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Volume 24, N. 3, pp. 491–495, 2005 Copyright © 2005 SBMAC ISSN 0101-8205

www.scielo.br/cam

Erratum:

(Computational and Applied Mathematics, Vol. 23, N. 2-3, pp. 259–284)

Size exclusion during particle suspension

transport in porous media: stochastic

and averaged equations

A. SANTOS1 and P. BEDRIKOVETSKY2

1Universidade Católica do Rio de Janeiro (PUC-Rio/DEC/GTEP) Rua Marques de São Vicente 225, 22453-900 Rio de Janeiro, RJ, Brazil

2Universidade Estadual do Norte Fluminense (UENF/LENEP) Rod. Amaral Peixoto, km 163 – Av. Brenand s/n.

27925-310 Macaé, RJ, Brazil

E-mails: asantos@civ.puc-rio.br / pavel@lenep.uenf.br

Abstract.

A pore scale population balance model is formulated for deep bed filtration of stable

particulate suspensions in porous media. The particle capture from the suspension by the rock

occurs by the size exclusion mechanism. The equations for particle and pore size distributions

have been derived from the stochasticMaster equation. The model proposed is a generalization

of stochastic Sharma-Yortsos equations – it accounts for particle flux reduction due to restriction

for large particles to move via small pores. Analytical solution for low particle concentration is

obtained for any particle and pore size distributions. The averaged macro scale equations, derived

from the stochastic pore scale model, significantly differ from the traditional deep bed filtration

model.

Mathematical subject classification:

76S05, 60H15.

Key words:

deep bed filtration, particle size distribution, pore size distribution, size exclusion

mechanism, stochastic model, averaging.

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492 ERRATUM: STOCHASTIC AND AVERAGED EQUATIONS

Figure 1 – Geometric model of the porous medium (a) Sketch for particulate suspension transport in porous media: particles are captured due to size exclusion. (b) Connectivity in the porous medium model.

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A. SANTOS and P. BEDRIKOVETSKY 493

Figure 4 – Concentration waves for different particle sizes. Each front moves with velocityα(rs). Line 1 corresponds to transport of small particles (rs1 <rpmi n). Lines

2 and 3 are related to filtration of intermediate size particles,rs2 <rs3. Line 4 shows

the large particle concentration (rs4>rpmax).

Figure 5 – Concentration distributions for suspended particles and vacant pores during filtration: (a) initial distributions; (b) distributions behind the concentration front for

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494 ERRATUM: STOCHASTIC AND AVERAGED EQUATIONS

Figure 6 – Suspended concentration at the core outlet. Lines 1 and 3 are related to large and small particles, respectively. Line 2 corresponds to intermediate size particle concentration.

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A. SANTOS and P. BEDRIKOVETSKY 495

Imagem

Figure 1 – Geometric model of the porous medium (a) Sketch for particulate suspension transport in porous media: particles are captured due to size exclusion
Figure 4 – Concentration waves for different particle sizes. Each front moves with velocity α(r s )
Figure 7 – Effect of particle size on dimensionless penetration depth h X (r s)i max for intermediate size particles
Figure 8 – Shapes of suspended particle and vacant pore size distributions. Areas c 1 and c 3 represent the fraction of particles that do not perform deep bed filtration (small and large particles, respectively).

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