24.01.2013 Views

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

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

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

SHOW MORE
SHOW LESS

Create successful ePaper yourself

Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.

7.10.1 Level III D Values<br />

©2001 CRC Press LLC<br />

7.10 LEVEL III CALCULATIONS<br />

In this chapter, we have examined the nature of molecular and eddy diffusivity,<br />

introduced the concept of mass transfer coefficients (k), and treated the problem of<br />

resistances occurring in series and parallel as material diffuses from one phase to<br />

another. Two new D values have been introduced, a kAZ product and a BAZ/DY<br />

product. We can treat situations in which various D values apply in series and in<br />

parallel.<br />

In some situations, diffusion D values may be assisted or countered by advective<br />

transfer D values. For example, PCB may be evaporating from a water surface into<br />

the atmosphere only to return by association with aerosol particles that fall by wet<br />

or dry deposition. We can add D values when the fugacities with which they are<br />

multiplied are identical, i.e., the source is the same phase. This is convenient, because<br />

it makes the equations algebraically simple and enables us to compare the rates at<br />

which materials move by various mechanisms between phases.<br />

We thus have at our disposal an impressive set of tools for calculating transport<br />

rates between phases. We need Z values, mass transfer coefficients, diffusivities,<br />

path lengths, and advective flow rates. Quite complicated models can be assembled<br />

describing transfer of a chemical between several media by a number of routes. In<br />

general, the total D value for movement from phase A to phase B will not be the<br />

same as that from B to A. The reason is that there may be an advective process<br />

moving in only one direction. Diffusive processes always have identical D values<br />

applying in each direction. D values for loss by reaction can also be included in the<br />

mass balance expression. We are now able to use these concepts to perform a Level<br />

III calculation.<br />

These calculations were suggested and illustrated in a series of papers on fugacity<br />

models (Mackay, 1979; Mackay and Paterson 1981, 1982; and Mackay et al. 1985).<br />

It is important to emphasize that these models will give the same results as other<br />

concentration-based models, provided that the intermedia transport expressions are<br />

ultimately equivalent. A major advantage of the fugacity approach is that an enormous<br />

amount of detail can be contained in one D value, which can be readily<br />

compared with other D values for different processes. It is quite difficult, on the<br />

other hand, to compare a reaction rate constant, a mass transfer coefficient, and a<br />

sedimentation rate and identify their relative importance.<br />

Figure 7.10 depicts the simple four-compartment evaluative environment with<br />

the intermedia transport processes indicated by arrows. In addition to the reaction<br />

and advection D values, which were introduced in Level II, there are seven intermedia<br />

D values. The emission rates of chemicals must now be specified on a medium-bymedium<br />

basis whereas, in Level II, only the total emission rate was needed.<br />

Table 7.1 lists the intermedia D values and gives the equations in terms of<br />

transport rate parameters. Subscripts are used to designate air, 1; water, 2; soil, 3;<br />

and sediment, 4.<br />

Table 7.2 gives order-of-magnitude values for parameters used to calculate intermedia<br />

transport D values. These values depend on the environmental conditions and

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!