 10 –6 Pa) and<br />

proceed through the calculations using this value. The result will be that Z for air<br />

will be very small compared to the other phases, and negligible concentrations will<br />

result in the air. It is obviously essential to recognize that these air concentrations<br />

are fictitious and erroneous. The relative values of the other concentrations and Z<br />

values will be correct, but the absolute fugacity will be meaningless.<br />

The second method, which is less convenient but more honest, is to select a new<br />

equilibrium criterion. We can illustrate this for air, water, and another phase(s) by<br />

equating fugacities as follows:<br />

©2001 CRC Press LLC<br />

f = C A/Z A = C W/Z W = C S/Z S<br />

We can divide through by P S to give<br />

f = C ART = C wP S /C S = C SP S /(C S K SW)<br />

f/P S = a = C ART/P S = C W/C S = C S/C S K SW<br />

The equilibrium criterion is now a, an activity that is dimensionless and is the<br />

ratio of fugacity to vapor pressure. The new Z values with units of mol/m 3 can be<br />

defined as

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