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 |
Geothermal Well Systems, Abandoned Wells, Niger Delta, Re-use of Oil Wells, Heat Recovery from Oil Wells
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 |
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 |
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 |
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 |
Author (s) | Depth (ft) | Temp. °C | Pressure (psia) | Fluid flow rate | Type of fluid used | Type of GWS | Heat generated |
|---|---|---|---|---|---|---|---|
Steward [31] | 6561.68 | 72 | Not stated | Not stated | CO2 | Deep geothermal single well | 1,800000 kWh |
Usuolori et al. [32] | 2438.4 | 96 | 3992 | Not stated | CO2 and Water vapour | Not stated | 59.39 J |
Sennaoui et al. [22] | 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) |
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 |
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 |
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 |
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 |
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 |
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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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
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
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
@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}
}
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 -