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Article

Pressure Transient Analysis for Vertical Well Drilled in Filled-Cave in Fractured Reservoirs

1
School of Petroleum and Natural Gas, Changzhou University, Changzhou 213164, China
2
State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southwest Petroleum University, Chengdu 610500, China
*
Author to whom correspondence should be addressed.
Fluids 2025, 10(12), 324; https://doi.org/10.3390/fluids10120324
Submission received: 28 October 2025 / Revised: 18 November 2025 / Accepted: 2 December 2025 / Published: 5 December 2025

Abstract

For capturing dynamic information about a filled-cave in the fractured reservoir, a novel Pressure Transient Analysis (PTA) analytical model for a well located at the filled-cave is established. In this new model, we consider the stress-sensitivity of the filled-cave and the inter-porosity flow of fracture. First, Perturbation transformation was used to obtain the pressure distribution in the filled-cave zone. Then, the Warren–Root model was applied to establish the pressure solution in the fractured reservoir. Next, the pressure and its derivative are obtained by the Laplace transformation and Steftest inversion. Lastly, the Bottomhole Pressure (BHP) and Bottomhole Pressure Derivative (BHPD) combined curve reveals the flow regimes of this novel model. The results show the composite model can be used to characterize the fractured reservoir with the filled-caves, and its flow follows the composite flow regimes. The spherical flow has an obvious slope of 0.5 on the BHPD curve, which can identify the size of the filled-caves. The boundary flow can be used to identify stress-sensitivity. Affected by the stress-sensitivity of the filled-cave, the BHPD’s slope of the boundary flow will be greater than 1. This research work provides technical support for capturing cave and fracture parameters in the fractured reservoir.

1. Introduction

In recent years, China’s marine carbonate oil reserves have been predominantly observed in the Tarim Basin, where the reservoirs are mainly characterized by fracture-cave type. The general geological framework and reserve distribution of such reservoirs have been documented in works like [1,2], while their specific characteristics and associated challenges are detailed in [3,4]. In these reservoirs, oil is mainly stored in natural fractures, caves, and the pores between cave fillings. The cave-filling space itself provides substantial storage capacity, and the complex nature of fluid flow in such fractured-vuggy carbonate reservoirs necessitates advanced modeling approaches, as demonstrated by multiphysics and multiscale methods [5]. Within this context, pressure transient analysis for wells penetrating filled-caves has been explored as a key to understanding these systems [6]. These filled-caves are not only critical storage spaces but also common targets that are easily drilled and completed [7,8].
Due to the differences in cementation and diagenesis history between the cave fillings and the surrounding rock, the filled-cave media often exhibit significant stress-sensitivity. This phenomenon, where permeability and porosity decrease with increasing effective stress, has been widely recognized in geomechanics [9] and specifically studied in carbonate reservoirs [10]. During production, a decrease in bottomhole pressure can readily alter the permeability of the near-wellbore formation, consequently directly influencing the productivity [11]. Therefore, precisely determining reservoir permeability plays a crucial role in subsequent productivity assessments. However, while the influence of stress-sensitivity on production is acknowledged, its explicit integration into well-test interpretation models for quantitative analysis remains a significant challenge. Furthermore, the discontinuous and highly heterogeneous nature of such reservoirs poses significant challenges for conventional core sampling and laboratory methods in accurately acquiring key physical parameters particularly permeability. The main reason is that due to the existence of natural fractures in the rock, the core sampling process is very easy to break, and it is difficult to obtain complete fracture rock samples under laboratory conditions, and rock parameters and permeability parameters cannot be obtained through testing.
Consequently, compared with conventional mean sandstone reservoirs, the use of pressure transient tests to obtain reservoir permeability [12,13,14] is very common in fracture-cavity reservoirs. However, the prevailing PTA (Pressure Transient Analysis) models suffer from key limitations when applied to wells drilled into filled-caves. Firstly, most existing models, including the foundational work by Gao et al. [6], do not consider the deformation characteristics of the medium filling the cave, making them unsuitable for analyzing wells drilled into the filling cave reservoir where stress-sensitive effects are pronounced. Secondly, conventional well-test models for fractured reservoirs predominantly assume radial flow geometry, as seen in studies like [15,16,17], or linearly supported radial flow [18], neglecting the distinct spherical flow characteristics [19,20] induced by the three-dimensional spatial geometry of a filled-cave. Consequently, such models are inadequate for characterizing the actual flow behavior in these complex systems, leading to potential misinterpretations, as discussed in [21,22]. This collective oversight of both the constitutive behavior of the filled-cave and its appropriate flow geometry defines a clear gap in the current modeling capabilities.
To solve these problems, we establish a novel composite model that incorporates the stress-sensitivity of filled-caves and the dual-porosity characteristics of the fractured reservoir, utilizing a spherical flow geometry. Perturbation theory and Laplace transform are used to solve the pressure solutions of each region for the inner and outer regions, respectively, and the global pressure response are obtained by coupling the pressure and flux at the composite interface. Finally, the flow regimes are identified using a combination curve of the bottomhole pressure (BHP) and its derivative, and the influence of various parameters on the pressure response and flow is analyzed. This work provides a technical foundation for characterizing cave and fracture parameters in the fractured-vuggy reservoir.

2. Methodology

2.1. Physical Model

The model idealizes a single, isolated karst cave body (a ‘bead’ in a bead-string structure [1,2,3,4]) surrounded by low-permeability matrix rock. The spherical representation is a simplification to leverage symmetry in deriving the analytical solution. As shown in Figure 1, one producing well is drilled into a filled-cave in the fractured reservoir. Compared with the surrounding fractured rock, the filled-cave formed relatively late, and its degree of compaction is much lower than that of the surrounding rock. Therefore, the filled-cave zone has high porosity, high permeability and high compressibility. The filled-cave is called the inner zone, its porosity is ϕ1, permeability is k1, the total compressibility is ct1, and the distance to the inner boundary is rf. The fractured rock is called the outer zone, its porosity is φ2, permeability is k2, the total compressibility is ct2, and the distance to the outer boundary is re. Other assumptions are as follows.
(1)
The producing well drills into the filled-cave, and the filled-cave zone is homogeneous. At the bottom of the wellbore is located in the ball center of the filled-cave, the fluid of the filled-cave flows into the wellbore through the perforated section in the form of spherical concentric flow.
(2)
Due to the main pressure-drop occurring around the wellbore and the compaction degree of the filled-cave being lower than the peripheral rock, the deformation caused by the stress-sensitivity of the filled-cave is considered in the flow process.
(3)
The peripheral rock develops natural fractures, and it is equivalent to the dual-porous medium. In the outer zone, the natural fracture is the flow channel, and the rock matrix is the storage volume without any infiltration capacity. In the pressure drop process, the internal fluid in the matrix only flows towards the rock fracture in the form of pseudo-steady-state.
(4)
The fluids present in both the inner and outer zones are single-phase and exist in a compressed liquid state. Within the rock fracture system, the internal fluid moves toward the filled-cave, exhibiting a spherical flow pattern that converges inward. There is no additional pressure loss induced by flow in the interface of the inner and outer zones.
(5)
Before the well is opened, the initial pressure is uniform throughout the reservoir. The test well is then produced at a constant rate. The impact of the wellbore storage effect and the formation skin effect are considered together.
(6)
The reservoir possesses a limited distance to its boundary, which may be either a closed (no-flow) type or a constant-pressure type. Throughout the entire flow process, variations in temperature and the effects of gravity are neglected.

2.2. Mathematical Model

The flow equation mathematically expresses the relationship between flow velocity and the pressure difference. For linear flow, it can be described by Darcy’s law
v = k μ p
where v is the flow velocity, m/s; k is permeability, m2; μ is viscosity, Pa·s; p is pressure, Pa.
In the production process with reservoir pressure decrease, reservoir fluid will be slightly compressed and formation rocks will slightly be deformed, their state equations are
ρ = ρ i e c L ( p p i ) ϕ = ϕ i e c f ( p p i ) k = k i e α k ( p p i )
where ρi density in the initial pressure, kg/m3; φi is porosity in the initial pressure, factor; ki is permeability in the initial pressure, m2; cL is the compressibility of liquid, 1/Pa; cf is the compressibility of formation, 1/Pa; αk is the deformation coefficient of permeability, 1/Pa.
Based on the principle of material balance, the continuity equation with the source item is
( ρ v ) + ρ q + ( ρ ϕ ) t = 0
where v is flow velocity, m/s; q is flowrate of source item, m3/s; t is the time, s.
Bring the flow Equation (1) and status Equation (2) into the continuous Equation (3) to obtain
2 p + q = 1 η p t
where the diffusivity conduction coefficient η with m2/s is
η = k μ ϕ c t
In the spherical coordinate system under symmetrical conditions, the differential diffusivity equation of inward spherical flow is expressed as
2 p r 2 + 2 r p r + q = 1 η p t
where r is the distance to the center of the ball, m.
The relationship between fluid flow and pressure is described by the Warren–Root (W-R) model, which relies on the assumption of pseudo-steady-state flow within the dual-porosity medium [23].
q = α k m μ ( p m p f )
where q is the flowrate m3/s; α is the shape factor of rock matrix, factor; km is the permeability of rock matrix, m2; pm is the pore fluid pressure at rock matrix, Pa; and pf is the pore fluid pressure at fracture, Pa.
The inter-porosity flow Equation (7) is brought into the diffusivity Equation (6) to obtain a differential diffusivity equation of composite inward spherical flow in stress-sensitive reservoir. To obtain a general form of diffusivity equation, the composite inward spherical flow with dimensions needs to be processed. Firstly, the dimensionless parameters are defined as shown in Table 1, where rw is wellbore radius, m; rf is composite distance, m; re is boundary distance, m; pi is initial pressure, MPa; C is wellbore storage coefficient, m3/MPa; S is skin factor, factor; B is fluid volume factor, factor; α is shape factor, m−2; αk is deformation coefficient of permeability, Pa−1; ϕ1 is porosity of inner zone, factor; k1 is permeability of inner zone, m2; ct1 is the total compressibility of inner zone, MPa−1; ϕ2 (ϕ2 = ϕ2m + ϕ2f) is porosity of outer zone, factor; ϕ2m is matrix porosity of outer zone, factor; φ2f is fracture porosity of outer zone, factor; k2 is permeability of outer zone, m2; k2m is the permeability of rock matrix of the outer zone, m2; k2f is the permeability of fracture of the outer zone, m2; ct2 (ϕ2ct2 = ϕ2mct2m + ϕ2fct2f) is the total compressibility of inner zone, MPa−1; ct2f is the fracture compressibility of inner zone, MPa−1; ct2m is the matrix compressibility of inner zone, MPa−1.
Then, the mathematical problems corresponding to the physical model are obtained by the initial condition and the inner and outer boundary conditions.
(1)
Dimensionless diffusivity equation of inward spherical flow in the stress-sensitive filled-cave (inner zone) is
2 p 1 D r D 2 + 2 r D p 1 D r D γ ( p 1 D r D ) 2 = e γ p 1 D p 1 D t D
(2)
See Appendix A, dimensionless diffusivity equation of inward spherical flow in the dual-pore media rock (outer zone) is
2 p 2 D f r D 2 + 2 r D p 2 D f r D + λ m ( p 2 D m p 2 D f ) = ω 12 M 12 ω f p 2 D f t D λ m ( p 2 D m p 2 D f ) = ω 12 M 12 1 ω f p 2 D m t D
(3)
Corresponding initial condition is
p 1 D ( t D = 0 ) = p 2 D f ( t D = 0 ) = 0
(4)
Corresponding flux condition in the wellbore, see Appendix B, is
C D d p w D d t D S e γ p 1 D r D p 1 D r D r w D = 1
(5)
Corresponding pressure condition in the wellbore, see Appendix B, is
p w D = p 1 D + S e γ p 1 D r D p 1 D r D r w D
(6)
Pressure condition in the interface of filled-cave and fractured rock is
p 1 D r f D = p 2 D f r f D
(7)
Flux condition in the interface of filled-cave and fractured rock is
p 1 D r D r f D = 1 M 12 p 2 D f r D r f D
(8)
If the boundary type is constant-pressure, the boundary condition can be written as
p 2 D f r e D = 0
(9)
If the boundary type is no-flow, the boundary condition can be written as
p 2 D f r D r e D = 0

2.3. Solution Approach

2.3.1. Inner Diffusivity Equation

The inner diffusivity equation contains a stress-sensitivity coefficient with an index form, which has strong non-linearity according to Pedrosa’s work [24], using Perturbation transformation to solve the non-linear flow equation. Perturbation transformation of the dimensionless is
p D = 1 γ L n ( 1 γ ζ D )
By Perturbation transformation, the outer diffusivity equation can be written as follows:
2 ζ 1 D r D 2 + 2 r D ζ 1 D r D = 1 1 γ ζ 1 D ζ 1 D t D
Based on Perturbation transformation, the ζD be also expanded as follows ζD0 + γζD1 + γ2ζD2 + ⋯. Hence, the term on the right-hand side of Equation (18) can also be expanded as follows:
1 1 γ ζ D = 1 + γ ζ D + γ 2 ζ D 2 +
Pedrosa [24] and Kikani [25] gave 0-, 1-, and 2-order approximation solutions of flow problems in the infinite-acting tress-sensitivity reservoir, respectively. Then the 0-order approximation of the inner flow equation is
2 ζ 1 D r D 2 + 2 r D ζ 1 D r D = ζ 1 D t D
By the Laplace transferring, the diffusivity equation of inner region is
2 ζ ¯ 1 D r D 2 + 2 r D ζ ¯ 1 D r D u ζ ¯ 1 D = 0
The diffusivity Equation (21) is a class of semi-level transformer Bessel Equations. The form of solution is
ζ ¯ 1 D = 1 r D [ A 1 sinh ( r D u ) + B 1 cosh ( r D u ) ]
The pressure gradient of distance to the center of ball can be written as
ζ ¯ 1 D r D = 1 r 2 D [ A 1 sinh ( r D u ) + B 1 cosh ( r D u ) ] + u r D [ A 1 cosh ( r D u ) + B 1 sinh ( r D u ) ]

2.3.2. Outer Diffusivity Equation

For the outer region, the corresponding diffusivity equation in the Laplace domain has the following mathematical representation:
2 p ¯ 2 D f r D 2 + 2 r D p ¯ 2 D f r D u f p ¯ 2 D f = 0 f = ω 12 M 12 λ m 1 ω f λ m + u 1 ω f + ω f
Equation (24) belongs to the Bessel Equation; its solution can be expressed as follows:
p ¯ 2 D f = 1 r D A 2 sinh ( r D u f ) + B 2 cosh ( r D u f )
The pressure guidance of spherical distance to the center of the ball can be written as
p ¯ 2 D f r D = 1 r 2 D A 2 sinh ( r D u f ) + B 2 cosh ( r D u f ) + u f r D A 2 cosh ( r D u f ) + B 2 sinh ( r D u f )

2.3.3. Boundary Conditions

The pressure and flux in the wellbore are
C D u ζ ¯ w D S r D ζ ¯ 1 D r D r w D = 1 u ζ ¯ w D = ζ ¯ 1 D S r D ζ ¯ 1 D r D r w D
The pressure and flux in the inner boundary are
ζ ¯ 1 D p ¯ 2 D f r f D = 0 ζ ¯ 1 D r D 1 M 12 p ¯ 2 D f r D r f D = 0
The pressure or flux in the outer boundary is
p ¯ 2 D f r e D = 0 p ¯ 2 D f r D r e D = 0

2.3.4. Solution of BHP

According to the inner boundary condition Equation (27), composite interface condition Equation (28), and outer boundary conditions Equation (29), the coefficients A and B of Equations (22) and (25) are obtained
a 11 a 12 a 21 a 22 a 23 a 24 a 31 a 32 a 34 a 34 a 43 a 44 A 1 B 1 A 2 B 2 = 1 u 0 0 0
where
a 11 = ( 1 + C D S u + C D u ) s i n h u + u 1 + C D S u c o s h u a 12 = ( 1 + C D S u + C D u ) c o s h u + u 1 + C D S u s i n h u a 21 = 1 r f D s i n h r f D u a 22 = 1 r f D c o s h r f D u a 23 = 1 r f D s i n h r f D u f a 24 = 1 r f D c o s h r f D u f a 31 = 1 r f D 2 s i n h r f D u + u r f D 2 c o s h r f D u a 32 = 1 r f D 2 c o s h r f D u + u r f D 2 s i n h r f D u a 33 = 1 M 12 1 r f D 2 s i n h r f D u f + u r f D 2 c o s h r f D u f a 34 = 1 M 12 1 r f D 2 c o s h r f D u f + u r f D 2 s i n h r f D u f a 43 = 1 r e D s i n h r e D u f , a 44 = 1 r e D c o s h r e D u f          o r a 43 = 1 r e D 2 s i n h r e D u f + u r e D 2 c o s h r e D u f a 44 = 1 r e D 2 c o s h r e D u f + u r e D 2 s i n h r e D u f
A1 and B1 of Equation (30) can be calculated through the Crammer law
A 1 = a 22 a 34 a 44 a 43 a 34 a 32 a 23 a 44 a 43 a 24 u Δ B 1 = a 21 a 34 a 44 a 43 a 34 a 31 a 23 a 44 a 43 a 24 u Δ
where Δ is a value calculated by Det(aij).
Bring A1 and B1 into the solution of Equation (22) to obtain the dimensionless inner pressure solution after Perturbation transformation. In the Laplace domain, the dimensionless bottomhole pressure (BHP) solution after Perturbation transformation is
ζ ¯ w D = A 1 sinh ( u ) + B 1 cosh ( u )
To obtain the dimensionless bottomhole pressure (BHP) in the time domain, the numerical inversion was performed using the method proposed by Stehfest [26].
p w D = 1 γ L n 1 γ L 1 ( ζ ¯ w D )

3. Results

3.1. Model Verification

Prior to analyzing the novel flow behaviors, the correctness of the proposed analytical model was verified by degenerating it to established classical cases. The comprehensive model presented in this study can be reduced to simpler, well-validated models under specific parameter constraints. Firstly, by setting the stress-sensitivity coefficient γ = 0, the inner zone model simplifies to a homogeneous, spherical flow model without permeability alteration. Secondly, by setting the inter-porosity flow coefficient to a very large value (λm = 108), the outer dual-porosity zone approximates an equivalent homogeneous system with pseudo-steady-state flow being instantaneous. Figure 2 demonstrates the excellent agreement between the degenerate solution of our model (γ = 0, λm = 108, and M12 = 0) and the classic spherical flow solution for a homogeneous reservoir presented by Chatas [19]. The match across all flow regimes, including the wellbore storage unit-slope line, the transition, and the characteristic −0.5 slope of the spherical flow derivative, is nearly perfect. This confirms the accuracy of our solution methodology for the spherical flow geometry.

3.2. BHP Response and Flow Regimes

In this part, the BHP response curve and the sensitivity of each parameter are analyzed. The dimensionless wellbore storage coefficient CD is 10, the skin factor S is 0.3, and the other parameter values are shown in Table 2.
According to the characteristics of the BHP and its derivative (BHPD) curves, the bottomhole pressure response reflects eight flow regimes (Figure 3). The type curve presented in Figure 2 reveals a complex sequence of flow regimes, which is a direct consequence of the integrated physical processes considered in our novel model. In the following sections, we will not only describe the sensitivity of the pressure response to key parameters but also discuss the underlying physical mechanisms and contrast our findings with what would be predicted by conventional models that omit stress-sensitivity or use simplified flow geometries. This comparative analysis highlights the practical significance and novelty of our work.

3.3. Flow Regimes

As shown in Figure 3, ① is a wellbore storage regime, it is influenced by the wellbore storage coefficient. ② is the transient flow regime, which is controlled by the skin factor. ③ is a spherical flow regime for the inner zone, it is a steady-state flow with −0.5 slope in the BHPD curve. ④ Transitional flow caused by the mobility and storability difference between the inner zone and outer zone. ⑤ is a spherical flow regime for the outer zone, it is a steady-state flow with −0.5 slope in the BHPD curve. ⑥ is the flow regime induced by pseudo-steady-state inter-porosity flow with an obvious V-shape in the BHPD curve. ⑦ In the flow regime dominated by boundary effects, the BHPD curve exhibits a unit slope, a −0.5 slope, or a sharp drop in response to closed, infinite-acting, and constant-pressure boundaries, respectively. ⑧ is the flow regime controlled by the stress-sensitivity of the filled-cave with a slope greater than 1 in the BHPD curve. All flow regimes and curve features can be listed and found in Table 3.

4. Discussion

Taking the closed boundary as an example, the sensitivity of each parameter to the typical curve of BHP response is analyzed according to each flow stage.

4.1. Composite Distance

Denoted as the inner zone, the filled-cave has a composite radius equal to its own radius, defined by the distance to the inner-outer zone interface. It follows that the composite radius increases with the filled-cave radius. Moreover, Figure 4 demonstrates that the radius of the filled-cave governs the timing at which the transitional flow regime (④) emerges. The larger the scope of the filled-cave, the longer the duration of the inner spherical flow (③), and the later the transitional flow regime (④) appears.

4.2. Stress-Sensitivity Factor

Since the inner zone was formed later, the degree of compaction is lower than that of the surrounding rocks. Therefore, the rock in the filled-cave zone has a stress-sensitive phenomenon in the process of pressure reduction, i.e., the porosity and permeability of the inner zone decrease with the depletion of pressure. Here, the stress-sensitivity coefficient (γ) is introduced to represent the coupling between medium deformation and permeability. The magnitude of γ directly reflects the extent of this influence, with a larger value indicating a more significant effect. Figure 5 shows the effect of the stress-sensitivity factor on BHP. Stress-sensitivity affects the entire flow stage. The stress-sensitivity factor increases and the early-middle stage pressure curve moves up as a whole, which indicates that the pressure loss increases under the same production rate, indicating that the reservoir permeability becomes worse. In the later stage, especially in the stage where stress-sensitivity control flow regime ⑧, the pressure upturn occurs earlier, and the degree of the upwarp is intensified, indicating that the influence of the formation deformation on the flow is gradually increasing.
The upward deviation in the late-time pressure derivative, characterized by a slope greater than 1, is a unique signature of stress-sensitivity that cannot be captured by any of the existing models for filled-caves, including Ref. [6]. This has critical implications for well test interpretation: misinterpreting this late-time rise as a closed boundary effect in a homogeneous reservoir would lead to a grossly underestimated drainage volume. Our model provides the first analytical framework to correctly identify this phenomenon as formation damage due to permeability impairment near the wellbore, allowing for a more realistic assessment of well performance and reserves.

4.3. Mobility Ratio

The marked permeability contrast between the inner zone and the outer reservoir results in a mobility ratio M12 > 1, a key parameter affecting the bottomhole pressure (BHP). Figure 6 shows the mobility ratio greatly affects the entire flow stage. The transitional flow regime becomes more distinct as the mobility in the inner zone increases, particularly when compared to cases where the outer zone mobility remains constant (④). When the mobility of the inner and outer regions differs greatly (M12 > 10), the outer spherical flow (⑤) is easily covered up by the transitional flow (④) or even disappears. On the other hand, the large mobility ratio in the inner zone indicates that the physical properties of the filled-caves are excellent (that is, the degree of compaction is extremely low), and the reservoir in the inner area is greatly affected by stress-sensitivity. Therefore, for a filled-cave with a large difference in mobility, such as M12 = 100, the outer zone is equivalent to a closed boundary.
A higher M12 signifies that the filled-cave is a high-permeability “sweet spot” relative to the surrounding fractured rock. The discussion of these findings is two-fold. Firstly, the pronounced transitional flow regime at high M12 values is a direct result of this sharp contrast. It represents the time when the pressure transient encounters the lower-mobility outer zone, acting as a flow barrier. This is a critical period for accurately estimating the cave’s size from the derivative curve. Secondly, and more importantly from an engineering perspective, a high M12 has a direct and adverse coupling with stress-sensitivity. The excellent flow capacity of the inner zone implies that a larger pressure drop is concentrated across a smaller volume near the wellbore, thereby amplifying the stress-sensitive permeability damage. Consequently, for a well with excellent initial productivity (high M12), the productivity decline due to stress-sensitivity can be more severe. This insight, provided by our model, is vital for production forecasting and designing appropriate drawdown management strategies to mitigate formation damage in high-deliverability filled-cave wells.

4.4. Storability Ratio

Since the inner zone possesses greater porosity and compressibility than the outer zone, the storability ratio ω12 leads to a value exceeding 1. The magnitude of ω12 is a critical factor affecting the behavior of the bottomhole pressure (BHP), Figure 7, reveals the larger the storability ratio coefficient, the later the boundary control flow occurs. Compared with the influence of the mobility ratio M12, while the storability ratio has a minimal impact on BHP in the middle flow stage, discernible only through analysis of the BHPD curves, its influence grows progressively more evident during the late flow period. With the increase in the storability ratio, the time when the BHPD curve rises is delayed.

4.5. Diffusivity Ratio

The mobility ratio and the storability ratio reflect the difference between the inner and outer zones from the perspective of fluid flow and reservoir properties, respectively. In the process of pressure transmission, diffusivity η = k/(μφct) can represent the overall difference in flow process. In this part, the diffusivity ratio η12 is the ratio of the diffusivity η1 to the diffusivity η2, that is, η12 = M12/ω12. Figure 8 shows the influence of mobility ratio (storage ratio) on BHP under the same pressure propagation velocity (η12 = 1). It can be seen that under the parameter form of diffusivity ratio, the influence of mobility ratio M12 on BHP has obvious quantitative characteristics.
In the outer spherical flow stage (⑤), firstly, according to the pressure derivative value p’wD(M12) under different M12, and then the characteristic value of the pressure derivative under any M12 is calculated D = p’wD(M12)/p’wD(M12 = 1). The scatter data for D vs. M12, as shown in Figure 9, have a good linear relationship, i.e., DM12. This relationship can be used to calculate the mobility ratio M12 from the BHPD curve, intuitively.

4.6. Inter-Porosity Flow Coefficient

The inter-porosity flow coefficient, which quantifies the difficulty of matrix fluid transfer into fractures, governs the timing of the inter-porosity flow regime (⑥), as illustrated in Figure 10. A larger value of this coefficient consequently leads to an earlier appearance of this flow regime.

4.7. Storability Ratio of Fracture

While the fracture storability ratio represents the fracture storage fraction in the outer zone (a larger value meaning more fracture fluid), Figure 11 reveals that a smaller ratio makes the inter-porosity flow regime (⑥) more evident and the V-shape on the BHPD curve deeper.

4.8. Boundary Distance

As illustrated in Figure 12, the boundary distance determines the onset timing of the boundary-dominated flow regime (⑦). An increase in this distance not only delays the occurrence of regime (⑦) but also diminishes the prominence of the stress-sensitivity controlled flow (⑧). This is because the larger the boundary distance, the more sufficient the reservoir fluid, the smaller the pressure drop under the same production conditions, and the smaller the deformation of the formation caused by the stress-sensitivity of the reservoir.

5. Conclusions

For capturing the cave and fracture dynamic information of a fracture-cave reservoir, a novel PTA analytical model for a well located at the filled-cave, considering the stress-sensitivity of the cave and inter-porosity flow of fracture, is established. According to the BHP response and parameter sensitivity, the following conclusions should be highlighted.
(1)
The composite model can be used to characterize the fractured reservoir with the filled-caves, and its flow follows the composite flow regimes The stress-sensitivity effect of the filled-cave area and the inter-porosity flow phenomenon within the fractured reservoir should be considered. In this model, the corresponding analytical solution can be obtained by using Perturbation transformation.
(2)
There are eight flow regimes for a well drilled into filled-caves in fractured reservoirs. Among them, the spherical flow and boundary flow can be used to identify the size of the filled-caves and the stress-sensitivity, respectively. The spherical flow has an obvious slope of 0.5 on the BHPD curve.
(3)
Affected by the stress-sensitivity of the filled-cave, the BHPD’s slope of the boundary flow will be greater than 1. The greater the stress-sensitivity coefficient, the greater the deviation of the boundary flow. At the same time, other flow stages (inter-porosity flow) will also deviate.

Author Contributions

Conceptualization, W.S.; methodology, G.W.; formal analysis, S.R.; investigation, J.B.; resources, L.T.; writing—original draft preparation, J.C.; visualization, Z.X.; supervision, J.Q.; project administration, Q.Z.; funding acquisition, W.S. All authors have read and agreed to the published version of the manuscript.

Funding

The research was funded by Open Fund (PLN202415) of State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation (Southwest Petroleum University), the Natural Science Research Project of Jiangsu Higher Education Institutions, China (Grants No. 25KJB480001), and the Natural Science Foundation of Jiangsu Province, China (Grants No. BK20250971).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

The original contributions presented in this study are included in the article. Further inquiries can be directed to the corresponding author.

Conflicts of Interest

The authors declare no conflicts of interest.

Abbreviations

The following abbreviations are used in this manuscript:
BHPBottomhole Pressure
BHPDBottomhole Pressure Derivative
PTAPressure Transient Analysis

Appendix A. Derivation of Equation (9): Dimensionless Flow Equation for the Outer Zone

Step 1: Establish the physical equations in the outer zone
The flow in the outer zone is governed by two continuity equations, one for the fracture system and one for the matrix system.
Fracture system flow equation: the fracture system acts as the primary flow path, and its continuity equation includes a source term representing fluid transfer from the matrix.
ρ v 2 f + ρ q m f + ρ ϕ 2 f t = 0
where qmf is the volumetric flow rate from matrix to fractures per unit rock volume.
Matrix system flow equation: the matrix system acts as the primary storage, and its continuity equation describes depletion due to fluid outflow.
ρ q m f + ρ ϕ 2 m t = 0
Step 2: Introduce constitutive relationships and assumptions
Darcy’s law (for flow in fractures)
v 2 f = k 2 f μ p 2 f
Warren–Root pseudo-steady-state inter-porosity flow
q m f = α k 2 m μ ( p 2 m p 2 f )
This definition corrects and clarifies Equation (7), and Fluid and Rock Equations of State (assuming small compressibility) see Equation (2).
Step 3: Derive the pressure diffusion equations
Substituting Darcy’s law and the equations of state into the continuity equations and retaining only first-order terms in pressure (linearization) yields the pressure diffusion equations.
For the fracture system
k 2 f μ ρ p 2 f + ρ α k 2 m μ ( p 2 m p 2 f ) + ρ ϕ 2 f c t 2 f p 2 f t = 0
Using the linearization ∇⋅(ρpf) ≈ ρ2pf, and dividing the entire equation by ρkf/μ, we obtain
2 p 2 f + α k 2 m k 2 f ( p 2 m p 2 f ) = μ ϕ 2 f c t 2 f k 2 f p 2 f t
For the matrix system
ρ α k 2 m μ ( p 2 m p 2 f ) + ρ ϕ 2 m c t 2 m p 2 m t = 0
Dividing by ρ and then multiplying by μ/kf (to maintain consistency with the fracture equation) gives
α k 2 m k 2 f ( p 2 m p 2 f ) = μ ϕ 2 m c t 2 m k 2 m p 2 m t
Step 4: Transform to spherical coordinates and define key parameters
Laplacian in spherical coordinates (spherical symmetry)
2 p 2 f = 1 r 2 r r 2 p 2 f r = 2 p 2 f r 2 + 2 r p 2 f r
This form is substituted into the fracture Equation (A6). Using the definitions from Table 1, we now convert Equations (A6) and (A8) into their dimensionless forms.
Convert the fracture Equation (A6)
2 p 2 D f r D 2 + 2 r D p 2 D f r D + λ m ( p 2 D m p 2 D f ) = ω 12 M 12 ω f p 2 D f t D
Convert the matrix Equation (A8)
λ m ( p 2 D m p 2 D f ) = ω 12 M 12 1 ω f p 2 D m t D
Combining the two derived dimensionless equations yields the exact form of Equation (9).

Appendix B. Derivation of Equation (11): Dimensionless Flux Condition in the Wellbore

Step 1: Establish the physical concept and material balance equation
At the wellbore, the total bottomhole flow rate q consists of two components
q = q s f + q w s
where qsf is the flow rate entering the wellbore from the formation, and qws is the flow rate contributed by the expansion of fluid stored in the wellbore volume.
Step 2: Quantify the wellbore storage flow rate qws
The wellbore storage effect describes the additional flow rate resulting from the compression or expansion of fluid in the wellbore when the well is opened or shut. It is defined by the wellbore storage coefficient C as
C = d V w s d p w
where C is wellbore storage coefficient, m3/Pa; dVws is the change in fluid volume in the wellbore, m3; dpw is the change in bottomhole pressure, Pa.
The flow rate is the derivative of volume with respect to time. Thus, the wellbore storage flow rate is
q w s = d V w s d t = C d p w d t
Step 3: Quantify the sandface inflow qsf and introduce the skin effect
According to Darcy’s law, at the wellbore wall (r = rw), the theoretical inflow velocity without considering skin is
v i d e a l = k μ p r | r = r w
For spherical flow, on a sphere of radius rw, the flow area A = 4πrw2. Therefore
q i d e a l = 4 π r w 2 k 1 μ p 1 r | r = r w
The skin effect S quantifies the additional pressure drop due to damage or improvement in the near-wellbore region. The relationship between the actual flowing bottomhole pressure pw and the theoretical sandface pressure p1,ideal(rw) is
p 1 , i d e a l r w p w = q s f μ B 2 π k 1 h S
However, for spherical flow, this relationship needs adjustment. The steady-state pressure drop formula for spherical flow differs from that for radial flow. Based on derivations found in classical Ref. [19] (Chatas, 1966), the pressure drop relationship considering skin for spherical flow becomes
p 1 , i d e a l r w p w = q s f μ B 2 π k 1 r w S
A more straightforward and widely accepted approach is to define the effective flow rate considering skin. Physically, the skin effect can be viewed as an additional pressure drop across an infinitesimally thin skin zone, proportional to the flow rate. Therefore, the sandface flow rate qsf is equal to the flow rate qideal entering this skin zone from the deeper formation (at r slightly greater than rw). The difference between the bottomhole flowing pressure pw and the formation pressure p1(rw) is determined by the skin factor.
Incorporating stress-sensitivity and the skin effect into Darcy’s law, the inflow rate can be expressed as
q s f = 4 π r w 2 k 1 r w 2 μ p 1 r | r = r w
where k1(rw) is the permeability at the wellbore wall, affected by stress-sensitivity. According to the manuscript’s assumption and Equation (2), k1 = k1i exp[αk(p1pi)]. Therefore
q s f = 4 π r w 2 k 1 i μ e α k ( p 1 p i ) p 1 r | r = r w
based on the dimensionless variables in Table 1 process Equation (5). Note that exp[αk(p1pi)] = exp[−αk(pip1)] = exp(−γp1D) (because αk(pip1) = γp1D).
q s f q B = 4 π r w 2 k 1 i μ e γ p 1 D p 1 r | r = r w
And then, substitute dimensionless pressure (p1D) and dimensionless distance (rD) into the equation above.
In well test analysis for spherical flow, a scaling factor is typically introduced to match the standard definition. A common result is that the dimensionless sandface inflow rate, considering stress-sensitivity, is expressed as:
q s f q = e γ p 1 D r D p 1 D r D | r D = r w D
where rwD = 1. For constant total production rate qq, the total rate is normalized to 1. Therefore, Equation (11) directly gives the dimensionless formation inflow rate relative to the total production rate.
Step 4: Establish the dimensionless material balance equation (deriving Equation (11))
Convert the physical material balance Equation (A12) to dimensionless form and Equation (A12) becomes q = qsf + qws. We already have qsf/q from Equation (A22).
Thus
q w s q = C D p w D t D
Step 5: Combine to form the flow rate condition (Equation (11)
Substitute Equations (A22) and (A23) into the dimensionless material balance Equation (A12).
C D p w D t D e γ p 1 D r D p 1 D r D | r D = r w D = 1
This is the core of Equation (11), where S is implicitly included in the pressure condition. To explicitly introduce the skin factor S, it is incorporated directly into the flow term, resulting in the more general form
C D p w D t D S e γ p 1 D r D p 1 D r D | r D = r w D = 1
Step 6: Derive the pressure condition considering skin (Equation (12)
Based on the physics expressed in Equation (4), there exists a pressure drop (skin pressure drop) between the bottomhole flowing pressure and the formation pressure at the wellbore wall, proportional to the flow rate. In dimensionless form, this skin pressure drop is expressed as
p 1 D r w D p w D = S
This dimensionless flow rate is precisely the sandface inflow rate we derived earlier, considering stress-sensitivity. Therefore
p w D = p 1 D + S e γ p 1 D r D p 1 D r D | r w D

References

  1. Li, Q.; Du, X.; Tang, Q.; Xu, Y.; Li, P.; Lu, D. A novel well test model for fractured vuggy carbonate reservoirs with the vertical bead-on-a-string structure. J. Pet. Sci. Eng. 2021, 196, 107938. [Google Scholar] [CrossRef]
  2. Du, X.; Li, Q.; Li, P.; Xian, Y.; Zheng, Y.; Lu, D. A novel pressure and rate transient analysis model for fracture-caved carbonate reservoirs. J. Pet. Sci. Eng. 2022, 208, 109609. [Google Scholar] [CrossRef]
  3. Popov, P.; Qin, G.; Bi, L.; Efendiev, Y.; Ewing, R.E.; Kang, Z.; Li, J. Multiscale Methods for Modeling Fluid Flow Through Naturally Fractured Carbonate Karst Reservoirs. Presented at the SPE Annual Technical Conference and Exhibition, Anaheim, CA, USA, 11–14 November 2007. [Google Scholar] [CrossRef]
  4. Shi, W.; Cheng, J.; Liu, Y.; Gao, M.; Tao, L.; Bai, J.; Zhu, Q. Pressure transient analysis of horizontal wells in multibranched fault-karst carbonate reservoirs: Model and application in SHB oilfield. J. Pet. Sci. Eng. 2023, 220, 111167. [Google Scholar] [CrossRef]
  5. Popov, P.; Qin, G.; Bi, L.; Efendiev, Y.; Kang, Z.; Li, J.; Ewing, R.E. Multiphysics and multiscale methods for modeling fluid flow through naturally fractured carbonate karst reservoirs. SPE Reserv. Eval. Eng. 2009, 12, 218–231. [Google Scholar] [CrossRef]
  6. Gao, B.; Huang, Z.-Q.; Yao, J.; Lv, X.-R.; Wu, Y.-S. Pressure transient analysis of a well penetrating a filled cavity in naturally fractured carbonate reservoirs. J. Pet. Sci. Eng. 2016, 145, 392–403. [Google Scholar] [CrossRef]
  7. Wan, Y.; Liu, Y.; Ouyang, W.; Han, G.; Liu, W. Numerical investigation of dual-porosity model with transient transfer function based on discrete-fracture model. Appl. Math. Mech. Engl. 2016, 37, 611–626. [Google Scholar] [CrossRef]
  8. Wan, Y.; Liu, Y.; Wu, N. Numerical pressure transient analysis for Unfilled-caved carbonate reservoirs based on Stokes-Darcy coupled Theory. J. Pet. Sci. Eng. 2020, 190, 107085. [Google Scholar] [CrossRef]
  9. Davies, J.P.; Davies, D.K. Stress-Dependent Permeability: Characterization and Modeling. SPE J. 2001, 6, 224–235. [Google Scholar] [CrossRef]
  10. Aghabarari, A.; Ghaedi, M. Evaluation of the effects of homogenizing matrix block sizes on the simulation of naturally fractured reservoirs. J. Pet. Sci. Eng. 2022, 213, 110373. [Google Scholar] [CrossRef]
  11. Du, X.; Zhang, Y.; Zhou, C.; Su, Y.; Li, Q.; Li, P.; Lu, Z.; Xian, Y.; Lu, D. A novel method for determining the binomial deliverability equation of fractured caved carbonate reservoirs. J. Pet. Sci. Eng. 2022, 208, 109496. [Google Scholar] [CrossRef]
  12. Ehlig-Economides, C.A.; Joseph, J. A new test for determination of individual layer properties in a multilayered reservoir. SPE Form. Eval. 1987, 2, 261–283. [Google Scholar] [CrossRef]
  13. Gomes, E.; Ambastha, A.K. An analytical pressure-transient model for multilayered, composite reservoirs with pseudo-steady state formation crossflow. Present at the SPE Western Regional Meeting, Anchorage, AK, USA, 26–28 May 1993. [Google Scholar] [CrossRef]
  14. Onur, M.; Cinar, M. Analysis of Sandface-Temperature-Transient Data for Slightly Compressible, Single-Phase Reservoirs. SPE J. 2017, 22, 1134–1155. [Google Scholar] [CrossRef]
  15. Guo, B.; Stewart, G.; Mario, T. Linearly Supported Radial Flow—A New Flow Regime Identified in Dual-Porosity Reservoirs. Presented at the SPE International Petroleum Conference and Exhibition in Mexico, Villahermosa, Mexico, 1–3 February 2000. [Google Scholar] [CrossRef]
  16. Guo, B.; Stewart, G.; Toro, M. Linearly Supported Radial Flow—A Flow Regime in Layered Reservoirs. SPE Res. Eval. Eng. 2002, 5, 103–110. [Google Scholar] [CrossRef]
  17. Du, X.; Lu, Z.; Li, D.; Xu, Y.; Li, P.; Lu, D. A novel analytical well test model for fractured vuggy carbonate reservoirs considering the coupling between oil flow and wave propagation. J. Pet. Sci. Eng. 2018, 173, 447–461. [Google Scholar] [CrossRef]
  18. Shamu, J.; Zou, L.; Håkansson, U. An Experimental Study of 2D Radial Flow of a Yield Stress Fluid Between Parallel Disks. Presented at the ISRM 9th Nordic Grouting Symposium, Helsinki, Finland, 2–3 September 2019; Available online: https://onepetro.org/ISRMNGS/proceedings-abstract/NGS19/NGS19/ISRM-NGS-2019-02/42047 (accessed on 11 January 2025).
  19. Chatas, A.T. Unsteady Spherical Flow in Petroleum Reservoirs. SPE J. 1966, 6, 102–114. [Google Scholar] [CrossRef]
  20. Joseph, J.A.; Koederitz, L.F. Koederitz. Unsteady-State Spherical Flow with Storage and Skin. SPE J. 1985, 25, 804–822. [Google Scholar] [CrossRef]
  21. Jiang, L.; Chen, L.; Yu, H.; Kristensen, M.; Gisolf, A.; Hadrien, D. Detectable Radius of Investigation for One Flow Period with Bourdet Derivative. SPE J. 2024, 29, 4027–4042. [Google Scholar] [CrossRef]
  22. Gelvez, C.; Carlos, T. Fluid Contamination Transient Analysis. Petrophysics 2024, 65, 32–50. [Google Scholar] [CrossRef]
  23. Warren, J.E.; Root, P.J. The Behavior of Naturally Fractured Reservoirs. SPE J. 1963, 3, 245–255. [Google Scholar] [CrossRef]
  24. Pedrosa, O.J. Pressure transient response in stress-sensitive formations. Presented at the SPE California Regional Meeting, Oakland, CA, USA, 2–4 April 1986. [Google Scholar] [CrossRef]
  25. Kikani, J.; Pedrosa, O.A. Perturbation analysis of stress-sensitive reservoirs (includes associated papers 25281 and 25292). SPE Form. Eval. 1991, 6, 379–386. [Google Scholar] [CrossRef]
  26. Stehfest, H. Numerical inversion of Laplace transforms. Commun. ACM 1970, 13, 47–49. [Google Scholar] [CrossRef]
Figure 1. A physical model of a production well drilled into a filled-cave in the fractured reservoirs. (a) is a vertical sectional view, (b) is an overwhelming view.
Figure 1. A physical model of a production well drilled into a filled-cave in the fractured reservoirs. (a) is a vertical sectional view, (b) is an overwhelming view.
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Figure 2. Comparison between this model and the referenced model (Ref. [19]).
Figure 2. Comparison between this model and the referenced model (Ref. [19]).
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Figure 3. BHP type curve.
Figure 3. BHP type curve.
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Figure 4. BHP sensitivity of composite distance.
Figure 4. BHP sensitivity of composite distance.
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Figure 5. BHP sensitivity of stress-sensitivity factor.
Figure 5. BHP sensitivity of stress-sensitivity factor.
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Figure 6. BHP sensitivity of mobility ratio.
Figure 6. BHP sensitivity of mobility ratio.
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Figure 7. BHP sensitivity of storability ratio.
Figure 7. BHP sensitivity of storability ratio.
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Figure 8. BHP sensitivity of diffusivity ratio.
Figure 8. BHP sensitivity of diffusivity ratio.
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Figure 9. The relationship between D and pressure conductivity.
Figure 9. The relationship between D and pressure conductivity.
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Figure 10. BHP sensitivity of inter-porosity flow coefficient.
Figure 10. BHP sensitivity of inter-porosity flow coefficient.
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Figure 11. BHP sensitivity of storability ration of fracture.
Figure 11. BHP sensitivity of storability ration of fracture.
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Figure 12. The effect of boundary distance on BHP.
Figure 12. The effect of boundary distance on BHP.
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Table 1. Definition of dimensionless parameters.
Table 1. Definition of dimensionless parameters.
ParametersDefinition
Dimensionless distance r D = r r w
Dimensionless distance to inner boundary r f D = r f r w
Dimensionless distance to outer boundary r e D = r e r w
Dimensionless wellbore storage coefficient C D = 0.159 C ϕ 1 c t 1 r w 3
Dimensionless time t D = 3.6 k 1 t ϕ 1 c t 1 μ r w 2
Dimensionless pressure of inner zone p 1 D = k 1 r w p i p 1 1.842 × 10 3 q μ B
Dimensionless pressure of outer zone p 2 D = k 1 r w p i p 2 1.842 × 10 3 q μ B
Mobility ratio of inner zone to outer zone M 12 = k 1 / μ k 2 / μ
Storability ratio of inner zone to outer zone ω 12 = ϕ 1 c t 1 ϕ 2 c t 2
Stress-sensitivity coefficient γ = 1.842 × 10 3 q μ B k 1 r w α k
Storability ratio of fracture ω f = ϕ 2 f c t 2 f ϕ 2 c t 2
Inter-porosity flow coefficient λ m = α r w 2 k 2 m k 2 f
Table 2. Parameter values in the type model.
Table 2. Parameter values in the type model.
Dimensionless Parameters Type Curve PartSensitivity Analysis Part
Composite distance, rfD10.010~100
Stress-sensitivity factor, γ0.10~0.5
Mobility ratio, M122.01~100
Storability ratio, ω121.01~10
Inter-porosity flow coefficient, λm0.5 × 10−5(0.5~10) × 10−5
Storability of fracture, ωf0.010.05~0.9
Distance to outer boundary, reD2 × 103(1~100) × 103
Table 3. Flow regimes and curve feature of the type model.
Table 3. Flow regimes and curve feature of the type model.
Flow StageFlow RegimeHPD Curve Feature p’wD
Early① wellbore storageSlope = 1
② transitional flow
③ inner spherical flow Slope = −1/2
Middle④ transitional flow
⑤ outer spherical flowSlope = −1/2
⑥ inter-porosity flowV-shape
Late⑦ boundary control flowClosed boundary, slope = 1
Infinite-acting boundary, slope = −1/2,
⑧ stress-sensitivity control flowSlope > 1
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Shi, W.; Wang, G.; Rong, S.; Qin, J.; Chen, J.; Tao, L.; Bai, J.; Xu, Z.; Zhu, Q. Pressure Transient Analysis for Vertical Well Drilled in Filled-Cave in Fractured Reservoirs. Fluids 2025, 10, 324. https://doi.org/10.3390/fluids10120324

AMA Style

Shi W, Wang G, Rong S, Qin J, Chen J, Tao L, Bai J, Xu Z, Zhu Q. Pressure Transient Analysis for Vertical Well Drilled in Filled-Cave in Fractured Reservoirs. Fluids. 2025; 10(12):324. https://doi.org/10.3390/fluids10120324

Chicago/Turabian Style

Shi, Wenyang, Gerui Wang, Shaokai Rong, Jiazheng Qin, Juan Chen, Lei Tao, Jiajia Bai, Zhengxiao Xu, and Qingjie Zhu. 2025. "Pressure Transient Analysis for Vertical Well Drilled in Filled-Cave in Fractured Reservoirs" Fluids 10, no. 12: 324. https://doi.org/10.3390/fluids10120324

APA Style

Shi, W., Wang, G., Rong, S., Qin, J., Chen, J., Tao, L., Bai, J., Xu, Z., & Zhu, Q. (2025). Pressure Transient Analysis for Vertical Well Drilled in Filled-Cave in Fractured Reservoirs. Fluids, 10(12), 324. https://doi.org/10.3390/fluids10120324

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