The Efficacy and Superiority of the Expert Systems in Reservoir Engineering Decision Making Processes
Abstract
:1. Introduction
2. Decision-Making and Decision Quality
3. Significance of Data-Driven Decisions
4. Decision Making in Reservoir Engineering While Facing Uncertainties
- q(t): Production/injection rate at point x, y, z at time t
- p(t): Pressure at point x, y, z at time t
- Ω(D, R): Mathematical flow model with the relevant “built in” physics and thermodynamics
- D: Flow domain characteristics (e.g., fluid types, spatial and directional dependencies)
- R: Some predefined production/injection mechanism, and/or recovery process including the project design parameters (e.g., well geometry).
5. A Hybrid Computational Platform
- Rectangular and radial-cylindrical grid systems: Both rectangular and radial-cylindrical grid systems are incorporated and supported in these models so that they become adaptable to problems for a set of varying physical boundaries and boundary conditions.
- Black oil model: Black oil model with single, two, and three phase fluid flow conditions and variable bubble point formulation.
- Compositional model: This model is used to represent the multi-phase compositional fluid flow with advanced flash calculation techniques (VLE and VLLE computations).
- Shale gas/Coalbed Methane (CBM) model: A dual-porosity compositional shale gas/CBM model is developed as part of this module.
- EOR process models: These models include thermal EOR models, chemical EOR models, and miscible gas injection models.
6. Examples
6.1. Example 1—Design of Cyclic Steam Stimulation Process
6.2. Example 2—Characterization of a Fault Plane from PTA Data
- Single-well producing at a constant flow rate,
- Infinitely large reservoir,
- Single-phase, slightly compressible fluid,
- Homogeneous formation thickness, porosity, and anisotropic permeability distributions,
- Fully or partially sealing fault plane (expressed in percentage),
- Infinitely long fault plane with no width.
6.3. Example 3—Integration of Seismic, Well-Log and Production Data to Design an Infill Drilling Program
7. Taking One Step Further down the Road on the Hybrid Computational Platform
8. Concluding Remarks
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Appendix A
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- Zhang, Yi.: “An Optimization Protocol Applicable to Pattern-Based Field Development Studies”, M.S. Thesis, the Pennsylvania State University (08/2015).
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- Ketineni, S.: “Structuring an Integrative Approach for Field Development Planning Using Artificial Intelligence and its Application to Tombua Landana Asset in Angola”, Ph.D. Thesis, The Pennsylvania State University (12/2015).
- Hamam, H.: “Continuous CO2 Injection Design in Naturally Fractured Reservoirs Using Neural Network Based Proxy Models”, Ph.D. Thesis, The Pennsylvania State University (08/2016).
- Lai, I.: “Development of an Artificial Neural Network Model for Designing Waterflooding Projects in Three-Phase Reservoirs”, M.S. Thesis, The Pennsylvania State University (08/2016).
- Alquisom, M.: “Development of an Artificial Neural Network Based Expert System to Determine the Location of Horizontal Well in a Three-Phase Reservoir with Simultaneous Gas Cap and Bottom Water Drive”, M.S. Thesis, The Pennsylvania State University (08/2016).
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Short Biography of Author
Data Categories | Reservoir Engineering Components | |
---|---|---|
Reservoir characteristics (intrinsic) | Geophysical data | Seismic surveys Well Logs |
Petrophysical data | Permeability distribution Porosity distribution | |
Net pay thickness | ||
Formation depth | ||
Reservoir pressure | ||
Reservoir temperature | ||
Fluid contact | ||
Fluid properties | Fluid composition | |
PVT data | ||
Rock/fluid interaction characteristics | Relative permeability data | |
Capillary pressure data | ||
Project design parameters (extrinsic) | Field development data | Well specifications, Well architecture |
Well pattern, Well spacing | ||
Process (EOR) project design parameters | ||
Field response functions | Well data | Rate (production/injection), pressure data |
Project economics |
(A) Reservoir Variables Placed on the Input Layer | |||
Variable | Minimum Value | Maximum Value | Units |
Fluid viscosity | 1 | 50 | cp |
Fluid compressibility | 0.000001 | 0.0001 | psi−1 |
Initial reservoir pressure | 500 | 8000 | psi |
Flow rate | 20 | 2000 | STB/D |
Net pay thickness | 10 | 200 | ft |
(B) Reservoir Variables Placed on the Output Layer | |||
Variable | Minimum Value | Maximum Value | Units |
Permeability (kx and ky) | 2 | 1300 | md |
Porosity | 10% | 50% | - |
Distance to the fault plane | 98 | 1060 | ft |
Fault leaking capacity | 0% | 38% | - |
Fault orientation w.r.t principal flow directions | 10 | 90 | degrees |
Data Set | Number of Wells |
---|---|
GAMMA RAY | 18 |
INDUCTION RESISTIVITY | 35 |
INDUCTION CONDUCTIVITY | 29 |
SHORT NORMAL RESISTIVITY | 24 |
SPONTANEOUS POTENTIAL | 27 |
HISTORICAL PRODUCTION | 25 |
Category | Inputs | Units | Minimum | Maximum |
---|---|---|---|---|
Well Parameters | Wellhead pressure | psia | 100 | 2000 |
Tubing diameter | inches | 1 | 4 | |
Pipe roughness | ft | 1.00 × 10−4 | 2.00 × 10−3 | |
Total depth | ft | 200 | 16,000 | |
Fractional depth | fraction | 0 | 1 | |
Temperature at depth | °F | 60 | 340 | |
Wellhead temperature | °F | 60 | 180 | |
Temperature gradient | °F/ft | 0.005 | 0.02 | |
Reservoir Fluid Properties | Molar feed into well | lb-moles/s | 0.00125 | 0.5 |
Initial water mole fraction | fraction | 0 | 1 | |
Water cut | percentage | 0 | 98.7 | |
Oil viscosity | lb-moles/ft-s | 1.7 × 10−5 | 1.5 × 10−3 | |
Gas viscosity | lb-moles/ft-s | 3.4 × 10−6 | 9.9 × 10−5 | |
Water viscosity | lb-moles/ft-s | 4.7 × 10−4 | 8.1 × 10−4 | |
Oil specific gravity | fraction | 0.49 | 0.94 | |
Gas specific gravity | fraction | 0.47 | 0.93 | |
Water specific gravity | fraction | 1 | 1.05 | |
Oil flow rate | STB/D | 10 | 32,767 | |
Gas flow rate | MMSCF/D | 0 | 15.6 | |
Water flow rate | STB/D | 0 | 2180 | |
Gas-oil ratio | SCF/STB | 0 | 168,068 | |
Gas-liquid ratio | SCF/STB | 0 | 94,868 | |
Composition of Feed | Mole fraction of C1 | fraction | 0.20 | 0.94 |
Mole fraction of C2 | fraction | 2.4 × 10−5 | 0.59 | |
Mole fraction of C3 | fraction | 1.9 × 10−6 | 0.56 | |
Mole fraction of C4 | fraction | 9.3 × 10−6 | 0.65 | |
Mole fraction of C5 | fraction | 6.5 × 10−7 | 0.54 | |
Mole fraction of C6+ | fraction | 2.9 × 10−6 | 0.62 | |
Mole fraction of C20+ | fraction | 1.7 × 10−5 | 0.63 | |
Thermodynamic Properties of C6+ and C20+ | Critical temperature of C6+ | °R | 914 | 1409 |
Critical temperature of C20+ | °R | 1428 | 1724 | |
Critical pressure of C6+ | psia | 211 | 477 | |
Critical pressure of C20+ | psia | 105 | 203 | |
Accentricity factor of C6+ | unitless | 0.28 | 0.82 | |
Accentricity factor of C20+ | unitless | 0.86 | 1.33 | |
Molecular weight of C6+ | lb/lb-moles | 86 | 275 | |
Molecular weight of C20+ | lb/lb-moles | 291 | 539 | |
Volume shift parameter of C6+ | unitless | −0.059 | 0.142 | |
Volume shift parameter of C20+ | unitless | 0.139 | 0.358 | |
Critical volume of C6+ | cubic ft/lb-mole | 5.5 | 16.5 | |
Critical volume of C20+ | cubic ft/lb-mole | 17.2 | 31.3 | |
Parachor of C6+ | unitless | 250.1 | 710.5 | |
Parachor of C20+ | unitless | 742.2 | 1090.4 |
Depth (ft) | Pressure (psig) | Relative Deviation (%) | Pressure (psig) | Relative Deviation (%) | |||||
---|---|---|---|---|---|---|---|---|---|
ANN | Numerical | Field Data | Field Data vs. ANN | Field data vs. Numerical | Hasan and Kabir (1992) [12] | Ansari et al. (1994) [13] | Field data vs. Hasan and Kabir (1992) [12] | Field data vs. Ansari et al. (1994) [13] | |
0 | 505 | 505 | 505 | 0.0 | 0.0 | 505 | 505 | 0.0 | 0.0 |
400 | 582 | 595 | 587 | 0.9 | 1.3 | 593 | 586 | 1.0 | 0.2 |
650 | 634 | 655 | 647 | 2.0 | 1.2 | 654 | 641 | 1.1 | 0.9 |
1150 | 753 | 781 | 777 | 3.1 | 0.5 | 781 | 758 | 0.5 | 2.4 |
1650 | 889 | 917 | 920 | 3.4 | 0.3 | 918 | 885 | 0.2 | 3.8 |
2150 | 1042 | 1062 | 1074 | 3.0 | 1.1 | 1063 | 1021 | 1.0 | 4.9 |
2650 | 1208 | 1215 | 1237 | 2.4 | 1.8 | 1212 | 1165 | 2.0 | 5.8 |
3150 | 1384 | 1373 | 1407 | 1.6 | 2.4 | 1369 | 1316 | 2.7 | 6.5 |
3650 | 1568 | 1537 | 1582 | 0.9 | 2.8 | 1530 | 1473 | 3.3 | 6.9 |
4150 | 1756 | 1706 | 1850 | 5.1 | 7.8 | 1695 | 1634 | 8.4 | 11.7 |
4650 | 1945 | 1878 | 1960 | 0.8 | 4.2 | 1864 | 1799 | 4.9 | 8.2 |
5151 | 2135 | 2052 | 2105 | 1.4 | 2.5 | 2034 | 1968 | 3.4 | 6.5 |
Average | 2.2 | 2.4 | Average | 2.6 | 5.3 |
Computational Time Per Day of Simulation (s) | ||||
---|---|---|---|---|
Gas lift Injection rate (MSCFD) | Well Abandonment Time (days) | Full Numerical- Model 1 | Numerical-ANN Coupled Model 2 | Full ANN-Based Model 3 |
100 | 427.29 | 381.9 | 2.8 | 1.98 × 10−4 |
500 | 497.29 | 501.0 | 2.7 | 1.98 × 10−4 |
1000 | 547.29 | 469.8 | 2.4 | 1.98 × 10−4 |
1500 | 527.29 | 476.5 | 2.9 | 1.98 × 10−4 |
1700 | 527.29 | 484.9 | 2.9 | 1.98 × 10−4 |
2000 | 517.29 | 469.9 | 2.9 | 1.98 × 10−4 |
2500 | 517.29 | 441.1 | 2.8 | 1.98 × 10−4 |
2800 | 537.29 | 413.3 | 2.8 | 1.98 × 10−4 |
3000 | 527.29 | 465.8 | 3 | 1.98 × 10−4 |
Average | 456.0 | 2.8 | 1.98 × 10−4 |
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Ertekin, T. The Efficacy and Superiority of the Expert Systems in Reservoir Engineering Decision Making Processes. Appl. Sci. 2021, 11, 6347. https://doi.org/10.3390/app11146347
Ertekin T. The Efficacy and Superiority of the Expert Systems in Reservoir Engineering Decision Making Processes. Applied Sciences. 2021; 11(14):6347. https://doi.org/10.3390/app11146347
Chicago/Turabian StyleErtekin, Turgay. 2021. "The Efficacy and Superiority of the Expert Systems in Reservoir Engineering Decision Making Processes" Applied Sciences 11, no. 14: 6347. https://doi.org/10.3390/app11146347
APA StyleErtekin, T. (2021). The Efficacy and Superiority of the Expert Systems in Reservoir Engineering Decision Making Processes. Applied Sciences, 11(14), 6347. https://doi.org/10.3390/app11146347