A study of two-dimensional dispersion in unconsolidated porous media |
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Authors: | C G Voigt R E Hayes P A Tanguy |
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Institution: | (1) Department of Chemical Engineering, University of Alberta, T6G 2G6 Edmonton, Alberta, Canada;(2) Present address: Oil Sands Technology and Research Authority, 18th Floor, McFarlane Tower, 700 Fourth Avenue S.W., T2P 3J4 Calgary, Alberta, Canada;(3) Département de génie chimique, Université Laval, G1K 7P4 Québec, Canada |
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Abstract: | An experimental and numerical investigation into the magnitude of longitudinal and transverse dispersion in a two-dimensional flow field over a particle Peclet number range of 50–8500 is reported. Numerical modelling using a Galerkin finite element method is used to test various models, notably those of Fried and combarnous and Koch and Brady. Dispersion at low Peclet numbers (< 200) is found to be described adequately by either model, which at large Peclet, the degree of dispersion is significantly underestimated. An improved dispersion model for Peclet numbers greater than 200 is proposed. The transverse dispersion term and the choice of inlet boundary condition are found to have a negligible effect on the shape of the breakthrough curve.Nomenclature
A (z)
Polynomial in the z plane
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B (z)
Polynomial in the z plane
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C
Concentration
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C
f
Feed concentration
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C
o
Concentration at the entrance
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D
Dispersion tensor
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D
f
Molecular diffusion coefficient
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D
1
Longitudinal dispersion coefficient
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D
p
Particle diameter
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D
t
Transverse dispersion coefficient
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k
Permeability/viscosity
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k
Dimensionless permiability in the Koch and Brady model
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P
Pressure
- Pe
k
Modified Peclet number, Pe
p
k
- Pe
p
Particle Peclet number vD
p
/D
f
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v
Velocity
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z
Axial coordinate or complex variable
Greek letters
Solution domain
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Boundary
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Porosity |
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Keywords: | Dispersion |
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