2013
DOI: 10.1016/j.advwatres.2012.12.007
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Effects of compound-specific transverse mixing on steady-state reactive plumes: Insights from pore-scale simulations and Darcy-scale experiments

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Cited by 62 publications
(50 citation statements)
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“…his parameterization of D T , inspired by an earlier statistical model of Bear and Bachmat (1967), takes into account the inluence of aqueous difusion not only on the pore difusion but also on the mechanical dispersion term: where Pe = vd/D aq is the dimensionless grain Péclet number with d [L] representing the grain diameter, d (dimensionless) is the ratio between the length of a pore channel and its hydraulic radius, and b (dimensionless) is an exponent accounting for incomplete dilution of the solute in the pore channels. Average values of d = 6.2 and b = 0.5 were determined experimentally considering a wide range of low-through conditions in diferent porous media and were found in good agreement with the outcomes of pore-scale simulations Hochstetler et al, 2013).…”
supporting
confidence: 72%
“…his parameterization of D T , inspired by an earlier statistical model of Bear and Bachmat (1967), takes into account the inluence of aqueous difusion not only on the pore difusion but also on the mechanical dispersion term: where Pe = vd/D aq is the dimensionless grain Péclet number with d [L] representing the grain diameter, d (dimensionless) is the ratio between the length of a pore channel and its hydraulic radius, and b (dimensionless) is an exponent accounting for incomplete dilution of the solute in the pore channels. Average values of d = 6.2 and b = 0.5 were determined experimentally considering a wide range of low-through conditions in diferent porous media and were found in good agreement with the outcomes of pore-scale simulations Hochstetler et al, 2013).…”
supporting
confidence: 72%
“…Due to the small spatial scale at which mixing occurs, resolving steep concentration gradients at the field scale remains challenging despite the rapid development of improved monitoring techniques [e.g., Annable et al ., ; Anneser et al ., ; Devlin et al ., ]. Therefore, laboratory experiments [e.g., Castro‐Alcala et al ., ; de Anna et al ., ; Haberer et al ., ; Rolle et al ., ] and numerical simulations at multiple scales [e.g., de Dreuzy et al ., ; Herrera and Valocchi , ; Hochstetler et al ., ; Porta et al ., ; Rolle et al ., ; Tartakovsky et al ., ] are fundamental for the understanding of dilution in porous media. Most of these studies, however, focused on (quasi) two‐dimensional systems, while detailed experimental and modeling investigations in three‐dimensional domains are less common [e.g., Herrera et al ., ; Rashidi et al ., ; Silliman , ; Yoon and McKenna , ; Cirpka et al ., ].…”
Section: Introductionmentioning
confidence: 99%
“…2, insert). A similar constant shape behavior has been noted for viscous fingering in heterogeneous velocity fields (Jha et al, 2011a, b).…”
Section: Mixingmentioning
confidence: 53%