Page 668 - The Toxicology of Fishes
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648                                                        The Toxicology of Fishes


                                                 Atmospheric
                                                 Deposition

                          Point Source          Wet  Dry.
                          Discharge         Rain  Dep. Dep.  Absorption



                                                                 Volatilization  Advective Outflow
                                                                                  water + particles
                          Inflow
                          water + particles


                                                                                   Water Reaction

                                                             Deposition

                            W–S Diffusion

                                                                                    S–W Diffusion

                                               Resuspension       Active Sediment
                                                            Burial  Buried Sediment  Sediment Reaction

                       FIGURE 14.1 Input and output processes that are quantified by the Quantitative Water Air Sediment Interaction (QWASI)
                       model.

                       take a variety of forms; for example, a rate of outflow in units of g/hr can be expressed as the product
                                                               3
                       of a water flow rate (m /hr) and a concentration (g/m ). A reaction rate can be expressed as the product
                                        3
                       of a volume (m ), concentration (g/m ), and rate constant (hr ), the latter being 0.693/half-life (hr). A
                                   3
                                                    3
                                                                      –1
                       volatilization rate can be the product of an area (m ), concentration (g/m ), and mass transfer coefficient
                                                                              3
                                                             2
                       or velocity (m/hr). The resulting mass balance equations become quite lengthy, and extreme care must
                       be taken to ensure that units are consistent. The model is likely to be applied to a variety of toxicants
                       that differ in properties. The expressions must allow the user to input these various properties while
                       ensuring that the equations remain valid; that is, the model should be robust enough to accept these
                       inputs and treat them correctly.
                        An alternative and ultimately equivalent approach is to use the concept of fugacity as a surrogate
                       for concentration, as described by Mackay (2001). The concentration (C) (mol/m ) is expressed as a
                                                                                       3
                       product of fugacity f (Pa) and a Z value (mol/Pa m ). Fugacity can be regarded as partial pressure, or
                                                              3
                       escaping tendency, of a substance. The Z value is specific to the substance and the medium in which
                       it resides and can be viewed as a kind of solubility. Z values are deduced from equilibrium partition
                       coefficients. A partition coefficient K  between two phases 1 and 2, such as air and water, can be
                                                    12
                       shown to be Z /Z . Usually, Z is first defined for air, then the values for other phases such as water,
                                  1
                                    2
                       sediment, and fish are deduced. All process rates (mol/hr) are expressed as the product of a fugacity
                       (f) (Pa) and a D value (mol/Pa hr). Fugacity-based and concentration-based equations are essentially
                       identical, but the fugacity equations are more compact. D values are best thought of as rate constants
                       for the process expressed in terms of fugacity. Applying the list of D values in Table 14.1 to the diagram
                       in Figure 14.1 and defining fugacities for the chemical in air (f ), inflow water (f ), water column (f ),
                                                                                                    W
                                                                                     I
                                                                       A
                       and sediment (f ), we can write the fundamental mass balance equations for water and sediment
                                   S
                       compartments in the form:
                                                                        −
                                    inventory change (mol/hr) =  input rate (mol/hrr) output rate (mol/hr)  (14.1)
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