2017
DOI: 10.1007/s10596-017-9692-6
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A model for non-Newtonian flow in porous media at different flow regimes

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Cited by 34 publications
(37 citation statements)
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“…A local maximum for the polymer viscosity is obtained at a third critical rate . Beyond , there is another decrease in polymer viscosity; this shear rate is characterized as the onset of mechanical degradation (Dupas et al, 2012;Brakstad and Rosenkilde, 2016;Lohne et al, 2017;Skauge et al, 2018). Polymer injectivity in porous media is influenced by a number of factors including shear thickening.…”
Section: In-situ Rheology Of Associative Polymersmentioning
confidence: 99%
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“…A local maximum for the polymer viscosity is obtained at a third critical rate . Beyond , there is another decrease in polymer viscosity; this shear rate is characterized as the onset of mechanical degradation (Dupas et al, 2012;Brakstad and Rosenkilde, 2016;Lohne et al, 2017;Skauge et al, 2018). Polymer injectivity in porous media is influenced by a number of factors including shear thickening.…”
Section: In-situ Rheology Of Associative Polymersmentioning
confidence: 99%
“…Due to the time-consuming nature of in-situ measurement techniques, in-situ polymer rheology has often been evaluated analytically and numerically (Skauge et al, 2018). The difficulty with modelling polymer rheology lies in the fact that they are non-Newtonian fluids and the porous media in which they flow is a non-uniform pore geometry (Lohne et al, 2017;Skauge et al, 2018). The analytical study of polymer flow in porous media involves the use of time-independent models with the addition of some viscoelastic attributes (Delshad et al, Journal Pre-proof J o u r n a l P r e -p r o o f 2008; Sochi, 2010;Hatzignatiou et al, 2013;Yang et al, 2015).…”
Section: Existing Models For In-situ Polymer Rheologymentioning
confidence: 99%
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