Page 669 - The Toxicology of Fishes
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Exposure Assessment and Modeling in the Aquatic Environment                 649


                         TABLE 14.1
                         D Values Used to Describe the Equilibria and Kinetic Processes in the Mass Balance Model: Equations
                         Used to Calculate These D Values, Process Rate Expressions Df (mol/hr), and Actual D Values for
                         Anthracene and Pyrene Shown in the Illustrations
                                                          D Value    Process Rate
                         Process                Symbol   (mol/Pa hr)  (mol/hr)  Anthracene   Pyrene
                         Sediment burial         D B       G B C S      D B f S      3.2       59.5
                         Sediment transformation  D S      V S C S k S  D S f S     57.0      330
                         Sediment resuspension   D R       G R C S      D R f S      3.12      58.7
                         Sediment to water diffusion  D T  k T A S C S /K SW  D T f S  101    435
                         Water to sediment diffusion  D T  k T A S C W  D T f W    101        435
                         Sediment deposition     D D       G D C P     D D f W      41.9      787
                         Water transformation    D W      V W C W k W  D W f W    4840       7060
                         Volatilization          D V      k V A W C W  D V f W     348        389
                         Absorption              D V     k V A W C A /K AW  D V f A  348      389
                         Water outflow            D J       G J C W      D J f W   1580       6800
                         Suspended particle outflow  D Y    G Y C P     D Y f W      22.4      422
                         Rain dissolution        D M      G M C A /K AW  D M f A    24.2      104
                         Wet particle deposition  D C      G C C Q      D C f A     23.8      157
                         Dry particle deposition  D Q      G Q C Q     D Q f A       8.9       58.8
                         Water inflow             D I        G I C I     D I f I   1580       6800.8
                         Suspended particle outflow  D X    G X C X      D X f I    108       2020


                       This equation is conceptually identical to that for money in a bank. The change in the balance over a
                       month (the inventory change in $/month) equals the difference between the rate of deposits or inputs
                       and the rate of withdrawals or outputs, also expressed in $/month. Mathematically, this is expressed by
                       a differential mass balance equation for water and sediments. The fugacity versions are more concise
                       than the concentration versions and are given in Equation 14.2 and Equation 14.3 to illustrate the concept.
                                    dV Z W W f )  dt =  E W + ( D I + D X) + ( D V + D Q + D C + D M)
                                     (
                                                       I f
                                                                  A f
                                       W
                                                 + ( D   D T) − f W( D V + D W + D J + D Y + D D + D T)  (14.2)
                                                   S f D R +
                                         dV Z S S f )  dt =  W f ( D D + D T) − ( D R +  D T +  D D + D B)  (14.3)
                                            S (
                                                                  S f
                       Each of the Df terms represents the rate of a specific process (mol/hr or g/hr) by which the chemical
                       enters, leaves, or changes location in the system. The groups (VZf) are the total amount (mol or g) in
                       the compartment. Values of each D must be established from environmental conditions and chemical
                       properties. We make no attempt here to explain all such terms in detail; the aim is merely to convey
                       that this is one approach by which a process mass balance can be established for a two-compartment
                       system.
                        At steady state, which can be achieved after a long time with constant inputs, the water and sediment
                       concentrations and fugacities become constant, the derivatives on the left become zero, and the two
                       resulting algebraic equations can be solved to give the prevailing steady-state fugacities or concentrations:

                                                    f I D +
                                                               f A D +
                                               E W + (    D X) + (    D Q +  D C +  D M)
                                   f W =               I           V
                                                         D (
                                       D V +  D W +  D J +  D Y + D D + D T)( D S + D B) ( D R +  D T +  D S + D B)  (14.4)
                                          f W( D D + D T)
                                    f S =
                                       D R + D T +  D S +  D B
                                            D
                       The differential equations can, if desired, be solved analytically or numerically, yielding equations that
                       describe how the concentrations change with time (i.e., the dynamic situation).
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