5.5 Mass Loss Expressions for Multiple Concurrent Loss Routes
In general, first-order decay/degradation,
leaching, wind suspension, water erosion, and volatilization could all
be happening concurrently; and some type of remediation methodology could
be implemented at some point during the simulation time. The multiple,
concurrent processes can interact; which can cause the mathematical expression
for a given term in Equation 5.56 to be different from what it would be
if that process was the only one removing mass from the source zone. When
processes occur simultaneously, the appropriate mathematical formulations
are as follows.
The mass flux term for
loss from the source zone by decay/degradation is still given by the expression
in Equation 5.57. This is true even for the scenario in which an ISS remediation
methodology has been implemented. Recall that the conceptual model for
this scenario assumes that a spatial gradient in concentration develops
inside the waste form as contaminants diffuse out of it. However, it is
true that
which demonstrates that Equation 5.57 is still valid. However, for
an ISS scenario, if decay products are also contaminants of interest, the
mass of decay products produced by the decay term (Equation 5.57) for the
parent contaminant is not added back into the mass of the source zone for
consideration in subsequent time steps. The necessity of this restriction
arises from the fact that the mass flux term for leaching from an ISS waste
form is based on spatial concentration gradients and contaminant masses
in the source zone at the initial time, rather than at the actual time.
(This is different than the way the source-term release module handles
the accumulation and subsequent loss of decay products of concern for other
scenarios.)
The term for leaching can take on one of several different forms
depending on the particular scenario being simulated (e.g., whether a NAPL
phase exists, whether a clean soil layer exists above the source zone,
whether a remediation methodology has been implemented). In general form,
the mass flux term for loss from the source zone by leaching is still given
by Equation 5.60. When a NAPL phase exists in the source zone, the mass
flux term for loss from the source zone by leaching is still calculated
by Equation 5.60 directly, with the value of Cwicalculated form the phase partitioning theory described in Section 2.2.4, as before.
When no NAPL phase exists in the source zone, the mass flux term
for leaching may take on a number of forms. When no ISV or ISS remediation
methodology has been implemented, consider that the aqueous concentration
of the contaminant is given by Equation 2.7, and the volume of the source
zone is given by Equation 5.69. Substituting Equations 2.7 and 5.69 into
Equation 5.60, we obtain
Now all that remains is to determine the correct way to express the
thickness, h, of the source zone that appears in Equation 5.89. The position
of the lower boundary of the source zone is constant in time. On the other
hand, the position of the upper boundary of the source zone may be changing
due to volatilization and/or wind suspension and water erosion. Firstly,
consider a scenario where a clean layer of soil exists above the source
zone initially. Depending on the relative rates of wind suspension, water
erosion, and volatilization, it could be the case that the clean layer
will always exist during the simulated time frame (and maybe even grow
in thickness); or it could be the case that the clean layer will eventually
be stripped away at some time during the simulated time frame. Secondly,
consider a scenario where a clean layer of soil does not exist above the
source zone initially. Again, depending on the relative rates of wind suspension,
water erosion, and volatilization, a clean layer may never develop; or
it may develop and always exist thereafter during the simulated time frame;
or it may develop but eventually be stripped away at some time during the
simulated time frame. As long as a clean layer is present, the process
controlling the thickness of the source zone is volatilization. When no
clean layer is present, the processes controlling the thickness of the
source zone are wind suspension and/or water erosion. The criterion that
must be used to determine which of these two regimes the system is in is
a comparison between the position of the top of the source zone, z, and
the position of the soil surface, which can be expressed as (S+E)t. Hence,
the thickness of the source zone is given by
Substituting the appropriate expression for h from Equation 5.90 into
Equation 5.89, the mass flux term for loss from the source zone by leaching
(when no NAPL phase is present) is given by
for all times when a clean layer of soil exists above the source zone
(i.e., when z (S+E)t), and is given by
for all times when a clean layer of soil does not exist above the source
zone (i.e., when z (S+E)t).
For scenarios where an ISV remediation methodology has been implemented,
the leaching term could still be given by the expression in Equation 5.64.
However, as stated previously, expressions for the actual surface area
and volume of the dissolving cracked glass as functions of time would be
difficult to obtain in most instances. For ISV scenarios, wind suspension,
water erosion, and volatilization mass fluxes are assumed to be zero because
of the nature of the cracked glass waste form. This means that decay is
the only other loss process occurring besides leaching. Therefore, the
overall total concentration of a contaminant in the glass can be expressed
as
If we make the same idealizing assumption that was made when deriving
Equation 5.66, the mass flux term for loss from the source zone by leaching
for an ISV waste form is given by
For scenarios where an ISS remediation methodology has been implemented,
wind suspension, water erosion, and volatilization mass fluxes are assumed
to be zero because of the nature of the ISS waste form. This is a good
assumption for wind suspension and water erosion because the grouting of
the source zone into a solid waste form prevents soil particles from being
removed by these processes. However, in reality volatilization could still
occur by outward diffusion through the grout, and then upward diffusion
through a clean layer of soil, if one is present. Simulating volatilization
in this scenario would require some type of coupled, two-region diffusion
theory. It would also require some kind of conceptualization of how downwardly
percolating vadose zone water impinging on the upper face of the waste
form (i.e., the boundary between the two regions) and being channeled around
the waste form, affects boundary conditions of the mathematical problem
at the interface. Such theory for volatilization was not developed for
the current version of the source-term release module.
Recall that the conceptual model for leaching from an ISS waste
form consists of diffusive movement of contaminants within the waste form
to the outer boundary of the waste form, where they are lost to the vadose
zone water that percolates past the faces of the waste form. The vadose
zone water is assumed to move past the waste form fast enough that a zero
concentration boundary condition applies for all contaminants at the faces
of the waste form. The conceptualization leads to theory that predicts
transient-state spatial gradients in concentration within the waste form.
For any contaminant, i,
the expression for mass flux out of the waste form developed from this
theory (Equation 5.67 for the case where leaching is the only loss process)
depends on the mass of contaminant i present in the waste form at the initial
time (which was assumed to be spatially uniformly distributed within the
waste for at that time). If contaminant i also undergoes decay/degradation,
this same type of theoretical development can be used to obtain a similar
expression for leaching loss mass flux (as a function of time) that accounts
for the interaction of the decay/degradation process. Specifically, for
all contaminants that are initially present in the source zone, the mass
flux term for loss from the source zone by leaching (when decay/degradation
also occurs) for an ISS waste form is given by
where
Mi,p is the total mass or activity of the p-th member of the decay/degradation chain that starts with contaminant i (g or Ci)
li,k is the first-order decay/degradation
coefficient for the k-th member of the decay/degradation chain that
starts with contaminant i (yr-1).
Note that for clarity
later in the theoretical development, we have added an additional index
to the subscripts of variables that depend on the particular contaminant
species. The specific value '1' used for the second subscript indices p
and k in Equation 5.95 denotes that this particular contaminant, i,
was present in the source zone at the initial time (i.e., contaminant i
is considered to be the first member of a possible decay/degradation chain
of contaminants of concern). The quantity Mio",1 is the initial
mass of contaminant i in the source zone. The quantity Mi,1
is the mass of contaminant i in the source zone at time t that originated
from Mio",1, but that has been reduced from the value Mio",1
because of decay/degradation. The quantities li,1
and Dgi,1 are merely the first-order decay coefficient and effective
diffusion coefficient in the waste form, respectively, for contaminant
i. However, the added subscript index denotes that these are for a "parent"
compound in a possible decay/degradation chain. Note also that Equation
5.95 is similar to Equation 5.67, except that an exponential decay factory
for each contaminant initially present has been included. This factor,
multiplied by the initial mass of the contaminant, is an expression of
how the mass of contaminant i would have changed over time if no
leaching loss would have occurred.
If every contaminant i
merely decayed/degraded into a nontoxic compound that was not of concern,
Equation 5.95 is all that would be needed to predict the leaching of each
contaminant of concern. However, if a contaminant initially present in
the source zone decays/degrades into another contaminant, Equation 5.95
cannot account for this additional progeny mass during the simulation because
only the initial mass (rather than the actual mass as time t) appears in
the equation. In other words, there is no simple way to add contaminant
mass back into the calculations for subsequent times (as we do with the
solution of equations for other scenarios). One might be tempted to use
the same type of equation as Equation 5.95, only reset the initial mass
variable to the added mass, and reset the time variable to make t = 0 coincide
with the time of production of the new mass. However, this is not a valid
approach because the theory behind Equation 5.95 assumes that the mass
is spatially uniformly distributed at the initial time, while what is really
occurring in the source zone is that new mass is being produced nonuniformly
over space because gradients in the contaminant that produced it already
exist at time t.
The source-term release
module accounts for the leaching of progeny contaminants in the following
way. For each contaminant i that is initially present in the source
zone (as a "parent" contaminant), the module uses a set of equations to
calculate the leaching losses of all progeny contaminants that were derived
from the initial mass of contaminant i. Specifically, for all contaminants
that are progeny of contaminant i, the mass flux term for loss from
the source zone by leaching (when decay/degradation also occurs) for an
ISS waste form is given by
Note that this equation is not an exact solution to the coupled contaminant
diffusion problem because all contaminants may have their own unique effective
diffusion coefficient in the waste form. Rather, Equation 5.96 contains
the implicit assumption that all progeny contaminants have the same effective
diffusion coefficient as their parent contaminant. In Equation 5.96, the
product of the first three factors on the right-hand side of the equation
is an expression of how the masses of progeny of contaminant i would
have changed over time if no leaching loss would have occurred (i.e, it
is the mass versus time function predicted by the Bateman equation [Bateman
1910]).
Contaminants that are part of a decay/degradation chain
of one of the contaminants present initially may actually be one of the
initial contaminants, or may be the same as one of the contaminants in
the decay/degradation chain of another initial contaminant. Therefore,
after all of the mass fluxes denoted by Equations 5.95 and 5.96 are calculated,
the ones that correspond to the same contaminant are added together to
produce one set of leaching mass flux terms (i.e., this summation procedure
is how the module accounts for the accumulation and subsequent loss of
daughter products).
When the soil is contaminated all the way up to the surface,
the mass flux terms for loss from the source zone by wind suspension or
water erosion are given by
Note that Equations 5.97 and 5.98 are similar to the expressions
in Equations 5.71 and 5.72 for individual loss pathways, except for the
fact that the thickness of the source zone must now be expressed as a function
of both of these particle loss processes. When there is a clean layer of
soil at the surface, the mass flux terms for wind suspension and water
erosion are zero.
The appropriate mass flux terms for volatilization in scenarios
where multiple contaminant loss processes are occurring concurrently were
developed as follows. As was described above for the calculation of leaching
loss mass flux terms, there may or may not be a clean layer present at
any given time (depending on the relative rates of wind suspension, water
erosion, and volatilization). When a clean layer is present, the mass flux
term for contaminant loss from the source zone by volatilization is given
by
Note that Equation 5.99 is similar to Equation 5.73 (for the case where
loss is by volatilization alone), except that the length of the diffusion
path also depends on how much soil has been removed from the surface by
wind suspension and water erosion. When a NAPL phase exists in the source
zone, the vapor concentration in Equation 5.99 is calculated by the phase
partitioning theory described in Section 2.2.4. When no NAPL phase exists
in the source zone, Cvi,
can be calculated by a simple phase partitioning relation, and the mass
flux term is given by
When a clean layer is not present, or when it is so thin that Equation
5.99 would predict unreasonably high values, the mass flux term for volatilization
at that time is again taken to be the bounding value calculated by Equation
5.86.
Mass balance arguments (similar to those invoked when volatilization
was the only process occurring) lead to the equation used by the module
to compute the rate of recession of the upper boundary of the source zone,
based on an individual contaminant, when a bounding value is not used for
the volatilization flux term:
When a NAPL phase exists in the source zone, the vapor concentration
in Equation 5.101 is calculated by the phase partitioning theory described
in Section 2.2.4. When no NAPL phase exists in the source zone, Cvi,
can be calculated by a simple phase partitioning relation, and the rate
of recession of the top boundary of the source zone, based on an individual
contaminant, is given by
When a bounding value is used for volatilization flux, the rate of
recession of the top boundary of the source zone, based on an individual
contaminant, is still given by Equation 5.87. As in the case where volatilization
was the only loss process occurring, for contaminants that are components
of the NAPL phase, Equation 5.80 is then used to calculate a single updated
position of the top boundary of the source zone for all of the NAPL-phase
components.
As a final note, recall that the source-term release module tests
to determine if a NAPL phase exists at the beginning of each time step.
Based on the specific theory presented in this section for the contaminated
vadose zone source zone, Equation 2.1 can be rewritten as
for all times when a clean layer exists and
for all times when a clean layer does not exist. Equations 5.103 and
5.104 are the test criteria that the module actually uses for contaminated
vadose zone simulations.