Research Article | | Peer-Reviewed

A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta

Received: 1 July 2026     Accepted: 27 July 2026     Published: 20 August 2026
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Abstract

Majority of matured and abandoned wells in depleted oil reservoirs in the Niger Delta are becoming economically unviable. Recently, application of geothermal well system has gained acceptance in the re-use of wells in depleted oil reservoirs. Unfortunately, there are limited studies in the conversion of matured and abandoned wells into geothermal well system in the Niger Delta. Therefore, this study evaluates the techno-economic feasibility of applying geothermal well systems (GWS) in wells in depleted oil reservoirs in the Niger Delta. In this study, characterization and screening of the gathered data from wells in depleted oil reservoirs were performed for GWS application, considering a reservoir temperature above 80°C (176°F) and a water cut of more than 85%. The screened well data were modelled using petroleum production software, PROSPER™, to evaluate their performances and estimate geothermal gradients. A model was developed from a simple regression technique in Microsoft Excel software to predict fluid flowing temperature gradient, using the simulated geothermal data. From the result, the temperature gradient varies by 0.011°F/ft. Estimation of overall heat recovery was then calculated with a simplified heat model, considering an open loop vertical coaxial single geothermal well system. The estimated overall heat recovery ranged from 0.1 MW to 8 MW, for the wells under study. Sensitivity analyses were also conducted to assess the impact of various operating parameters on the overall heat recovery. Finally, economic analyses were performed to evaluate the economic viability of converting matured and abandoned oil wells into geothermal well systems; the simplified economic analyses, considering net present value (NPV), showed geothermal well system with heat capacity above 5 MW to be economically viable. The study demonstrates that wells in depleted oil reservoirs in the Niger Delta can be effectively repurposed for geothermal electricity generation.

Published in International Journal of Oil, Gas and Coal Engineering (Volume 14, Issue 4)
DOI 10.11648/j.ogce.20261404.13
Page(s) 88-107
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2026. Published by Science Publishing Group

Keywords

Geothermal Well Systems, Abandoned Wells, Niger Delta, Re-use of Oil Wells, Heat Recovery from Oil Wells

1. Introduction
The global imperative to reduce dependence on fossil fuels has galvanized stakeholders to pursue innovative strategies for sustainable energy systems, with particular emphasis on decarbonizing heating and cooling in the built environment . Geothermal energy also referred to as ground source energy has emerged as a technically robust and environmentally advantageous solution, offering consistent, low-carbon heating and cooling by exploiting the Earth's stable subsurface temperatures. Compared to conventional air source heat pumps, ground source heat pump (GSHP) systems exhibit superior efficiency and reliability due to their reliance on the relatively invariant thermal properties of the ground .
In the category known as hot sedimentary aquifer (HSA), the heat source is the normal geothermal gradient or possibly a local decaying radiogenic granite heating the aquifers in permeable rocks, for example, commonly from Mesozoic carbonates to Plio-Pleistocene fluvial sediments. HSA are mostly in subsided basins (for example, North of Alpes, Hungary, and Utah in the USA, Paris and Aquitaine Basins in France, Australia, and China). Medium temperature (MT) reservoir temperatures range from 100°C to 190°C, and they can be hosted in volcanic and sedimentary formations . MT fields are relatively widespread at both the plate boundaries and intra-plates such as in California and Utah, South America, Philippines, Azores, New Zealand, Kenya, Hawai, Europe (Croatia), and Central East China . High temperature (HT) resources are the most sought-after as their reservoir temperature is 190°C to 374°C, and they are high enthalpy. These convective systems are generally found down to 3 km, and occasionally > 3.5 km depth. HT resources are mostly in young porous volcanic rocks at active plate boundaries (e.g., Iceland, Indonesia, East Africa, Turkey, and New Zealand), and occasionally in intraplate context above a hotspot such as Yellowstone in the USA .
There is a growing body of research focusing on the repurposing of abandoned and depleted oil and gas wells for geothermal exploitation . Traditionally, the high capital expenditure associated with drilling and completion has been a limiting factor in geothermal project economics. However, the strategic reutilization of existing well infrastructure significantly mitigates upfront costs by obviating the need for new drilling and surface facility installation . Furthermore, leveraging hydrocarbon wells for geothermal applications aligns with the principles of circular economy and infrastructure optimization.
As global oil markets face volatility and declining production in mature fields, petroleum operators are increasingly investigating alternative revenue streams including geothermal co-production and field conversion to optimize asset value and extend field life cycles. This paradigm shift is supported by emerging research on integrated reservoir management that combines hydrocarbon extraction with sustainable geothermal development .
Li and Zhang were among the first to systematically propose the conversion of abandoned oil reservoirs for geothermal power production, introducing technical models for heat extraction and power conversion. A notable milestone was achieved when Wang et al. documented the commissioning of a geothermal power plant utilizing oil wells with formation temperatures of approximately 99°C. For such low- to medium-enthalpy geothermal resources, power generation is typically accomplished through Organic Rankine Cycle (ORC) technology and, in some cases, thermoelectric modules, both of which are optimized for efficient energy conversion at moderate temperature gradients .
Extensive global studies corroborate the technical and economic viability of harnessing waste heat from oil and gas fields. For example, McKenna et al. estimated that coproduced fluids from Gulf Coast oilfields could generate over 1 GW of electrical power. Similarly, Bennett and Horne demonstrated that Los Angeles oilfields possess a net electrical production potential exceeding 7.4 MW. In the context of China, Wang et al. reported a recoverable geothermal resource on the order of 4.24 million joules from oilfield operations. These findings are complemented by a global survey of oilfield geothermal reuse, including Austria’s long-standing use of abandoned well water for spa heating since the 1970s and greenhouse heating applications in Albania, as well as industrial and district heating projects in China and Hungary . The feasibility and scale of geothermal utilization are fundamentally governed by the thermal regime (temperature, pressure, flow rate) of the reservoir, which is a function of local geothermal gradient, well depth, and petrophysical characteristics such as permeability . This underscores the necessity of site-specific screening to optimize geothermal resource development.
Wen-Long et al. investigated the problem of geothermal power generation from abandoned oil wells in Texas. It develops a mathematical model accounting for masses, energy, and momentum conservation equations for fluid flows in the well. Isobutane is chosen as a working fluid. One more approach is described by Davis and Michaelides . The authors suggested using water as a well fluid. The wellbore is used as a heat exchanger which enables the generation of electricity through the binary cycle unit.
Wen-Long et al. researched on the evaluation of working fluids for geothermal power generation from abandoned oil wells. The authors suggested using freon as a working fluid. Modern binary turbines allow for using low-grade heat of the medium. These technologies are used by RASER operating in Alaska. The design of wells is described by Mukhametshin . Depending on the formation structure, various well construction designs are developed.
Wight and Bennett propose a numerical model of energy production from abandoned oil wells in Iran. The mathematical model accounts for the geometrical parameters of the casing wells and exact temperature gradients. The simulation results were optimized for the flow rate of the input and output fluid and temperatures. The use of the Rankine organic cycle in abandoned wells shows the efficiency of the studies . The authors analyze different liquids for different temperature gradients. Well, depths and their temperature gradients are classified. Based on this classification, working fluids were selected.
Wei and Guo advanced the evaluation of geothermal potential in abandoned oil and gas wells by developing a robust mathematical model that simulates heat transfer dynamics from geothermal zones to surface wellheads. Their model incorporates variables such as pipe and wellbore insulation, fluid flow characteristics, and reservoir temperature distributions. Results demonstrate that adequate insulation is critical in maintaining high return fluid temperatures, thereby improving the overall energy conversion efficiency of retrofitted geothermal wells. These findings underscore the importance of system design optimization in maximizing geothermal energy recovery from existing hydrocarbon infrastructure. Topor et al. researched on assessing the geothermal potential of selected depleted oil and gas reservoirs based on geological modeling and machine learning tools. Advanced modeling techniques were employed to analyze the studied formations’ heat, storage, and transport properties. The obtained results were then used to calculate the heat in place (HIP) and evaluate the recoverable heat (Hrec) for both water and CO2 as working fluids, considering a geothermal system lifetime of 50 years.
Gabdrakhmanova et al. developed a new approach to the selection of resource-attractive wells. They developed a mathematical model that is determined by the temperature gradient, well depth, bottom, and coolant temperatures. Depending on the depth and temperature gradients, these nomograms determine injection rates. Based on these nomograms, it is possible to predict what thermal power can be obtained from a certain well at a given coolant injection rate.
Gudmundsdottir and Horne used the feedforward model (MLP) and recurrent neural network (RNN) models to predict tracer concentrations in the production well to investigate the breakthrough in the synthetic fractured reservoir. They found that the MLP model performed better and faster in training compared to the RNN model.
Yan et al. developed a robust general thermal decline model for geothermal reservoirs. They integrated it with deep learning (DL) and multi-objective optimization for geothermal reservoir management considering uncertainties in reservoir property. They also used the Fourier neural operator to predict the geothermal temperature field over time with a heterogeneous fracture aperture field in EGS with high precision and further performed reservoir optimization for temperature control based on a control neural network (NN) or stochastic gradient descent method. Kalogirou et al. developed thermal maps at three different depths such as 20, 50, and 100 m using artificial NNs.
Regions characterized by intense tectonic activity exhibit elevated geothermal gradients, leading to higher temperatures at shallower depths in contrast to regions with normal geothermal gradients (about 1.5°C every 100 meters). Although high-temperature regions are optimal for generating power, their isolated locations frequently present substantial obstacles to development. Electricity generation is technically and economically impractical at temperatures below 80°C. Conventional geothermal power facilities of significant size necessitate reservoir temperatures that surpass 150°C . There are a significant number of abandoned oil and gas wells globally, with around 3.2 million in the United States alone and over 200,000 in China . Many wells in the Niger Delta are reaching their economic limits and abandoned wells are growing in numbers, with potentially few of them already experiencing varying degrees of leakage, thereby causing environmental hazards. Though, applications of geothermal well system has gained acceptance in the re-use of depleted oil reservoirs in some countries, however, there are limited studies (and no field application to the est of our knowledge) on the conversion of depleted oil reservoirs into a geothermal well system in the Niger Delta.
This study intends to explore the technical feasibility and economic analysis of converting depleted oil reservoirs in the Niger Delta region into a geothermal well system. The specific objectives will be to characterize and screen wells in depleted oil reservoirs for geothermal system development in the Niger Delta; model the well performances of some Niger Delta wells in depleted oil reservoirs for geothermal gradient estimation; model and evaluate geothermal well systems in some depleted oil reservoirs; perform sensitivity analysis to assess the impact of different operating parameters on overall heat recovery; and evaluate the economic feasibility of converting wells in depleted oil reservoirs in the Niger Delta into geothermal wells.
2. Data Used for the Study and Methodology
The Niger Delta is one of the most productive deltaic petroleum systems, with decades of oil and gas exploration and exploitation activities, in the world. It has over 12,000 m of sediments, which is composed of three diachronous siliciclastic units: the deep-marine pro-delta Akata Group, the shallow-marine delta-front Agbada Group and the continental, delta-top Benin Group .
Lithologically, the Niger Delta is stratified into three major formations: the Akata, Agbada, and Benin Formations . Thermal conductivity in the Niger Delta formations typically ranges between 1.2-2.5 W/(m·K), depending on lithology. Formation water in Agbada formation typically has densities of 1,050-1,170 kg/m3 and salinities that can exceed 35,000 ppm . The Benin sands serve as the region’s main aquifer, with groundwater densities around 1,000 kg/m3 and relatively low total dissolved solids compared to deeper formations.
In the Nigerian oil and gas sector, as at 2023, there were over 200 fields, more than 1200 reservoirs and over 2500 wells with records of technical allowable rates . The dataset used in this study was sourced from a confidential report provided by the reservoir management database of a major oil-producing company operating in the Niger Delta. The dataset underwent rigorous quality assurance and validation using established petroleum engineering protocols to ensure data integrity and reliability. Key parameters assessed included detailed rock and fluid properties, as well as comprehensive well characteristics.
2.1. Methodology
The approach adopted in this study involves characterization and screening the gathered well data, well performance simulation, overall heat estimation from the well and economic analysis.
2.1.1. Characterization and Screening
Characterization and screening of wells in depleted oil reservoirs for use for GWS were carried out using a dataset of 110 wells obtained from the Niger Delta. Figure 1 depicts the temperature distributions of the wells, showing a reservoir temperature from 90°F to 265°F. According to Riney , electricity generation for GWS is technically and economically impractical at temperatures below 80°C (176°F). Therefore, over 50 wells from the gathered wells were candidates for GWS development. Figure 2 presents the candidate wells considered for GWS application.
Figure 1. General distribution of temperature for gathered wells.
Further screening was carried out considering water cut to identify wells approaching abandonment, Figure 3 shows the distribution of water cut values for the gathered wells, ranging from 1% to 98%. Considering a water cut of 85% to mark wells approaching abandonment, about 33 wells were identified, as presented in Figure 4. Therefore, with a reservoir temperature above 176°F and water cut above 85%, ten (10) wells were identified as immediate candidate for GWS application. These ten (10) wells (as summarized in Table 1) were considered in this study for modelling of the well performance of GWS in depleted oil reservoirs.
Figure 2. Temperature distribution for the gathered well above 176°F.
Figure 3. Water cut distributions for the gathered wells.
Figure 4. Water cut distributions for the gathered wells, above 85%.
Table 1. Reservoir, fluid, and well parameters.

Well Properties

Well 1

Well 2

Well 3

Well 4

Well 5

Well 6

Well 7

Well 8

Well 9

Well 10

Fluid Type

oil

oil

Oil

oil

oil

Oil

oil

oil

oil

oil

Tubing Size (M)

2.875

2.375

2.375

2.875

2.875

2.875

31/5’’

2.875

2.375

2.375

Current GOR (scf/bbl)

418

1139

4258

1376

10938

1505

333

3500

2536

2142

APIo

38.03

35.14

30.29

30.60

36.09

33.74

26.97

39.74

41.00

41.00

BSW (%)

85.00

57.00

87.00

19.00

40.00

20.00

16.60

91.00

81.00

37.00

THP (psig)

189

600

200

420

2000

725

305

290

232

1102

Current Reservoir Pressure (psia)

4058

3352

3230

3230

3281

3401

4030

3585

3564.7

3250

Porosity (%)

23

29

26

23

28

26

31

18

22

25

Permeability (md)

423

526

662

436

511

605

431

220

453

395

Water Saturation (%)

17

22

10

16

21

12

40

30

13

25

Thickness (ft)

80

59

90

110

42

30

120

35

61

32

Casing Depth (ft)

10510

7375

10908

7972

8820

8248

7,718

9507

9199

8566

Tubing Depth +0.5h (ft)

10456

7362

10875

7959

8751

8225

7,702

9493

9181

8520

Reservoir Temperature (°F)

218

162

221

182

168

152

150

194

190

182

Drainage Area (ft)

31

32

22

17

52

54

19

72

34

94

2.1.2. Well Performance Simulation
Figure 5. Typical wellbore schematic of one the modeled wells.
PROSPER® - a commercial software for well performance simulation was then employed to model and evaluate the temperature and pressure profiles, the IPR and VLP of the screened wells (see, Table 1 of the summary of the reservoir, fluid and well properties) to determine stable operating points or productivity of the wells; and sensitivity analyses were performed on critical variables such as tubing head pressures or reservoir pressure, tubing diameters, and water cut percentages. A typical modeled well is presented in the Figure 5.
2.1.3. Estimation of Overall Heat Recovered
The overall heat recovered was estimated using Equations (1) and (2).
Qrev= Cpw+ρw×qw+Cpo×ρo×qo×Ti-To(1)
Q=Cp×ρ×q×Ti-To(2)
where Qrev is the recoverable thermal power, Q is the heat flow, Cp is the specific heat of the fluid, (W/kg K); ρ is the fluid density (kg/m3), q is the fluid flow rate (m3/s), Ti is the fluid temperature at wellhead (°C), To is the fluid temperature at the exit of electrical generator (°C), Cpw is the specific heat of water, equal to 4186 W/kg K, ρw is the water density (kg/m3), qw is the water flow rate (m3/s), Cpo is the specific heat of oil, equal to 2286 W/kg K, ρo is the oil density (kg/m3), qo is the oil flow rate (m3/s).
2.2. Economic Analysis
A simplified economic evaluation was carried out to assess the investment in converting depleted oil wells to create geothermal wells, considering vertical coaxial GWS. The simplified capital cost economics of the geothermal well system (GWS) installation were estimated using Equation (3), taking into account the recommendations of Tester et al. .
Ccap= Cgath+Csim+Cplant(3)
where Ccap, capital expenditure (CAPEX), Cgath, field gathering system cost calculated based on a 750 m from each well to the power plant, at an assumed installation cost of $500 per meter for Niger Delta, Csim, the reservoir simulation cost, the U.S. Department of Energy (DOE) provides a baseline estimate of $1.25 million per well for new wells in enhanced geothermal systems and Cplant, surface power plant cost, was estimated based on the plant type, capacity, and geofluid production temperature. According to NUPRC, the plant capital cost was estimated at $ 250 kWt/h.
Other economic indices: return on investment (ROI), net present value (NPV), and internal rate of return (IRR) were estimated as expressed in Equations (4) through (6).
PV= FV1+i-t(4)
NPV=PV(5)
IRR=Co+n=1nCn1+RORn=0(6)
where PV = present value, FV = future value, t = time in years, i= discount rate and Co = initial cost.
3. Results and Discussion
The screening of the gathered data for wells in depleted oil reservoirs for use for GWS showed only ten (10) wells out of the 110 wells investigated were potential candidates, considering Riney’s statement that electricity generation for GWS is technically and economically impractical at temperatures below 80°C (176°F), and also considering water cut of 85% and more. Summary of the reservoir, fluid and well properties has been presented in Table 1.
3.1. Pressure and Temperature Gradients Estimation
Figure 6 presents typical pressure gradient curves for some five (5) selected wells, while Figure 7 depicts the temperature gradient curves for some five (5) selected wells. The pressure gradients for the selected wells range from 0.223 to 0.381 psig/ft, and the temperature gradient ranges from 0.02 to 0.023°F/ft. Figure 8 shows the regression analysis performed to identify the linear correlation between temperature and depth of the wells. An average temperature gradient of 0.011 oF/ft was obtained, with an approximate regression performance (R2) value of 0.87.
Figure 6. Combine pressure gradient curves for some selected 5 wells.
Figure 7. Combine temperature gradient curves for some 5 wells.
Figure 8. Regression analysis of the temperature gradients for the wells studied.
3.2. Inflow Performance Relationship (IPR) / Vertical Lift Performance (VLP)
The inflow performance relation (IPR) is a plot of pressure against the flow rate of the reservoir fluids. The absolute open flow potential (AOFP) for well 1 is 1547342 stb/day, as shown in Figure 9. Figure 9 also shows the AOFPs for four (4) other wells under study; these values range from 45444 to 154731stb/day. Figure 10 shows the IPR and VLP curves to generate the stable operating condition for a flowing well - well 1, as a case study, and Table 2 presents the summary of the IPR/VLP sensitivity results for well 1 for various tubing sizes, where stable operating point is possible.
Figure 9. IPR curves for some selected wells.
Figure 10. IPR/VLP curve for well 1.
Table 2. Summary of IPR/VLP sensitivity results for well 1.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Oil rate (stb/day)

Water rate (stb/day)

Gas rate (MMscf/day)

Node pressure (psig)

60

4000

3

3922.4

1569

2353.5

0.65583

3910.7

60

4000

4

7368.3

2947.3

4421

1.232

3832.26

60

4000

5

10686.9

4274.7

6412.1

1.787

3756.71

3.3. Sensitivity Analyses of Some Parameters Affecting Well Performance
Sensitivity analyses on water cut, tubing size and reservoir pressure were performed to evaluate their effects on the wells’ productivities under study. According to the sensitivity analyses carried out, it was observed that, at water cut of 60%, 70% and 80%, the results show a stable linear progressive operating solution condition. Also, as the reservoir pressure increases, the liquid rate increases alongside with different tubing sizes. However, for some of the tubing sizes, there were no stable operating solution details. Hence, it can be concluded that a higher flow rate depends on the tubing internal diameter size. Figures 11 through 13 present the sensitivity analysis for a case - well 3, at varying water cut, tubing sizes and reservoir pressure.
Figure 11. Sensitivity analysis for well 3 with 60% water cut.
Figure 12. Sensitivity analysis for well 3 with 70% water cut.
Figure 13. Sensitivity analysis for well 3 with 80% water cut.
3.4. Estimated Heat Generation from Well
The estimated overall heat recovered for the proposed GWS in this study was evaluated. It was observed that, as the liquid flow rate increases alongside different tubing sizes, there is a high rate of recoverable heat generated that is sufficient for the production of geothermal well system for electricity production. The estimated overall heat capacity for well 3 at varying internal tubing diameter and water cut is shown in Figure 14.
Figure 14. Thermal heat power for vertical coaxial system for well 3.
Table 3 presents the summary of the estimated average heat recovery (along with its standard deviation) for the wells under study. Tables 6 through 10 present the estimated heat recovery for some of the wells under study at various operating conditions.
Table 3. Summary of the estimated average heat recovery (along with its standard deviation) for the wells under study.

WELL

Average Estimated Heat Recovery, from the stable operating conditions J/s

Standard deviation of the estimated Heat Recovery, from the stable operating conditions, J/s

1

2137106.706

926383.6

2

3828415.673

1113605

3

8809371.794

2113289

4

5750277.777

1652454

5

85364.39235

11484.27

6

2625683.539

605983.2

7

2396355.487

269760.5

8

8073533.634

1487695

9

5604048.093

1522610

10

3537336.387

8200.522

3.5. Economic Analyses
Table 4 present the summary of the economic analyses for the ten (10) wells evaluated for GWS development proposed in this study. Figure 15 presents the NPV of some of the potential candidate wells for GWS development for the study. According to guidelines for the preparation of feasibility studies and economic viability oil business , typical IRR thresholds for viability project is roughly 12- 15% on investment. Nine out of the ten (10) wells evaluated met this criterion. Well 5 did not meet the IRR threshold of 12 - 15%, as the well produces more of gas. The gas-oil ratio of well 5 is quite high.
Table 4. Summary of wells economic analysis for GWS development.

Well

Total Cost ($)

Total Revenue ($)

Average Qrev (j/s)

NPV at 10%, ($)

NPV at 20%, ($)

NPV at 30% ($)

IRR (%)

Remarks

Well 1

10729873

1797221.503

2137106.706

2110496.63

-1397850.516

-3376470.233

18

Possible viable for Geothermal well system is greater than 12- 15% IRR

well 2

16649455

3219544.444

3828415.673

6352796.333

67939.65556

-3476561.737

20

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 3

34200553

7408329.304

8809371.794

18728752.85

4266990.111

-3889081.031

25

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 4

23375972

4835753.599

5750277.777

6777254.461

-2296251.089

-7310105.602

20

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 5

3548775.4

71787.70944

85364.39235

-3035883.293

-3176019.723

-3255053.151

0.5

not economic viable for geothermal well system

Well 6

12439892

2208094.829

2625683.539

3335989.681

-974421.2384

-3405384.79

19

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 7

11637244

2015239.11

2396355.487

2760767.058

-1173171.174

-3391813.58

19

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 8

23567921

6789518.845

8073533.634

24940252

11686466.08

4211663.533

40

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 9

22864168.33

4712780.284

5604048.093

10806606.67

1606811.742

-3581641.647

25

Possible viable for Geothermal well system is greater than 12- 15% IRR

Well 10

15630677.36

2974758.408

3537336.387

5622683.709

-184327.3651

-3459335.834

20

Possible viable for Geothermal well system is greater than 12- 15% IRR

Figure 15. Combined NPV curve plot for selected wells.
3.6. Comparing This Study with Some Related Existing Studies
The technical and economic findings of this research are consistent with published studies on geothermal repurposing of depleted oil reservoirs. For example, Bu et al. and Wang et al. reported similar ranges of recoverable heat and economic feasibility when evaluating abandoned oilfield assets in China and elsewhere. The recoverable heat and power generation estimates derived in this study for the Niger Delta wells fall within the expected range for low- to medium-enthalpy geothermal systems. These comparative results strengthen confidence in the methodology and confirm that repurposing depleted hydrocarbon wells in the Niger Delta is in line with global trends and technical best practices. Key differences observed relate to local geological and operational characteristics, suggesting the need for site-specific screening and adaptation of international models when applied to the regional context. As summarized in Table 5, the present study compares favourably with other existing studies. The results are in tandem with typical thermal heat output of geothermal wells for high temperature geothermal wells development.
Table 5. Analysis of the study with some related existing studies.

Author (s)

Depth (ft)

Temp. °C

Pressure (psia)

Fluid flow rate

Type of fluid used

Type of GWS

Heat generated

Steward

6561.68

72

Not stated

Not stated

CO2

Deep geothermal single well

1,800000 kWh

Usuolori et al.

2438.4

96

3992

Not stated

CO2 and Water vapour

Not stated

59.39 ×1018 J

Sennaoui et al.

2500

178.26

Not stated

1-57Kg/s

Cool fluid

Coaxial close-loop (vertical & L-shape)

1361.95 KW

This study

10211

90

3585

2890.3 stb/day

Oil and water

Vertical Coaxial open loop

8073.53 KW (Well 8)

4. Conclusion
A comprehensive evaluation was conducted on a dataset of 110 wells, with screening based on reservoir temperature and water cut to identify suitable candidates for geothermal conversion. Reservoir temperatures ranged from 90°F to 265°F, and applying a minimum threshold of 176°F for electricity generation narrowed the candidate pool to over 50 wells. Subsequent screening using a water cut of ≥85% identified 10 wells as immediate candidates for the geothermal well system (GWS) application.
Well performance was assessed using a production system simulator, involving more than 1,000 simulation runs to examine the influence of tubing size, reservoir pressure, temperature, and water cut. The results revealed pressure gradients of 0.223 - 0.381 psig/ft and temperature gradients of 0.020 - 0.023°F/ft. Inflow performance and vertical lift analyses confirmed stable operating conditions, with liquid production rates strongly influenced by tubing internal diameter and reservoir pressure. The estimated recoverable heat ranged from 0.1 MW to 8 MW.
Economic analysis, using net present value (NPV) and internal rate of return (IRR) criteria, demonstrated that several wells are economically viable. The thermal power output achieved approximately 8 MW, with IRR values meeting the 12-15% viability threshold. Based on these findings, the following conclusions were drawn:
1) The findings of this study confirm that vertical coaxial open-loop depleted oil configuration reservoirs can be technically and economically viable for direct reuse for geothermal applications.
2) Flow rate is a primary control on thermal output for GWS development that is heavily dependent on well geometry.
3) Pressure and temperature gradients, water cut, and overall heat recovered are key reservoir and operational parameters considered for GWS.
4) Sensitivity analyses indicate that a higher flow rate depends on the tubing internal diameter size, considering water cut, tubing size, and reservoir pressure.
5) The recoverable heat and power generation estimates derived in this study for the Niger Delta wells fall within the expected range for low- to medium-enthalpy geothermal; therefore, the technical assessment and economic analysis presented in this work demonstrate that depleted oil reservoirs, particularly those with high water cut and adequate reservoir temperature, can be successfully repurposed as geothermal well systems. The results provide compelling evidence that geothermal conversion is not only feasible but also offers a practical pathway for extending the productive life of mature oilfields. This recovery of interest in geothermal applications, especially in regions like the Niger Delta, opens up new opportunities for sustainable energy generation by leveraging existing oilfield infrastructure. The findings encourage further exploration and investment in geothermal well systems as a means to diversify energy portfolios and promote cleaner energy sources.
5. Recommendation and Suggestion for Further Studies
Based on the conclusions drawn, the following recommendations are proposed:
Conduct comprehensive field evaluations to validate the technical and economic findings of this study. Power plant operators and energy generation companies should collaborate on pilot-scale field analyses to confirm model predictions and refine system design.
Foster partnerships between the oil and gas and geothermal sectors to leverage shared expertise and infrastructure, enhancing project feasibility and reducing costs.
Support further research on advanced well configurations, working fluids, and heat extraction technologies to maximize geothermal output from depleted reservoirs in the Niger Delta.
Future studies should investigate the application of closed-loop horizontal well configurations and hybrid system designs for geothermal energy production from depleted oil reservoirs. Such research could provide deeper insights into optimizing heat recovery, enhancing system efficiency, and expanding the range of viable reservoir candidates in the Niger Delta.
Abbreviations

AOFP

Absolute Open Flow Potential

API

American Petroleum Institute

BSW

Basic Sediment & Water

CAPEX

Capital Expenditure

DL

Deep Learning

FV

Future Value

GOR

Gas-Oil Ratio

GSHP

Ground Source Heat Pump

GWS

Geothermal Well Systems

HIP

Heat In Place

HSA

Hot Sedimentary Aquifer

HT

High Temperature

IPR

Inflow Performance Relationship

IRR

Internal Rate of Return

MT

Medium Temperature

NN

Neural Network

NPV

Net Present Value

ORC

Organic Rankine Cycle

NUPRC

Nigerian Upstream Petroleum Regulatory Commission

PROSPER™

Production System Performance Software

PV

Present Value

ROI

Return On Investment

RNN

Recurrent Neural Network

THP

Tubing Head Pressure

VLP

Vertical Lift Performance

Author Contributions
Joy Jumbo Itah: Data curation, Formal Analysis, Writing – original draft
Aniefiok Livinus: Conceptualization, Resources, Supervision, Writing – review & editing
Isaac Ouets: Writing – review & editing
Data Availability Statement
The full datasets used and/or analysed during the current study available from the corresponding author on reasonable request.
Conflicts of Interest
The authors declare no conflicts of interest.
Appendix
Table 6. Estimated Heat Recovery, J/s, for Well 1, where there are stable operating conditions.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Qrev, J/s; W

60

4000

3

3922.4

1204965.301

60

4000

4

7368.3

2148731.654

60

4000

5

10686.9

3057623.162

Table 7. Estimated Heat Recovery, J/s, for Well 2, where there are stable operating conditions.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Q, Heat Recovery, J/s.W

60

3000

3

4409.4

2681158.18

60

3000

3.5

6035.9

2909024.631

60

3000

4

7613.3

3129980.379

60

3000

5

10266

3501570.793

60

4000

2

3622.5

2570937.123

60

4000

3

9859.8

3444674.221

60

4000

3.5

13900.9

4010768.263

60

4000

4

18293.3

4626054.375

60

4000

5

27122.7

5862883.59

70

3000

3

2483.8

2469424.487

70

3000

3.5

3184.1

2583871.346

70

3000

4

3912.4

2702894.211

70

3000

5

4541.9

2805760.972

70

4000

2

3476.8

2631685.945

70

4000

3

9454.3

3608593.315

70

4000

3.5

13260.8

4230696.743

70

4000

4

17311.2

4892630.107

70

4000

5

25177.3

6178184.453

80

4000

2

3241.6

2668947.713

80

4000

3

8784.2

3704152.473

80

4000

3.5

12152.8

4333353.381

80

4000

4

15634.4

4983613.259

80

4000

5

21959.3

6164946.719

90

4000

2

2788.5

2649429.644

90

4000

3

7356.3

3609223.683

90

4000

3.5

9972.2

4158881.456

90

4000

4

12488.7

4687667.036

90

4000

5

16443.1

5518562.439

95

4000

2

2443.7

2605490.642

95

4000

3

6206.4

3440051.52

95

4000

3.5

8181.8

3878180.806

95

4000

4

9951.6

4270713.454

95

4000

5

12444.8

4823709.844

Table 8. Estimated Heat Recovery, J/s, for Well 3, where there are stable operating conditions.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Qrev, J/s.W

60

1800

2

442

6252486.496

60

1800

3.5

2787.6

6911672.938

60

1800

4

4117.1

7285293.106

60

1800

5

7318.7

8184988.457

60

2000

2

630.6

6305506.181

60

2000

3

2362.9

6792331.809

60

2000

3.5

3645

7152603.381

60

2000

4

5220.9

7595448.898

60

2000

5

9105.1

8687036.167

60

2500

2

1103.5

6438383.255

60

2500

3

3719

7173399.088

60

2500

3.5

5580.3

7696476.691

60

2500

4

7827.6

8328029.198

60

2500

5

13329.2

9874077.604

60

3000

2

1578

6571728.701

60

3000

3

4916.4

7509877.374

60

3000

3.5

7304.5

8181007.297

60

3000

4

10194.3

8993117.125

60

3000

5

17307.7

10992127.88

60

4000

2

2427

6810317.285

60

4000

3

7038.6

8106301.998

60

4000

3.5

10407.8

9053115.55

60

4000

4

14468.7

10194303.39

60

4000

5

24645.9

13054321.98

70

1800

3.5

2461.4

6935278.876

70

1800

4

3674.9

7333113.865

70

1800

5

6684.4

8319832.692

70

2000

3

2187.4

6845445.168

70

2000

3.5

3378.9

7236067.232

70

2000

4

4893.9

7732775.504

70

2000

5

8603.9

8949137.015

70

2500

2

695.2

6356184.008

70

2500

3

3628.9

7318079.131

70

2500

3.5

5477.6

7924152.213

70

2500

4

7699.6

8652657.678

70

2500

5

13131.2

10433500.86

70

3000

2

1382.9

6581658.182

70

3000

3

4933.7

7745843.077

70

3000

3.5

7342.2

8535471.059

70

3000

4

10252.1

9489544.373

70

3000

5

17368.3

11822644.72

70

4000

2

2494.9

6946238.775

70

4000

3

7266.1

8510553.681

70

4000

3.5

10741.8

9650055.382

70

4000

4

14927.6

11022431.53

70

4000

5

25399.8

14455830.86

80

1800

5

4184.7

7696242.505

80

2000

3.5

2269.3

6978556.428

80

2000

4

3431.7

7414142.183

80

2000

5

6417.7

8532941.852

80

2500

3

3099.1

7289508.452

80

2500

3.5

4778.5

7918765.938

80

2500

4

6764

8662727.672

80

2500

5

11589.9

10470970.6

80

3000

3

4645.7

7868978.017

80

3000

3.5

6947.3

8731437.812

80

3000

4

9697

9761715.214

80

3000

5

16407.5

12276122.27

80

4000

2

2502.2

7065814.09

80

4000

3

7323.7

8872464.554

80

4000

3.5

10835.4

10188261.39

80

4000

4

15051.7

11768126.24

80

4000

5

25496.1

15681606.64

90

3000

3

2716

7273162.277

90

3000

3.5

4344.6

7959654.794

90

3000

4

6160.5

8725161.63

90

3000

5

10551.9

10576260.58

90

4000

2

2233.1

7069607.902

90

4000

3

6632.1

8923938.613

90

4000

3.5

9808.9

10263060.37

90

4000

4

13649.7

11882127.93

90

4000

5

22900.7

15781744.53

95

4000

3

4638.7

8192295.057

95

4000

3.5

6941.9

9217092.509

95

4000

4

9617.8

10407740.41

95

4000

5

15717

13121580.17

Table 9. Estimated Heat Recovery, J/s, for Well 4, where there are stable operating conditions.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Qrev, J/s.W

60

2500

3

3217.2

3867962.563

60

2500

3.5

4757.1

4157141.315

60

2500

4

6371.1

4460215.67

60

2500

5

9377.8

5024802.758

60

3000

3

5691.7

4332620.24

60

3000

3.5

8197.5

4803161.641

60

3000

4

10979.4

5325561.179

60

3000

5

16733.3

6406006.857

60

4000

2

3525.5

3925860.906

60

4000

3

9863.3

5115969.176

60

4000

3.5

14235.3

5936936.387

60

4000

4

19182.4

6865907.481

60

4000

5

30238.1

8941922.995

70

3000

3

4890.7

4335280.434

70

3000

3.5

7009.4

4799437.369

70

3000

4

9291.8

5299428.683

70

3000

5

13714.7

6268396.578

70

4000

2

3448

4019218.073

70

4000

3

9642.7

5376323.942

70

4000

3.5

13831.6

6293997.035

70

4000

4

18570.4

7332161.274

70

4000

5

29009.8

9619145.833

80

3000

3

2703.9

3940820.586

80

3000

3.5

3804.4

4216354.108

80

3000

4

4851.6

4478555.362

80

3000

5

6386.8

4862906.472

80

4000

2

3261.7

4080465.131

80

4000

3

9142.2

5552773.056

80

4000

3.5

13040.6

6528845.234

80

4000

4

17361.6

7610699.25

80

4000

5

26437.2

9882974.499

90

4000

2

2864.6

4070700.654

90

4000

3

7952.3

5503762.89

90

4000

3.5

11139

6401343.693

90

4000

4

14505.9

7349687.259

90

4000

5

20888.4

9147446.465

95

4000

2

2453.3

3993273.356

95

4000

3

6578.8

5219841.934

95

4000

3.5

8980

5933744.154

95

4000

4

11372.1

6644954.884

95

4000

5

15374

7834781.486

Table 10. Estimated Heat Recovery, J/s, for Well 5, where there are stable operating conditions.

Water cut (%)

Reservoir pressure (psig)

Tubing size (inches)

Liquid rate (stb/day)

Qrev, J/s.W

60

4000

2

86.2

66255.0972

60

4000

3

2672.4

77367.8264

60

4000

3.5

3990.1

83029.82531

60

4000

4

5418.2

89166.64148

60

4000

5

8621.3

102930.6128

70

4000

3

2611.7

78977.76487

70

4000

3.5

3843.2

85151.10545

70

4000

4

5175.6

91830.77454

70

4000

5

7910

105538.885

80

4000

4

2345.3

79321.52398

80

4000

5

2365.6

79438.25884

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Cite This Article
  • APA Style

    Itah, J. J., Livinus, A., Ouets, I. (2026). A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta. International Journal of Oil, Gas and Coal Engineering, 14(4), 88-107. https://doi.org/10.11648/j.ogce.20261404.13

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    ACS Style

    Itah, J. J.; Livinus, A.; Ouets, I. A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta. Int. J. Oil Gas Coal Eng. 2026, 14(4), 88-107. doi: 10.11648/j.ogce.20261404.13

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    AMA Style

    Itah JJ, Livinus A, Ouets I. A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta. Int J Oil Gas Coal Eng. 2026;14(4):88-107. doi: 10.11648/j.ogce.20261404.13

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  • @article{10.11648/j.ogce.20261404.13,
      author = {Joy Jumbo Itah and Aniefiok Livinus and Isaac Ouets},
      title = {A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta},
      journal = {International Journal of Oil, Gas and Coal Engineering},
      volume = {14},
      number = {4},
      pages = {88-107},
      doi = {10.11648/j.ogce.20261404.13},
      url = {https://doi.org/10.11648/j.ogce.20261404.13},
      eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ogce.20261404.13},
      abstract = {Majority of matured and abandoned wells in depleted oil reservoirs in the Niger Delta are becoming economically unviable. Recently, application of geothermal well system has gained acceptance in the re-use of wells in depleted oil reservoirs. Unfortunately, there are limited studies in the conversion of matured and abandoned wells into geothermal well system in the Niger Delta. Therefore, this study evaluates the techno-economic feasibility of applying geothermal well systems (GWS) in wells in depleted oil reservoirs in the Niger Delta. In this study, characterization and screening of the gathered data from wells in depleted oil reservoirs were performed for GWS application, considering a reservoir temperature above 80°C (176°F) and a water cut of more than 85%. The screened well data were modelled using petroleum production software, PROSPER™, to evaluate their performances and estimate geothermal gradients. A model was developed from a simple regression technique in Microsoft Excel software to predict fluid flowing temperature gradient, using the simulated geothermal data. From the result, the temperature gradient varies by 0.011°F/ft. Estimation of overall heat recovery was then calculated with a simplified heat model, considering an open loop vertical coaxial single geothermal well system. The estimated overall heat recovery ranged from 0.1 MW to 8 MW, for the wells under study. Sensitivity analyses were also conducted to assess the impact of various operating parameters on the overall heat recovery. Finally, economic analyses were performed to evaluate the economic viability of converting matured and abandoned oil wells into geothermal well systems; the simplified economic analyses, considering net present value (NPV), showed geothermal well system with heat capacity above 5 MW to be economically viable. The study demonstrates that wells in depleted oil reservoirs in the Niger Delta can be effectively repurposed for geothermal electricity generation.},
     year = {2026}
    }
    

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  • TY  - JOUR
    T1  - A Simulation Approach on the Techno-economic Feasibility of Wells in Depleted Oil Reservoirs for Geothermal Well Systems in the Niger Delta
    AU  - Joy Jumbo Itah
    AU  - Aniefiok Livinus
    AU  - Isaac Ouets
    Y1  - 2026/08/20
    PY  - 2026
    N1  - https://doi.org/10.11648/j.ogce.20261404.13
    DO  - 10.11648/j.ogce.20261404.13
    T2  - International Journal of Oil, Gas and Coal Engineering
    JF  - International Journal of Oil, Gas and Coal Engineering
    JO  - International Journal of Oil, Gas and Coal Engineering
    SP  - 88
    EP  - 107
    PB  - Science Publishing Group
    SN  - 2376-7677
    UR  - https://doi.org/10.11648/j.ogce.20261404.13
    AB  - Majority of matured and abandoned wells in depleted oil reservoirs in the Niger Delta are becoming economically unviable. Recently, application of geothermal well system has gained acceptance in the re-use of wells in depleted oil reservoirs. Unfortunately, there are limited studies in the conversion of matured and abandoned wells into geothermal well system in the Niger Delta. Therefore, this study evaluates the techno-economic feasibility of applying geothermal well systems (GWS) in wells in depleted oil reservoirs in the Niger Delta. In this study, characterization and screening of the gathered data from wells in depleted oil reservoirs were performed for GWS application, considering a reservoir temperature above 80°C (176°F) and a water cut of more than 85%. The screened well data were modelled using petroleum production software, PROSPER™, to evaluate their performances and estimate geothermal gradients. A model was developed from a simple regression technique in Microsoft Excel software to predict fluid flowing temperature gradient, using the simulated geothermal data. From the result, the temperature gradient varies by 0.011°F/ft. Estimation of overall heat recovery was then calculated with a simplified heat model, considering an open loop vertical coaxial single geothermal well system. The estimated overall heat recovery ranged from 0.1 MW to 8 MW, for the wells under study. Sensitivity analyses were also conducted to assess the impact of various operating parameters on the overall heat recovery. Finally, economic analyses were performed to evaluate the economic viability of converting matured and abandoned oil wells into geothermal well systems; the simplified economic analyses, considering net present value (NPV), showed geothermal well system with heat capacity above 5 MW to be economically viable. The study demonstrates that wells in depleted oil reservoirs in the Niger Delta can be effectively repurposed for geothermal electricity generation.
    VL  - 14
    IS  - 4
    ER  - 

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