2013
DOI: 10.1002/wrcr.20433
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Upscaling colloid transport and retention under unfavorable conditions: Linking mass transfer to pore and grain topology

Abstract: [1] We revisit the classic upscaling approach for predicting Darcy-scale colloid retention based on pore-scale processes, and explore the implicit assumption that retention is a Markov process. Whereas this assumption holds under favorable attachment conditions, it cannot be assumed to hold under unfavorable conditions due to accumulation of colloids in the near-surface fluid domain. We develop a novel link between two-layer mass transfer parameters and the topologies of the pore and collector domains, startin… Show more

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Cited by 50 publications
(67 citation statements)
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References 62 publications
(121 reference statements)
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“…The parameter η describes the efficiency of colloid delivery to the surface (favorable conditions) or the near‐surface fluid domain (unfavorable conditions) at the pore scale. Its implementation into continuum‐scale models (upscaling) is performed under the simple assumption that the control volume considered in the continuum model is represented by a collection of identical pore‐scale collectors comprising the same volume and having the same porosity as the control volume [ Logan et al ., ; Nelson and Ginn , ; Johnson and Hilpert , ]. Under this assumption, the equation expressing η as a rate constant ( k ) for the Happel sphere‐in‐cell geometry is k=3(1θ)1/32dcln(1η)v where d c is the average collector diameter, v is velocity, and θ is porosity.…”
Section: Upscaling From Pore To Continuum Scalementioning
confidence: 99%
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“…The parameter η describes the efficiency of colloid delivery to the surface (favorable conditions) or the near‐surface fluid domain (unfavorable conditions) at the pore scale. Its implementation into continuum‐scale models (upscaling) is performed under the simple assumption that the control volume considered in the continuum model is represented by a collection of identical pore‐scale collectors comprising the same volume and having the same porosity as the control volume [ Logan et al ., ; Nelson and Ginn , ; Johnson and Hilpert , ]. Under this assumption, the equation expressing η as a rate constant ( k ) for the Happel sphere‐in‐cell geometry is k=3(1θ)1/32dcln(1η)v where d c is the average collector diameter, v is velocity, and θ is porosity.…”
Section: Upscaling From Pore To Continuum Scalementioning
confidence: 99%
“…Hence, mixing of near‐surface and bulk fluid between subsequent collectors is reasonably inferred. In contrast, absence of mixing between collectors under unfavorable conditions would yield increasing excess of colloids in the near‐surface fluid (via secondary minimum attraction), increasingly so with each subsequent collector, such that k would increase with increased transport distance [ Johnson and Hilpert , ]. Whereas k does vary with transport distance under unfavorable conditions (e.g., hyperexponential and nonmonotonic profiles of retained colloids), it does not strictly increase with transport distance.…”
Section: Upscaling From Pore To Continuum Scalementioning
confidence: 99%
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“…These two states are sufficient to track mobile colloids as they move through the dual networks of pores and grains. However, a colloid can also be immobilized onto a grain via primary energy minimum interactions, when it reaches State a in which it attaches to a grain surface [ Johnson and Hilpert , ]. …”
Section: The Modelmentioning
confidence: 99%