2017
DOI: 10.3997/2214-4609.201700273
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Pore-scale Visualization of Oil Recovery by Viscoelastic Flow Instabilities during Polymer EOR

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Cited by 7 publications
(9 citation statements)
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“…As a summary of the streamline visualization, Hincapie et al [ 29 ] defined the elastic turbulence characteristics as follows: (1) changing stream width, (2) changing stream direction, (3) penetration of the stream into small corners, (4) build-up and immediate collapse of vortices and (5) streamline crossing, especially near grains. Rock et al [ 11 ] consider the penetration of small corners and build-up of vortices, in particular, as the main reason for an increased oil recovery due to viscoelastic effects, as observed by Clarke et al [ 55 ]. This will be discussed in detail in the coming section.…”
Section: Viscoelasticity In Enhanced Oil Recoverymentioning
confidence: 99%
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“…As a summary of the streamline visualization, Hincapie et al [ 29 ] defined the elastic turbulence characteristics as follows: (1) changing stream width, (2) changing stream direction, (3) penetration of the stream into small corners, (4) build-up and immediate collapse of vortices and (5) streamline crossing, especially near grains. Rock et al [ 11 ] consider the penetration of small corners and build-up of vortices, in particular, as the main reason for an increased oil recovery due to viscoelastic effects, as observed by Clarke et al [ 55 ]. This will be discussed in detail in the coming section.…”
Section: Viscoelasticity In Enhanced Oil Recoverymentioning
confidence: 99%
“…Since the sandstone resembling micromodels usually do not consist of single, circle-shaped grains, it is not possible to determine D p visually with an image algorithm. Therefore, Rock et al [ 11 ] proposed the rearrangement of the Ergun equation [ 92 ] which is given by: where L is the flow length along the micromodel, Δ p the measured differential pressure along the micromodel and µ the viscosity of the fluid. Since the viscosity of the viscoelastic polymer solutions change with different flow rates, it is necessary to determine D p with the pressure data obtained during the permeability flooding with deionized water which is a Newtonian fluid and hence, has no viscosity changes with changing flow rates.…”
Section: Viscoelasticity In Enhanced Oil Recoverymentioning
confidence: 99%
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“…Mechanical degradation might occur along with the onset of shear thickening [51]. Onset of shear thickening has received a great attention in the literature as it is an indication of viscoelasticity in porous medium [50,[52][53][54][55]. Any alteration of the molecular structure of HPAM through exposing it to shear rate above or below the onset of shear thickening may change its apparent shear thickening behavior [56].…”
Section: Polymer Injectivity and Mechanical Degradationmentioning
confidence: 99%
“…Mechanical degradation might occur along with the onset of shear thickening [51]. Onset of shear thickening has deserved high attention in the literature as it is an indication of viscoelasticity in porous medium [50,[52][53][54][55]. Any alteration of molecular structure of HPAM through exposing HPAM to shear rate above or below the onset of shear thickening may change its apparent shear thickening behavior [56].…”
Section: Mechanical Degradationmentioning
confidence: 99%