Study on Two-Phase Flow Behavior and Analysis of Influencing Factors Based on Unsteady Oil–Water Relative Permeability Experiment
Abstract
1. Introduction
- (1)
- Stage-resolved and stratigraphically comparable dataset: Early-stage cores and late-stage infill cores were collected from the same reservoir interval and overlapping or stratigraphically correlated layers, and the infill cored intervals were screened as waterflood-affected zones using integrated field evidence (logging-based interpretation and injection–production history), thereby improving representativeness for stage-wise comparisons.
- (2)
- Unified unsteady-state JBN workflow with quantitative descriptors: Unsteady-state tests were processed using a consistent JBN procedure, and key characteristic parameters (e.g, Swir,Sw(Sor), two-phase flow interval, movable-oil saturation, and krw(Sor)) were quantified to enable systematic cross-core comparisons.
- (3)
- Curve-type classification linked to mechanisms: Water-phase curve geometries were classified into concave-up, linear, or concave-down seepage types, and their differences were interpreted within a pore-scale connectivity–heterogeneity framework.
- (4)
- Operational sensitivity analysis with clarified causality: The impacts of pressure gradient and injected pore volume on displacement efficiency were evaluated; additionally, water cut was treated as a flooding-stage indicator rather than a direct microscopic control factor to avoid causal misinterpretation.
- (5)
- Micro-CT used as qualitative structural support: Raw grayscale micro-CT slices (without phase segmentation) were incorporated as qualitative evidence of pore connectivity and preferential flow pathways, supporting the proposed mechanistic interpretations.
2. Experimental Material and Methods
2.1. Experimental Material
- (1)
- Cores were cleaned for 48 h using Soxhlet extraction with a toluene–ethanol mixture (3:1 by volume) to remove residual oil and organic matter.
- (2)
- The cleaned cores were oven-dried at 105 °C until a constant weight was achieved (mass variation < 0.1%).
- (3)
- Porosity was re-measured using a helium porosimeter, with deviations from the original data controlled within 2%.
- (4)
- Cores were placed in a vacuum saturation device, evacuated to −0.1 MPa for 4 h, and then fully saturated with simulated formation water.
2.2. Experimental Principles and Algorithm Procedures
3. Experimental Results and Analysis
3.1. Analysis of Experimental Results for Oil–Water Two-Phase Relative Permeability Curves
3.2. Analysis of Fluid Flow Characteristics and Patterns in Core Samples with Different Permeabilities
4. Controlling Factors of Relative-Permeability Behavior and Displacement Efficiency
4.1. Impact of Permeability on Oil Displacement Efficiency
4.1.1. Pore-Scale Interpretation of Curve-Type Differences and Development-Stage Effects
4.1.2. Quantitative Correlations Between Permeability and Relative-Permeability Characteristic Parameters
4.2. Impact of Pressure Gradient on Oil Displacement Efficiency
4.3. Impact of Injection Multiple on Oil Displacement Efficiency
4.4. Relationship Between Water Cut (As a Flooding-Stage Indicator) and Displacement Efficiency
5. Conclusions
- (1)
- Based on unsteady-state coreflood experiments on Jilin Oilfield sandstones, oil–water relative-permeability curves were classified into three types according to the geometry of the water-phase curve. The convex-upward water-phase curve commonly exhibits a two-stage pattern: at first, increasing water saturation raises water relative permeability while oil relative permeability drops sharply; later, oil relative permeability declines more gradually as water relative permeability increases more steeply. The linear and concave-down types occur less frequently and are mainly associated with reservoir heterogeneity and complex flow behavior during waterflooding.
- (2)
- Analysis of cores from different development stages shows strong linear correlations between permeability and movable oil saturation (R2 = 0.89), as well as between permeability and irreducible water saturation (R2 = 0.84). By contrast, residual oil saturation tends to increase as permeability decreases, but the relationship is relatively weak.
- (3)
- A single-factor analysis was conducted to evaluate the impacts of individual parameters on oil-displacement efficiency. For low-permeability cores, increasing the pressure gradient at the early flooding stage significantly enhances recovery; however, once permeability exceeds 10 mD, the effect of the pressure differential becomes much less pronounced. Increasing the injected water volume generally improves recovery across permeability classes, but the incremental benefit diminishes and eventually approaches a plateau beyond a threshold injection level.
- (4)
- Micro-CT images provide qualitative structural evidence supporting the proposed mechanisms. Nevertheless, quantitative pore–throat statistics and clay-mineral characterization (e.g., SEM and XRD) are not included in the present dataset. Future work will integrate these microstructural and mineralogical measurements to further validate the linkage between microscopic processes (e.g., clay swelling and particle migration) and relative-permeability curve types.
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
- Lei, Z.D.; Li, J.C.; Chen, Z.W.; Dai, X.; Ji, D.Q.; Wang, Y.H.; Liu, Y.S. Characterization of multiphase flow in shale oil reservoirs considering multiscale porous media by high-resolution numerical simulation. SPE J. 2023, 28, 3101–3116. [Google Scholar] [CrossRef]
- Ahmed, E.; Klemetsdal, Ø.; Raynaud, X.; Meyner, O.; Nisen, H.M. Adaptive timestepping, linearization, and a posteriori error control for multiphase flow of immiscible fluids in porous media with wells. SPE J. 2023, 28, 554–574. [Google Scholar] [CrossRef]
- Zhuravljov, A.; Lanetć, Z. Relevance of Analytical Buckley-Leverett Solution for Immiscible Oil Displacement by Various Gases. J. Pet. Explor. Prod. Technol. 2019, 9, 617–626. [Google Scholar] [CrossRef]
- Ghafri, A.Y.A.; Mackay, E.; Stephen, K. The Relevance of the Linear Stability Theory to the Simulation of Unstable Immiscible Viscous-Dominated Displacements in Porous Media. J. Pet. Sci. Eng. 2021, 207, 13. [Google Scholar] [CrossRef]
- Mu, L.Y.; Liao, X.W.; Chen, Z.M.; Zou, J.D.; Chu, H.Y.; Li, R.T. Analytical solution of Buckley-Leverett equation for gas flooding including the effect of miscibility with constant-pressure boundary. Energy Explor. Exploit. 2019, 37, 960–991. [Google Scholar] [CrossRef]
- Khan, M.Y.; Mandal, A. Improvement of Buckley-Leverett equation and its solution for gas displacement with viscous fingering and gravity effects at constant pressure for inclined stratified heterogeneous reservoir. Fuel 2021, 285, 119172. [Google Scholar] [CrossRef]
- Garcia, R.D.O.; Silveira, G.P. Numerical Solutions of the Classical and Modified Buckley-Leverett Equations Applied to Two-Phase Fluid Flow. Open J. Fluid Dyn. 2024, 14, 184–204. [Google Scholar] [CrossRef]
- Spayd, K.; Shearer, M. The Buckley-Leverett equation with dynamic capillary pressure. SIAM J. Appl. Math. 2011, 71, 1088–1108. [Google Scholar] [CrossRef]
- Wang, P.; Tartakovsky, D.M.; Jarman, K.D., Jr.; Tartakovsky, A.M. CDF solutions of Buckley-Leverett equation with uncertain parameters. Multiscale Model. Simul. 2013, 11, 118–133. [Google Scholar] [CrossRef]
- Arabzai, A.; Honma, S. Numerical simulation of the Buckley-Leverett problem. Proc. Sch. Eng. Tokai Univ. 2013, 38, 9–14. Available online: https://www.academia.edu/83063291/Numerical_Simulation_of_the_Buckley_Leverett_Problem (accessed on 15 January 2026).
- Rangel-German, E.R.; Kovscek, A.R. Matrix-fracture shape factors and multiphase-flow properties of fractured porous media. In Proceedings of the SPE 95105-MS Presented at the SPE Latin American and Caribbean Petroleum Engineering Conference, Rio de Janeiro, Brazil, 20–23 June 2005. [Google Scholar] [CrossRef]
- Tian, F.C.; Fu, Y.Q.; Liu, X.W.; Li, D.P.; Jia, Y.P.; Shao, L.F.; Yang, L.L.; Zhao, Y.D.; Zhao, T.; Yin, Q.W. A comprehensive evaluation of shale oil reservoir quality. Processes 2024, 12, 472. [Google Scholar] [CrossRef]
- Cao, J.; Liu, Z.; Zhang, Z.P.; Wang, Y.Z.; Wang, L.L. Analysis of Waterflooding Oil Recovery Efficiency and Influencing Factors in the Tight Oil Reservoirs of Jilin Oilfield. Processes 2025, 13, 1490. [Google Scholar] [CrossRef]
- Liu, B.L.; Yu, H.M.; Wang, Y.Q.; Yu, Z.; Zhao, L.F. A Study on Characteristics of Oil-Water Relative Permeability Curves and Seepage Mechanisms in Low-Permeability Reservoirs. Processes 2025, 13, 3460. [Google Scholar] [CrossRef]
- Wu, J.T.; Zhang, L.; Liu, Y.X.; Ma, K.Q.; Luo, X.B. Effect of Displacement Pressure Gradient on Oil-Water Relative Permeability: Experiment, Correction Method, and Numerical Simulation. Processes 2024, 12, 330. [Google Scholar] [CrossRef]
- Deng, S.; Lin, Z. A Method for Calculating Oil Saturation in Unsteady-State Experiments of High-Permeability Reservoirs. Pet. Geol. Oilfield Dev. Daqing 2020, 39, 50–55. Available online: https://link.cnki.net/doi/10.19597/J.ISSN.1000-3754.201812037 (accessed on 15 January 2026).
- Wang, D.Q.; Yin, D.Y. Study on Empirical Formula of Relative Permeability Curve in Water-Drive Reservoirs. Lithol. Reserv. 2017, 29, 159–164. [Google Scholar] [CrossRef]
- Ma, Y.L.; Zhao, S.J.; Zhang, Z.H.; Wang, L.L.; Si, Y.P. Calculation Method of Relative Permeability Curve for Low-Permeability and Low-Viscosity Reservoirs—T-Type Water Drive Characteristic Curve Method. Pet. Eval. Dev. 2012, 2, 28–31. [Google Scholar] [CrossRef]
- Jiang, R.Z.; Qiao, X.; Chen, W.C.; Xu, J.C.; Sun, Z.B.; Xie, L.S. The Influence of Reservoir Property Time Variation on Reservoir Waterflooding Development. Fault-Block Oil Gas Field 2016, 23, 768–771. Available online: https://xueshu.baidu.com/usercenter/paper/show?paperid=a9974d06345f1fa424f2b52398e3d8e8 (accessed on 15 January 2026).
- Zhang, X.X.; Du, L.; Bai, L.; Hu, W. A New Method for Optimizing and Correcting Oil-Water Relative Permeability Curves by Unsteady-State Method. Fault-Block Oil Gas Field 2016, 23, 185–188. Available online: https://qikan.cqvip.com/Qikan/Article/Detail?id=668432124 (accessed on 15 January 2026).
- Peng, C.Z.; Xue, X.N.; Wang, F.L.; Shi, J.P. Experimental Data Processing Method for Oil-Water Relative Permeability by Unsteady-State Method. Pet. Geol. Oilfield Dev. Daqing 2018, 37, 74–78. [Google Scholar] [CrossRef]
- Zhao, G.Z.; Dong, D.P.; Xiao, L.C. Two-Phase Low-Velocity Non-Darcy Flow Model and Relative Permeability Curve Acquisition Method. Pet. Geol. Recovery Effic. 2022, 29, 69–76. [Google Scholar] [CrossRef]
- Xu, S.J.; Wang, C.Q.; Cao, S.J. Improvement of Calculation Method for Gas-Water Relative Permeability in Tight Sandstone Gas Reservoirs. J. Xi’an Shiyou Univ. Nat. Sci. Ed. 2023, 38, 75–80. [Google Scholar] [CrossRef]
- He, Y. Experimental Research on the Characteristics of Relative Permeability Curves of Fractured Carbonate Oil Reservoirs. Ph.D. Thesis, China University of Geosciences (Beijing), Beijing, China, 2017. [Google Scholar]












| Well Number | Layer Number | Sample Number | Depth (m) | Length (cm) | Diameter (cm) | φ (%) | Ka (mD) | Remarks | |
|---|---|---|---|---|---|---|---|---|---|
| Early Development | JIjian2 | 8 | S1 | 1183.30 | 5.751 | 2.523 | 14.56 | 1.653 | |
| JIjian2 | 13 + 14 | S1-2 | 1325.10 | 6.930 | 2.523 | 13.57 | 2.235 | ||
| JIjian1 | 16 | S2 | 1240.20 | 7.762 | 2.523 | 9.58 | 4.623 | ||
| JIjian1 | 16 | S2-3 | 1260.80 | 7.543 | 2.523 | 10.47 | 5.632 | ||
| JI6-4 | 8 | S3 | 1221.35 | 5.654 | 2.561 | 15.48 | 9.387 | ||
| JI7-18 | 17 | S4 | 1283.04 | 5.713 | 2.542 | 15.32 | 11.456 | ||
| JI4-7 | 26 | S5 | 1243.82 | 5.263 | 2.523 | 14.83 | 17.069 | ||
| JI7-18 | 8 | S4-1 | 1256.39 | 6.965 | 2.590 | 16.53 | 26.956 | ||
| JIjian3 | 8 | S6 | 1221.52 | 4.826 | 2.546 | 18.62 | 31.986 | ||
| JIjian3 | 8 | S6-1 | 1239.76 | 5.361 | 2.572 | 17.57 | 48.561 | ||
| JIjian3 | 8 | S6-2 | 1209.57 | 5.430 | 2.554 | 22.39 | 49.642 |
| Well Number | Layer Number | Sample Number | Depth (m) | Length (cm) | Diameter (cm) | φ (%) | Ka (mD) | Remarks | |
|---|---|---|---|---|---|---|---|---|---|
| Late–stage infill | JI+2-014 | 5 + 6 | S7 | 1206.29 | 8.259 | 2.610 | 10.97 | 2.061 | A |
| JI1-12.1 | 14 | S8 | 1246.46 | 5.230 | 2.610 | 11.20 | 3.126 | ||
| JI+2-014 | 5 + 6 | S7-1 | 1203.40 | 4.830 | 2.610 | 11.05 | 8.621 | ||
| JI+2-014 | 5 + 6 | S7-2 | 1206.68 | 8.312 | 2.610 | 13.66 | 9.662 | A | |
| JI+28-015 | 19 | S9 | 1310.71 | 4.723 | 2.613 | 15.70 | 12.891 | ||
| JI+2-014 | 8 | S7-3 | 1224.92 | 4.671 | 2.614 | 15.73 | 13.331 | A | |
| JI+2-014 | 6 | S7-4 | 1229.35 | 7.312 | 2.610 | 16.68 | 21.561 | A | |
| JI1-12.1 | 13 | S8-1 | 1240.63 | 7.620 | 2.610 | 17.82 | 30.568 | ||
| JI+28-015 | 26 | S9-1 | 1251.31 | 6.263 | 2.610 | 18.24 | 35.663 | ||
| JI+2-014 | 8 | S7-5 | 1227.64 | 7.994 | 2.623 | 15.51 | 37.753 | A | |
| JI1-12.1 | 13 | S8-2 | 1238.07 | 6.784 | 2.620 | 19.21 | 35.93 |
| Device | Function | Range | Accuracy/Resolution |
|---|---|---|---|
| Injection pump | Constant rate | 0.01–10 mL/min | ±0.5% FS |
| Confining-pressure pump | Apply confining pressure | 0–25 MPa | ±0.25% FS |
| Differential pressure transducer | Measure ΔP across core | 0–2 MPa | ±0.25% FS |
| Electronic balance | Measure produced fluid mass | 0–2 kg | 0.01 g |
| Temperature controller | Maintain 22 °C | 0–60 °C | ±0.1 °C |
| Fluid | Density (g/cm3) | Viscosity (mPa·s) | Note |
|---|---|---|---|
| Refined white oil | 0.83 | 15.6 | 22 °C |
| Neutral kerosene | 0.8 | 1.2 | 22 °C |
| Mixed oil (white oil:kerosene = 3:1, v/v) | 0.82 | 13.0 | 22 °C |
| Synthetic formation water (4700 mg/L) | 1.00–1.01 | ~1.0 | 22 °C |
| Well Number | Layer Number | Sample Number | Ka (mD) | Swir (%) | Sw (Sor) (%) | Sc (%) | Sw (%) | Krw (Sor) | η (%) |
|---|---|---|---|---|---|---|---|---|---|
| JIjian2 | 8 | S1 | 1.653 | 54.39 | 77.57 | 28.03 | 69.99 | 0.1156 | 48.36 |
| JIjian2 | 13+14 | S1-2 | 2.235 | 53.45 | 75.56 | 22.26 | 65.62 | 0.1263 | 56.16 |
| JIjian1 | 16 | S2 | 4.623 | 50.36 | 76.23 | 28.82 | 68.06 | 0.1065 | 56.33 |
| JIjian1 | 16 | S2-3 | 5.632 | 48.16 | 78.49 | 25.55 | 70.51 | 0.1364 | 54.89 |
| JI6-4 | 8 | S3 | 9.387 | 48.69 | 79.42 | 32.09 | 73.04 | 0.1162 | 66.21 |
| JI7-18 | 17 | S4 | 11.456 | 46.23 | 77.61 | 29.61 | 67.46 | 0.1492 | 56.36 |
| JI4-7 | 26 | S5 | 17.069 | 48.03 | 76.42 | 31.72 | 69.38 | 0.1463 | 61.03 |
| JI7-18 | 8 | S4-1 | 26.956 | 44.86 | 75.30 | 27.59 | 58.63 | 0.1311 | 53.59 |
| JIjian3 | 8 | S6 | 31.986 | 43.45 | 81.87 | 40.45 | 73.57 | 0.1203 | 67.25 |
| JIjian3 | 8 | S6-1 | 48.561 | 43.54 | 76.57 | 34.71 | 65.51 | 0.1942 | 63.71 |
| JIjian3 | 8 | S6-2 | 49.642 | 40.84 | 78.31 | 38.92 | 66.06 | 0.1340 | 64.35 |
| mean value | 19.02 | 47.45 | 77.58 | 30.89 | 67.98 | 0.1341 | 58.93 | ||
| Well Number | Layer Number | Sample Number | Ka (mD) | Swir (%) | Sw (Sor) (%) | Sc (%) | Sw (%) | Krw (Sor) | η (%) |
|---|---|---|---|---|---|---|---|---|---|
| JI+2-014 | 5+6 | S7 | 2.061 | 50.85 | 77.43 | 26.50 | 63.14 | 0.1566 | 55.43 |
| JI1-12.1 | 14 | S8 | 3.126 | 50.26 | 67.51 | 16.20 | 59.021 | 0.1512 | 48.94 |
| JI+2-014 | 5+6 | S7-1 | 8.621 | 50.17 | 71.89 | 20.48 | 64.50 | 0.1152 | 54.55 |
| JI+2-014 | 5+6 | S7-2 | 9.662 | 49.03 | 81.22 | 30.97 | 70.98 | 0.1369 | 62.85 |
| JI+28-015 | 19 | S9 | 12.891 | 47.88 | 77.46 | 30.37 | 68.58 | 0.1077 | 59.77 |
| JI+2-014 | 8 | S7-3 | 13.331 | 46.98 | 76.96 | 30.61 | 71.96 | 0.1225 | 58.31 |
| JI+2-014 | 6 | S7-4 | 21.561 | 41.86 | 74.71 | 32.36 | 66.20 | 0.1173 | 63.21 |
| JI1-12.1 | 13 | S8-1 | 30.568 | 44.84 | 72.38 | 31.53 | 70.06 | 0.1603 | 61.92 |
| JI+28-015 | 26 | S9-1 | 35.663 | 41.74 | 72.56 | 31.42 | 61.56 | 0.1803 | 57.69 |
| JI+2-014 | 8 | S7-5 | 37.753 | 46.62 | 79.87 | 38.56 | 70.32 | 0.1836 | 68.66 |
| JI1-12.1 | 13 | S8-2 | 35.93 | 43.68 | 76.42 | 33.02 | 67.31 | 0.1489 | 64.13 |
| mean value | 19.18 | 46.72 | 75.31 | 29.27 | 66.69 | 0.1436 | 59.59 | ||
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content. |
© 2026 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license.
Share and Cite
Dong, L.; Dong, D.; Lou, W.; Cao, J. Study on Two-Phase Flow Behavior and Analysis of Influencing Factors Based on Unsteady Oil–Water Relative Permeability Experiment. Processes 2026, 14, 346. https://doi.org/10.3390/pr14020346
Dong L, Dong D, Lou W, Cao J. Study on Two-Phase Flow Behavior and Analysis of Influencing Factors Based on Unsteady Oil–Water Relative Permeability Experiment. Processes. 2026; 14(2):346. https://doi.org/10.3390/pr14020346
Chicago/Turabian StyleDong, Liqiang, Depeng Dong, Wenqiang Lou, and Jie Cao. 2026. "Study on Two-Phase Flow Behavior and Analysis of Influencing Factors Based on Unsteady Oil–Water Relative Permeability Experiment" Processes 14, no. 2: 346. https://doi.org/10.3390/pr14020346
APA StyleDong, L., Dong, D., Lou, W., & Cao, J. (2026). Study on Two-Phase Flow Behavior and Analysis of Influencing Factors Based on Unsteady Oil–Water Relative Permeability Experiment. Processes, 14(2), 346. https://doi.org/10.3390/pr14020346

