1967
DOI: 10.2118/1688-pa
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Flow of Polymer Solutions Through Porous Media

Abstract: This paper discusses the physical parameters involved in the slow flow of high molecular weight polymer solutions in porous media. The interacting erects of polymer properties and porous media properties on flow performance are considered. Experiments were conducted with the polyethylene oxides, with molecular weights ranging from 200,000 to over 5,000,000. Frontal advance velocities ranged from 1 to 30 ft/day. The porous matrix consisted of a flow cell packed with glass beads. Polymer solutions were character… Show more

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Cited by 89 publications
(45 citation statements)
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“…[5] gives : [7] Provided the radial momentum flux terms (in the cylindrical coordinate system) are properly negligible it may be shown that the pressure gradient term of eq. [7] is zero, on the basis of symmetry arguments alone, i. e. independently of any constitutive approximations. Under these conditions eqs.…”
Section: Stress Fieldmentioning
confidence: 99%
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“…[5] gives : [7] Provided the radial momentum flux terms (in the cylindrical coordinate system) are properly negligible it may be shown that the pressure gradient term of eq. [7] is zero, on the basis of symmetry arguments alone, i. e. independently of any constitutive approximations. Under these conditions eqs.…”
Section: Stress Fieldmentioning
confidence: 99%
“…Under these conditions eqs. [4] and [7] give: [8] o It was noted earlier that replacement of vz with V, the mean velocity through the orifice, would lead to an error of less than 4%, this error being primarily due to the actual velocities not coinciding perfectly with their axial projections. The same arguments apply to the second term within the square brackets of eq.…”
Section: Stress Fieldmentioning
confidence: 99%
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“…The formulations describing the flow of viscous fluids do not apply to viscoelastic fluids as a consequence of the discovery (Sadowski and Bird, 1965;Marshall and Metzner, 1967;Dauben and Menzie, 1967;Savins, 1969) that in flows through packed beds or porous media viscoelastic fluids exhibit enhanced potential drops exceeding those predicted on the basis of the viscous flow behaviour. It may be noted that Christopher and Middleman (1965) developed an equation based on the Kozeny-Ergun bed model (Kozicki, 2001) that successfully predicts the flow of high shear-thinning fluids (Kozicki and Tiu, 1988) and provides an improved fit of the data of Sadowski and Bird (1965).…”
mentioning
confidence: 99%