Hostname: page-component-7b7567c8c-2n9c9 Total loading time: 0 Render date: 2026-11-15T10:32:36.096Z Has data issue: false hasContentIssue false

A semi-infinite hydraulic fracture driven by a shear-thinning fluid

Published online by Cambridge University Press:  25 January 2018

Fatima-Ezzahra Moukhtari
Affiliation:
Geo-Energy Laboratory - Gaznat Chair on Geo-Energy, Ecole Polytechnique Fédérale de Lausanne, ENAC-IIC-GEL-EPFL, Station 18, CH-1015, Switzerland
Brice Lecampion*
Affiliation:
Geo-Energy Laboratory - Gaznat Chair on Geo-Energy, Ecole Polytechnique Fédérale de Lausanne, ENAC-IIC-GEL-EPFL, Station 18, CH-1015, Switzerland
*
†Email address for correspondence: brice.lecampion@epfl.ch

Abstract

We use the Carreau rheological model which properly accounts for the shear-thinning behaviour between the low and high shear rate Newtonian limits to investigate the problem of a semi-infinite hydraulic fracture propagating at a constant velocity in an impermeable linearly elastic material. We show that the solution depends on four dimensionless parameters: a dimensionless toughness (function of the fracture velocity, confining stress, material and fluid parameters), a dimensionless transition shear stress (related to both fluid and material behaviour), the fluid shear-thinning index and the ratio between the high and low shear rate viscosities. We solve the complete problem numerically combining a Gauss–Chebyshev method for the discretization of the elasticity equation, the quasi-static fracture propagation condition and a finite difference scheme for the width-averaged lubrication flow. The solution exhibits a complex structure with up to four distinct asymptotic regions as one moves away from the fracture tip: a region governed by the classical linear elastic fracture mechanics behaviour near the tip, a high shear rate viscosity asymptotic and power-law asymptotic region in the intermediate field and a low shear rate viscosity asymptotic far away from the fracture tip. The occurrence and order of magnitude of the extent of these different viscous asymptotic regions are estimated analytically. Our results also quantify how shear thinning drastically reduces the size of the fluid lag compared to a Newtonian fluid. We also investigate simpler rheological models (power law, Ellis) and establish the small domain where they can properly reproduce the response obtained with the complete rheology.

Information

Type
JFM Papers
Copyright
© 2018 Cambridge University Press 
Figure 0

Figure 1.Viscosity as function of shear rate for two fracturing fluids: Hydroxypropylguar (HPG – data taken from Guillot & Dunand 1985) and in inset a viscoelastic surfactant (VES – data taken from Kefi et al.2004). These experimental data do not cover the large shear rate region where the viscosity typically tends toward the solvent viscosity (water in those cases) – see e.g. Pipe, Majmudar & McKinley (2008) for experimental data on Xanthan gum covering the complete range of shear rates. A number of rheological models can be used to reproduce these data over parts or all of the range of shear rates. We display here the best fit for the power-law (dashed brown line), Carreau (continuous black line) and Ellis (dot-dashed red line) rheological models. The corresponding best-fit parameters are listed in table 1 for these two fluids and the different models.

Figure 1

Table 1.Rheological parameters of HPG and VES fluids (for a given temperature) for the power-law, Carreau and Ellis models corresponding to the experimental data of figure 1. Note that the majority of fracturing fluids have a power-law index $n$ between $0.1$ and $0.5$.

Figure 2

Figure 2.Fluid velocity profiles for a lubrication flow between parallel plates (as it occurs within a fracture) at a given mean velocity $\langle u\rangle =V=1~\text{m}~\text{s}^{-1}$ for Carreau, power-law, Ellis and Newtonian fluids. The corresponding fluid pressure gradient is also displayed for each model. The rheological parameters correspond to an HPG fluid (see table 1 for the different models, figure 1 for the rheogram). For the Newtonian velocity profile (dotted green line), the low shear rate viscosity of the HPG is used. Note that the solution for a Carreau fluid is semi-analytical while the solution for the other models can be obtained analytically (see appendices A, B and C for details).

Figure 3

Figure 3.Sketch of a semi-infinite hydraulic fracture propagating at a constant velocity $V$ in an impermeable elastic material under a pre-existing normal compressive stress $\unicode[STIX]{x1D70E}_{o}$. A fluid lag zone of a priori unknown length $\unicode[STIX]{x1D706}$ adjacent to the fracture tip may be present.

Figure 4

Figure 4.Dimensionless fracture opening $w/\unicode[STIX]{x1D716}L_{\unicode[STIX]{x1D707}_{o}}$ along the fracture for $\unicode[STIX]{x1D705}=0,0.002,0.008,0.043,0.33,0.74$ (with corresponding lag size $\unicode[STIX]{x1D6EC}=0.049,0.048,0.047,0.041,0.008,8.3\times 10^{-8}$) in log–log scale for $\unicode[STIX]{x1D6FC}=10^{2}$, $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$, and $n=0.5$. The dashed lines correspond to the asymptotic solution in the toughness dominated regime ($\unicode[STIX]{x1D705}$-asymptote), power-law viscosity regime ($m_{n}$-asymptote) and low shear rate Newtonian viscosity regime ($m_{o}$-asymptote).

Figure 5

Figure 5.Dimensionless apparent viscosity $\unicode[STIX]{x1D6E4}$ along the fracture starting from the fluid front $\unicode[STIX]{x1D709}=\unicode[STIX]{x1D6EC}$ for $\unicode[STIX]{x1D705}=0$ ($\unicode[STIX]{x1D6EC}=0.049$) and $\unicode[STIX]{x1D705}=0.74$ ($\unicode[STIX]{x1D6EC}=8.3\times 10^{-8}$) in log–log scale for $\unicode[STIX]{x1D6FC}=10^{2}$, $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$, and $n=0.5$.

Figure 6

Figure 6.Dimensionless fluid pressure $p/\unicode[STIX]{x1D70E}_{o}$ along the fracture for $\unicode[STIX]{x1D705}=0,0.002,0.008,0.043,0.33,0.74$ in semi-log scale for $\unicode[STIX]{x1D6FC}=10^{2}$, $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$, and $n=0.5$. The dashed lines correspond to the asymptotic solution of pressure in the power-law viscosity regime ($m_{n}$-asymptote) and in the Newtonian viscosity regime ($m_{o}$-asymptote).

Figure 7

Figure 7.Extent of the regions where the numerical solution can be approximated by the different asymptotes ($\unicode[STIX]{x1D705}$-asymptote, $m_{n}$-asymptote and $m_{o}$-asymptote) with accuracy of $10^{-2}$ as function of dimensionless toughness with $\unicode[STIX]{x1D6FC}=10^{2},\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3},n=0.5$. The position of the fluid lag is also displayed for comparisons.

Figure 8

Figure 8.Dimensionless lag length $\unicode[STIX]{x1D706}/L_{\unicode[STIX]{x1D707}_{o}}$ versus the dimensionless toughness $\unicode[STIX]{x1D705}$ for a Carreau rheology for different values of $\unicode[STIX]{x1D6FC}$ ($\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3},n=0.5$). The corresponding results for a power-law rheology are also displayed for $\unicode[STIX]{x1D6FC}=10^{5}$ and $\unicode[STIX]{x1D6FC}=10^{3}$ for comparison.

Figure 9

Figure 9.(a) Dimensionless fracture opening $w/\unicode[STIX]{x1D716}L_{\unicode[STIX]{x1D707}_{o}}$ along the fracture for $\unicode[STIX]{x1D705}=0,0.013,0.045,0.085,0.11$ (with corresponding lag size $\unicode[STIX]{x1D6EC}=0.0004,0.00025,5.8\times 10^{-5},2.5\times 10^{-6},8.3\times 10^{-8}$) in log–log scale for $\unicode[STIX]{x1D6FC}=10^{7}$, $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$ and $n=0.5$ (the dashed lines correspond to the asymptotic solution of opening in the toughness dominated regime ($\unicode[STIX]{x1D705}$-asymptote), high shear rate Newtonian viscosity regime ($m_{\infty }$-asymptote) and the power-law viscosity regime ($m_{n}$-asymptote)). (b) Corresponding dimensionless apparent viscosity $\unicode[STIX]{x1D6E4}$ starting from the fluid front $\unicode[STIX]{x1D709}=\unicode[STIX]{x1D6EC}$ for $\unicode[STIX]{x1D705}=0,0.11$.

Figure 10

Figure 10.Dimensionless lag length $\unicode[STIX]{x1D706}/L_{\unicode[STIX]{x1D707}_{o}}$ versus the dimensionless toughness $\unicode[STIX]{x1D705}$ for different values of $n$, ($\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3},\unicode[STIX]{x1D6FC}=10^{2}$).

Figure 11

Figure 11.Dimensionless lag length $\unicode[STIX]{x1D706}/L_{\unicode[STIX]{x1D707}_{o}}$ versus the dimensionless toughness $\unicode[STIX]{x1D705}$ for a Carreau rheology with respect to $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}$ ($\unicode[STIX]{x1D6FC}=10^{3},n=0.5$). The results for a power-law rheology are also displayed for $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$.

Figure 12

Figure 12.Dimensionless fracture opening $w/\unicode[STIX]{x1D716}L_{\unicode[STIX]{x1D707}_{o}}$ along the fracture in log–log scale for Carreau (with $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$), Ellis, power-law rheology: (a) $\unicode[STIX]{x1D6FC}=7\times 10^{3}$ ($\unicode[STIX]{x1D6FC}_{e}=4975$, Ellis model), $n=0.46$ and $\unicode[STIX]{x1D705}=0.01$, (b) $\unicode[STIX]{x1D6FC}=10^{6}$ ($\unicode[STIX]{x1D6FC}_{e}=7.2\times 10^{5},$ Ellis model), $n=0.46$ and $\unicode[STIX]{x1D705}=0.002$.

Figure 13

Table 2.Characteristic scales for the zero-lag case for the three different rheology. The low shear rate viscosity Newtonian scaling is used for both the Ellis and Carreau model.

Figure 14

Table 3.Transition length scales between the different asymptotic regions expressed as a function of the asymptotes characteristic scales (4.1) and directly as function of the problem parameters.

Figure 15

Figure 13.Occurrence of the different viscous asymptotes as a function of $\bar{\unicode[STIX]{x1D6FC}}$ and $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}$ for $n=0.46$. Three distinct regions separate the parametric space: region A defined as $\bar{\unicode[STIX]{x1D6FC}}<\bar{\unicode[STIX]{x1D6FC}}_{l_{n}}(\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o},n)$ where the solution transitions from $k$ directly to $m_{o}$, region B defined as $\bar{\unicode[STIX]{x1D6FC}}_{l_{n}}(\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o},n)<\bar{\unicode[STIX]{x1D6FC}}<\bar{\unicode[STIX]{x1D6FC}}_{l_{\infty }}(\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o},n)$ where three asymptotes $k$, $m_{n}$ and $m_{o}$ can be observed and region C defined for $\bar{\unicode[STIX]{x1D6FC}}>\bar{\unicode[STIX]{x1D6FC}}_{l_{\infty }}(\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o},n)$ where up to four asymptotes $k$, $m_{\infty }$, $m_{n}$ and $m_{o}$ may be observed. The dot-dashed orange lines refer to the coordinates of the numerical simulations performed in figure 14.

Figure 16

Figure 14.Numerical bounds and transition length scales (black solid lines) between the different asymptotic regions: (a) variations of $\bar{\unicode[STIX]{x1D6FC}}$ for $n=0.46,$$\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$, (b) variations of $\bar{\unicode[STIX]{x1D6FC}}$ for $n=0.46,$$\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-1}$, (c) variations of $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}$ for $n=0.46,$$\bar{\unicode[STIX]{x1D6FC}}=10^{2}$ and (d) $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}$ for $n=0.46,$$\bar{\unicode[STIX]{x1D6FC}}=10^{5}$. The regions where the numerical results fall within $1\,\%$ of accuracy of an asymptote are also displayed. For the power-law region, limits where the numerical results are within $1\,\%$ accuracy of the $m_{n}$ asymptote are displayed in red, and in orange when within $5\,\%$ of accuracy.

Figure 17

Figure 15.Zero-lag case. Dimensionless fracture opening $w/w_{m_{o}k}$ as a function of the dimensionless distance from the tip $x/\ell _{m_{o}k}$ for the three rheologies (see table 2 for the expressions of the characteristic scales $w_{m_{o}k}$ and $\ell _{m_{o}k}$). The rheological parameters of the fluid are those of HPG. Influence of $\bar{\unicode[STIX]{x1D6FC}}$ with $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$: (a) $\bar{\unicode[STIX]{x1D6FC}}=74\times 10^{-8}$ (Ellis $\bar{\unicode[STIX]{x1D6FC}}_{e}=53.4\times 10^{-8}$), (b) $\bar{\unicode[STIX]{x1D6FC}}=74$ (Ellis $\bar{\unicode[STIX]{x1D6FC}}_{e}=53.4$; (c) $\bar{\unicode[STIX]{x1D6FC}}=10^{3}$ (Ellis $\bar{\unicode[STIX]{x1D6FC}}_{e}=2088.7$), (d) $\bar{\unicode[STIX]{x1D6FC}}=46.2\times 10^{3}$ (Ellis $\bar{\unicode[STIX]{x1D6FC}}_{e}=33.4\times 10^{3}$) with also the solution for different $\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}$ for the Carreau model. The Ellis model starts to depart from the Carreau in the intermediate region for $\unicode[STIX]{x1D6FC}\geqslant 10^{3}$ even for a large shear-thinning magnitude ($\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$).

Figure 18

Table 4.Values of the dimensionless parameters for example hydraulic fracturing fluids and materials for propagating velocity $V$. PMMA data from Bunger & Detournay (2008) and Bebertal sandstone data from Stoeckhert et al. (2015).

Figure 19

Figure 16.Exact and interpolated values of the dimensionless tangent viscosity in log–log scale with respect to the wall shear stress for different values of $\unicode[STIX]{x1D6FC}$ and: $n=0.46,\unicode[STIX]{x1D707}_{\infty }/\unicode[STIX]{x1D707}_{o}=10^{-3}$.