Geophys. J. Int. (2006) 164, 685–696 doi: 10.1111/j.1365-246X.2005.02827.x
Linear pressurization method for determining hydraulic permeability and specific storage of a rock sample
I. Song and J. Renner Institute for Geology, Mineralogy and Geophysics, Ruhr-University Bochum, D-44780 Bochum, Germany. E-mail: [email protected]
Accepted 2005 October 4. Received 2005 September 28; in original form 2005 July 4 Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021 SUMMARY We studied the methodology and applicability of linear pressurization for determining simul- taneously hydraulic permeability and specific storage of a rock sample. We analytically solved the governing equation for 1-D pressure diffusion through a homogenous, isotropic cylindrical rock specimen located between a downstream and an upstream reservoir considering linear pressurization of the upstream fluid as the boundary condition. The solution consists of a transient and a steady state for which both differential pressure between the two reservoirs and injection rate at the upstream reservoir assume constant values. Since the steady-state differential pressure is linearly proportional to the compressive storage of the downstream reservoir, tests conducted with a systematic variation of the size of the downstream reservoir permit determining permeability and specific storage from the intercept and slope of the linear relationship. Alternatively, simultaneous measurement of differential pressure and fluid injec- tion rate at steady-state conditions provides a basis for calculation of the hydraulic properties as previously presented for linear injection. Experiments were performed on Fontainebleau sandstone samples to document the feasibility of the method. The determined storage ca- pacity value is used to calculate various poroelastic parameters, such as bulk and pore-space compressibility, Skempton and the effective pressure coefficient. Key words: fluids in rocks, linear pressurization, permeability, poroelasticity, specific storage capacity.
1 INTRODUCTION Rocks are characterized by two hydraulic properties, the capacity for storing the fluid and the ability to transmit it. If fluid is injected into a saturated porous medium, one part of the fluid is stored in the pore space due to the deformation of the fluid and voids, while the other part is transported through interconnected conduits due to the pore pressure gradient. In a homogenous isotropic porous rock, laminar fluid flow is governed by permeability k defined through Darcy’s empirical relationship: =−k ∇ , q μ p (1)
where q , ∇ p, and μ denote the specific discharge, the pore pressure gradient and the dynamic fluid viscosity, respectively. In poroelasticity GJI Volcanology, geothermics, fluids and rocks
(e.g. Biot 1941; Detournay & Cheng 1988, 1993; Rice & Cleary 1976), the specific storage capacity, β s, denotes the proportionality constant between the volume of fluid stored per unit volume of rock, ζ , and the pore fluid pressure, p, in a sample under constant applied stress (e.g. Wang 2000):
ζ = βs p. (2) Consideration of mass conservation during the fluid flow yields a fluid continuity constraint expressed as a relationship between ζ and the specific discharge, q (e.g. Detournay & Cheng 1988, 1993; Rice & Cleary 1976; Wang 2000): ∂ζ =−∇· q. (3) ∂t Combining Darcy’slaw (eq. 1), the constitutive relation (eq. 2), and the continuity eq. (3) with the assumption that the hydraulic properties, β s, k and μ, are constant yields the partial differential equation describing temporal and spatial variations of pore fluid pressure in homogeneous, isotropic porous media (e.g. Rice & Cleary 1976): 1 ∂p ∇2 p − = 0, (4) κ ∂t where κ = k/(μβ s) denotes the hydraulic diffusivity.
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The emphasis of previous experimental and theoretical studies has clearly been on determining permeability (e.g. Bernab´e1987; Brace et al. 1968; Kwon et al. 2001; Lin 1982; Lin et al. 1986; Zeynaly-Andabily & Rahman 1995; Zoback & Byerlee 1975), though the hydraulic diffusivity, that is, the ratio between transport and storage efficiency, controls the pore pressure variations for time-dependent pressure gradients. The neglect of the storage parameter is partly related to the simple realization of steady-state methods applying Darcy conditions (eq. 1) to highly permeable rocks. For low-permeability rocks, the evaluation of transient pressure records circumvents long experimental durations (Hsieh et al. 1981; Song et al. 2004a; Zeynaly-Andabily & Rahman 1995) and the explicit measurement of flow rate. However, the procedure of calculating both hydraulic parameters, k and β s, using the transient pressure curve often involves cumbersome curve matching routines (Hsieh et al. 1981; Neuzil et al. 1981; Zeynaly-Andabily & Rahman 1995). Experimental design for the commonly used pressure pulse method (Brace et al. 1968) aims at negligible storage capacity of the sample compared to storage capacities of the reservoirs of the pore pressure system greatly simplifying analysis but leaving sample storage capacity undetermined. From a practical point of view, it is clearly desirable to measure storage capacity routinely together with permeability rather than performing separate tests (e.g. Green & Wang 1986; Hart & Wang 1995; Tokunaga & Kameya 2003). From a scientific perspective, focus should be on determination of the central parameter, hydraulic diffusivity, and its sensitivity to changes in conditions to which a sample Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021 is subjected rather than just the transport contribution. Furthermore, storage capacity is an important physical property on its own. Firstly, it determines the yield of reservoirs. The common practice to approximate the storage capacity by the product of fluid compressibility and porosity may fail for compliant pore space, fractured and jointed reservoirs. Secondly, the storage capacity controls the change in pore pressure as a result of a change in external pressure. Thus, if routinely performed in a systematic way, measurements of the specific storage capacity may contribute significantly to our understanding of stress transfer occurring during earthquakes (e.g. Lockner & Stanchits 2002; Pride et al. 2004; Stein 1999). The oscillatory pore pressure method (Fischer 1992) permits determination of both hydraulic parameters. However, it appears that in many cases the determination of the storage capacity remains rather uncertain, that is, not better constrained than to an order of magnitude (e.g. Rutter & Faulkner 1996). Recently, a linear flow injection technique was introduced permitting straightforward graphical determination of both, permeability and specific storage (Song et al. 2004b). The experimental arrangement consisted of a cylindrical specimen between two fluid reservoirs one of which is connected to a pump. By minimizing the storage capacity of the reservoirs, this method worked for tight micritic limestone with very low permeability down to 4 × 10−21 m2 (Song et al. 2002). Here, we suggest a technique in which instead of a constant flow-rate injection a linear pressurization is conducted at the upstream reservoir. This technique can be easily applied with a pressure-controlled hydraulic actuator. We present the analytic solution of the governing equation with the boundary condition of linear pressurization of the upstream reservoir inducing injection of fluid into a specimen located between a downstream and an upstream reservoir (Fig. 1a). The theoretical analysis of the solution provides two different approaches for determination of permeability and specific storage for which we present design considerations and experimental examples.
2 THEORETICAL ANALYSIS For 1-D pressure diffusion through a homogeneous, isotropic porous medium with pressure-independent hydraulic properties, the diffusion eq. (4) is expressed as: ∂2 p(x, t) 1 ∂p(x, t) − = 0. (5) ∂x 2 κ ∂t A constant pore pressure along the rock specimen equilibrated with up and downstream pressure constitutes the initial condition: p(x, 0) = 0 for 0 ≤ x ≤ L. (6)
During the test (t > 0), boundary conditions are determined by the pressurization of the upstream reservoir (x = L) with a constant rate: dp(L, t) = p˙ for t > 0, (7) dt u and by the sensitivity of the downstream reservoir (x = 0): μS ∂p(0, t) ∂p(0, t) d − = 0 for t > 0, (8) kA ∂t ∂x where
p(x, t): pore fluid pressure along a sample as a function of x and t (Pa) x: distance along the sample from the downstream boundary (m) t: time from the start of the experiment (s) A: cross-sectional area of the sample (m2) L: length of the sample (m) k: permeability of the sample (m2) μ: dynamic fluid viscosity (Pa s) −1 β s : specific storage of the sample (Pa ) 3 −1 Sd, Su: storage capacity of the down- and upstream reservoir (m Pa ) −1 p˙ u: constant pressurization rate of the upstream fluid (Pa s ).
C 2006 The Authors, GJI, 164, 685–696 Journal compilation C 2006 RAS Linear pressurization method for determining hydraulic permeability 687
downstream upstream reservoir reservoir
sample pressure pressure time time x x = 0 x = L (a)
downstream reservoir upstream reservoir
displacement transducers Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021 bypass valve
spacers main intensifier
sample
auxiliary intensifier confining pressure cell pressure pressure transducer transducer (b)
Figure 1. Schematic diagrams showing (a) the boundary conditions for linear pressurization and (b) the experimental test system composed of a cored rock specimen located between two reservoirs one of which is connected to two pressure intensifiers. The auxiliary intensifier was used for maintaining the initial volume of upstream reservoir constant at any initial pressure level. The volume of downstream reservoir was controlled by placing up to three steel spacers (white blocks) into the reservoir.
The boundary conditions and their experimental realization are illustrated in Figs 1(a) and (b), respectively. The partial differential eq. (5) with the initial and boundary conditions given by eqs (6)–(8) was solved using Laplace transforms (see Appendix A). The pore fluid
pressure divided by the upstream pressurization rate p˙ u is found as 2 2 2 ∞ x x 2 p(x, t) x − L μS 2L cos ϕm − ϕm δ sin ϕm κϕ = t + + d (x − L) + L L exp − m t , (9) κ κ ϕ2 ϕ2 δ − ϕ + ϕ + δ ϕ 2 p˙ u 2 kA m=1 m m 4 cos m m (1 5 ) sin m L where we introduced the dimensionless ratio of the storage capacities of the downstream reservoir and the sample S δ = d . (10) βs AL −1 The eigenvalues ϕ m are the roots of tan ϕ = (δϕ) . The analytic solution (eq. 9) consists of two parts: a transient exponentially decaying with time and a steady state in the form of a linear function of time t and a parabolic function of position x. At steady state, the pressure at a given
position increases linearly with the rate of the upstream pressurization, p˙ u, and the pore pressure distribution along the specimen is described
by a parabolic curve characterized by the hydraulic properties of the specimen, β s and k, the compressive storage of the downstream reservoir, S d and the dynamic viscosity of the fluid, μ. For a systematic discussion, we introduce dimensionless time κt τ = , (11) L2 and dimensionless position x ξ = , (12) L yielding a dimensionless pore pressure κ p(ξ,τ) P(ξ,τ) ≡ . (13) 2 L p˙ u The dimensionless version of the solution (eq. 9) reads ∞ 1 cos(ϕ ξ) − ϕ δ sin(ϕ ξ) P(ξ,τ) = τ + [ξ 2 + 2δξ − (1 + 2δ)] + 2 m m m exp −ϕ2 τ . (14) ϕ2 ϕ2 δ − ϕ + ϕ + δ ϕ m 2 m=1 m m 4 cos m m (1 5 ) sin m
C 2006 The Authors, GJI, 164, 685–696 Journal compilation C 2006 RAS 688 I. Song and J. Renner
10 1.6 upstream δ P =0.0 8 δ =0.2 1.2 δ =0.4 δ =0.6 6 δ =0.8 δ =1.0 0.8 4 δ =0.0 δ =0.2 δ 0.4 =0.4 2 δ =0.6
Dimensionless pressure, δ =0.8 dashed lines for downstream pressure δ =1.0 Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021 0 Dimensionless differential pressure 0.0 02468100246810 (a) Dimensionless time, τ (b) Dimensionless time, τ
Figure 2. Theoretical curves of (a) fluid pressures at the upstream and downstream reservoirs and (b) the differential pressures between them as a function of time in a dimensionless domain for different values of δ, the ratio of the compressive storage of the downstream to that of the specimen. The solid line represents the linear variation of the upstream pressure P u(τ), as given by the boundary condition (eq. 7). The dashed lines clearly show a transient stage in the downstream pressure during which P d(τ) increases with increasing rate until its slope becomes equal to that of P u(τ). The reaction of the downstream pressure is slower and thus the pressure difference becomes larger for the larger δ. In a real test, the pore fluid pressure is measured only at the upstream and downstream reservoirs corresponding to ξ = 1 and ξ = 0, respectively, thus the dimensionless up and downstream pressures become
Pu(τ) ≡ P(1,τ) = τ, (15) and ∞ 1 exp −ϕ2 τ P (τ) ≡ P(0,τ) = τ − − δ + 2 m , (16) d ϕ2 ϕ2 δ − ϕ + ϕ + δ ϕ 2 m=1 m m 4 cos m m (1 5 ) sin m respectively. The dimensionless analytic solution (eq. 14) depends on only one parameter, the dimensionless ratio of storage capacities δ. Thus, it is of fundamental importance to understand how δ affects fluid flow along the porous medium. First, we examine the role of δ for the response of downstream pressure to the variation of upstream pressure. Theoretical curves of dimensionless fluid pressure at upstream and downstream reservoirs as a function of the dimensionless time τ for different values of δ demonstrate that the response of the downstream pressure is slower for larger δ, that is, the duration of the transient stage increases with the magnitude of δ (Fig. 2a). After the transient stage (for large τ), the differential pressure between the two reservoirs stabilizes at a constant value (Fig. 2b) that is linearly proportional to the value of δ:
∞ κ p − 1 P∞ ≡ P (∞) − P (∞) = u p = + δ. (17) u-d u d 2 L p˙ u 2
1.0 1.0 τ = 0.02 τ = 0.32 τ = 0.08 τ = 0.64 0.8 τ = 0.16 0.8 τ ) = 1.28 ) τ τ , τ = 0.32 , τ = 2.56 ξ ξ ( τ = 0.64 ( τ = 5.12 P 0.6 P Δ 0.6 τ = 1.28 Δ τ = 10.24 τ = 2.56 τ = 20.48 asymptotic Asymptotic 0.4 0.4 δ = 0 δ = 10 Normalized Normalized Normalized Normalized 0.2 0.2
0.0 0.0 0 0.2 0.4 0.6 0.8 1 0 0.2 0.4 0.6 0.8 1 (a) Dimensionless position,ξ (b) Dimensionless position,ξ
Figure 3. Normalized dimensionless differential pore pressure, P(ξ, τ)/ P(1, ∞), along the specimen at different dimensionless times for (a) δ = 0 and (b) δ = 10. As δ is raised, the duration of the transient stage becomes longer, and the pore pressure variation at a given time becomes more linear along the specimen.
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1.0
0.8 p /p u p δ = 1000 0.6 δ δ = 10 = 100
δ = 1 0.4
Normalized pressure Normalized 0.2 S = S p /p u d d p Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021
0.0 0.001 0.01 0.1 1 10 100 1000 104 Dimensionless time, τ
Figure 4. Comparison between the evolution of pressure with dimensionless time, τ, for the linear pressurization method (solid lines) and the pressure pulse technique (dashed lines) at various values of the dimensionless ratio of sample and downstream storage capacity, δ, and identical size of up and downstream reservoirs, Su = Sd. Up and downstream pressures were normalized by the height of the pulse, pp, for the pulse technique. For the linear pressurization method, τ / ∞ the pressure difference between up and downstream was normalized to its asymptotic value, P u−d( ) Pu−d.
For the analysis of the pore pressure distribution along the specimen, we introduce the difference between the dimensionless pore pressure
along the sample P(ξ, τ) and the dimensionless downstream pore pressure P d(τ):
∞ 1 cos(ϕ ξ) − ϕ δ sin(ϕ ξ) − 1 P(ξ,τ) ≡ P(ξ,τ) − P (τ) = (ξ 2 + 2δξ) + 2 m m m exp − ϕ2 τ . (18) d ϕ2 ϕ2 δ − ϕ + ϕ + δ ϕ m 2 m=1 m m 4 cos m m (1 5 ) sin m
As δ is raised, the duration of the transient stage becomes longer (Fig. 2). At steady state, the pressure distribution along the sample is a parabolic function of position characterized only by δ. With increasing δ, the pore pressure variation along the specimen becomes more linear (solid lines in Fig. 3). In comparison to the widely applied pressure pulse technique (e.g. Hsieh et al. 1981), the linear pressurization method
requires slightly longer experimental duration for the same δ and S u = S d (Fig. 4).
3 DETERMINATION OF PERMEABILITY AND SPECIFIC STORAGE Linear pressurization of the upstream reservoir permits determining hydraulic properties in two ways.
3.1 Varying the storage capacity of the downstream reservoir ∞ The ratio between the steady-state differential pressure, pu−d, and the upstream pressurization rate, p˙ u, is a linear function of the storage capacity of the downstream reservoir (from eq. 9) ∞ ∞ ∞ μβ 2 μ pu−d pu pd s L L = − = + Sd, (19) p˙ u p˙ u p˙ d 2k kA
where p˙ u = p˙ d at steady-state condition. If linear pressurization experiments are performed with several different sizes of the downstream ∞ / reservoir, evaluation of the relation between pu−d p˙ u and S d permits the determination of permeability and specific storage. On a first glance, the necessity to perform several experiments appears as a disadvantage. However, the advantage of this approach lies in the determination of storage capacity based on pressure readings alone after the characteristics of the downstream reservoir are thoroughly determined once. The insertion of geometrically simple objects into the downstream reservoir constrains the relative sizes of the reservoir realizations (Fig. 1b).
3.2 Measuring flow rate and the storage capacity of upstream reservoir For our choice of coordinate system, the 1-D Darcy law is expressed as: k ∂p(x, t) Q(x, t) =−q(x, t)A = A, (20) μ ∂x where Q(x, t) is the volume of fluid crossing an area A per unit time in the direction of the x-axis. For increasing upstream pressure, the
actual flow rate in the specimen is neither constant nor equal to the rate derived from the speed vp of the piston in the actuator (Fig. 1b). The
C 2006 The Authors, GJI, 164, 685–696 Journal compilation C 2006 RAS 690 I. Song and J. Renner
100 108 7 δ = 0 10 e δ = 2 10000 6 -1 δ = 4 10 -log( / (s) Duration 10 5 δ = 6 10 1000 δ 100 = 8 4 δ 10 = 10 3 10 -2 10 10 1 102 1 0.1
10 0.01 e -3 0 10 10 ) -1 μβ L2/k 10 s Normalized transient part, 10-2 -4 -3 Downloaded from https://academic.oup.com/gji/article/164/3/685/2133401 by guest on 23 September 2021 10 Normalized differential pressure (s) 10 0204060801000.001 0.01 0.1 1 10 100 1000 (a) Dimensionless time, τ (b) Storage capacity ratio, δ
Figure 5. (a) The normalized contribution of transient flow, e, as a function of dimensionless time for different δ . The dimensionless time doubles for every order of magnitude reduction in the contribution of transient flow. The dashed horizontal line indicates a contribution of less than 1 per cent to ∞ ∞ / the differential pressure, pu−d, as an approximate bound for experimental resolution. (b) Normalized differential pressure ( pu−d p˙u) and experimen- tal duration to reach a contribution e of the transient solution as a function of δ. The open and the closed circles indicate how the diagram can be used 2 for two samples differing by three orders of magnitude in normalized hydraulic properties. If for the sample with ‘low permeability’ (μβ s L /k = 10) 2 downstream storage capacity is chosen such that δ = 0.01 and for the ‘high-permeability’ sample (μβ s L /k = 0.01) downstream storage capacity is chosen such that δ 600, then for either sample, the normalized differential pressure of about 6 s (left y-axis) corresponds to an easily mea- surable difference of 1 MPa at a pressurization rate of 1/6 MPa/s and a contribution e = 10−2 of the transient is reached after a duration of −log (10−2) × 10 s = 20 s (right y-axis). relationship between the actual flow rate into the specimen at the upstream boundary (x = L), Q(L, t) ≡ Q u, and the rate of upstream volume change, Q p = Apvp, associated with the advancing piston of cross-section Ap is given as
Qu = Qp − Su p˙ u. (21) The steady-state pressure gradient at x = L can be obtained from the derivative of eq. (9) with respect to x: ∂p(L, t) μp˙ = u (β AL + S ) . (22) ∂x kA s d Substituting eqs (21) and (22) into the 1-D Darcy law (20) yields ∞ − + v∞ − Qp (Su Sd)p˙ u Ap p Stot p˙ u βs = = , (23) ALp˙ u ALp˙ u which upon insertion into eq. (19) gives