FALTA, Ron, faltar@clemson.edu, Department of Geological Sciences, Clemson University, Clemson, SC 29634-0976
The unstable nature of air sparging gas flow below the water table causes
injected gas to flow locally through small channels, which are separated
by a distance of one or several millimeters. Although it is possible
to model the average air sparging darcy flux using a conventional multiphase
flow approach, this type of model does not resolve local mass transfer
effects which arise due to the millimeter scale gas channels. For
this reason, compositional multiphase flow simulators which assume local
chemical equilibrium between the phases may overestimate the rate of contaminant
mass transfer to the gas phase during air sparging.
An alternative method is proposed for modeling the
local mass transfer during air sparging. The method is based on the
existing dual media formulation which is commonly used for modeling flow
and transport processes in fractured media. Instead of considering
fractures and matrix blocks, the method is applied to porous media to simulate
the local gas channels which form during air sparging. This allows
resolution of the local diffusive mass transfer between the flowing gas
phase, and nearby stagnant water filled zones. Because each media
is modeled with a single node separated by some local average distance,
the diffusive mass transfer is mathematically analogous to a first order
interphase mass transfer reaction.
The new model is applied to laboratory column experiments
in which dissolved trichloroethylene (TCE) is removed by air sparging.
The new numerical formulation provides a good match with these data, it
is shown that the simulation results are very sensitive to the nature of
the local mass transfer limitations.
The numerical model is then applied to a hypothetical
field air sparging case involving a dissolved plume of TCE, with the same
material parameters as the laboratory experiments. In this instance,
the effluent gas concentration from the SVE recovery well is found to be
relatively insensitive to the details of the local mass transfer.
Instead, the long term behavior of the system depends more on the large
scale diffusive mass transfer of the contaminant in this case.