Page 130 - gas transport in porous media
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Chapter 7: Gas-Phase Dispersion in Porous Media
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                                                         −1
                                                           ), T is temperature (K), m is the solute mass
                           where k is Boltzmann’s constant (J·K
                           (M), and v rms is the root-mean-square velocity of the gas particles (L·T −1 ). Thus,
                           given thermal equilibrium and consequent equal kinetic energy, lower molecular
                           weight gases will exhibit higher average velocities relative to higher molecular weight
                           gases. This higher velocity translates into larger diffusion coefficients and larger
                           contributions to overall dispersion.
                             Diffusion processes often dominate transport in low permeability zones, such as
                           within aggregates or fine-textured lenses. In the case of volatile organic compounds
                           (VOCs), the occurrence of diffusion can both aid and present additional challenges to
                           remediation efforts. Specifically, the larger spatial distribution of the VOC caused by
                           diffusion may increase the probability of detecting the VOC in the subsurface, such
                           that a remediation plan can be implemented. Conversely, it is this same diffusion
                           processthatisoftenlargelyresponsibleforthetransportofVOCsinthevadose-zoneto
                           the water table resulting in groundwater contamination (e.g., Lupo, 1989). Moreover,
                           contaminant diffusion can influence the fate of contamination in a system by altering
                           its bioavailability. Diffusion largely governs gas-exchange between the atmosphere
                           and soil, including the exchange of carbon dioxide and oxygen, and atmospheric
                           pollutants, such as fluorocarbons (Weeks et al., 1982). Jury et al. (1991) estimate that
                           only 0.5%, 1%, 0.1%, and 7–9% of the overall subsurface gas exchange is induced by
                           temperature and barometric pressure changes, wind, and precipitation, respectively.
                           Thus, they conclude that diffusion is the primary gas transport mechanism in soil
                           systems. Little et al. (1992) review the critical role diffusion plays in transporting
                           subsurface VOCs into homes and buildings.


                           7.2.2  Mechanical Mixing
                           Mechanical mixing is a solute-independent component of dispersion, governed by the
                           physical properties of the porous medium and carrier gas velocity. Mechanical mixing
                           is a lumped term, incorporating a number of sources of velocity variations that result
                           in solute mixing and dilution. Such velocity variations may be caused by (A) non-
                           uniform velocity profiles along the cross section of individual pores (e.g., velocities
                           are higher in the center of the pore relative to near-wall velocities); (B) distributions in
                           pore sizes (e.g., large pores promote higher velocities than smaller pores); and (C) the
                           tortuosity of flow paths, as shown in Figure 7.2. The effective pore-size distribution
                           and tortuosity are influenced by the presence of soil-water.At larger scales, dispersion
                           may be caused by the presence of lenses of material with different permeabilities.
                           Larger-scale differences in permeability may further influence capillary forces and
                           the resultant large-scale water saturation, although much less is known about large-
                           scale mechanical mixing processes (Freeze and Cherry, 1979; Selker et al., 1999).
                           Because the magnitude of mechanical mixing depends on the degree of heterogeneity,
                           it is expected that the magnitude of gas-phase dispersivity will be proportional to the
                           system-scale as has been demonstrated for aqueous-phase dispersion (Pickens and
                           Grisak, 1981; Gelhar et al., 1992).
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