Submitted:
19 November 2024
Posted:
20 November 2024
You are already at the latest version
Abstract
Keywords:
1. Introduction
2. Cycles and Optimization Methods Used in Geothermal Power Plants
2.1. Dry Steam Cycle
2.2. Single and Double Flash Steam Cycles
2.3. Binary Cycle Systems
2.4. Optimization Methods Used in Geothermal Power Plants
3. Artificial Neural Networks and Genetic Algorithms
3.1. Artificial Neural Networks
3.2. Genetic Algorithm
4. Optimization of Geothermal Power Plants Using Genetic Algorithms and Artificial Neural Networks
5. Materials and Methods
- All processes are in thermodynamic equilibrium.
- Differences in kinetic and potential energy are negligible.
- Heat transfer to the environment from all equipment is negligible.
- Air is assumed to be an ideal gas.
- Cycles are considered to have balanced and steady flows.
- The amount of NCG (non-condensable gases) is negligible.
- It is assumed that all steam entering the plant condenses upon exiting.
- For exergy analyses, the annual average temperature of the region is taken as the dead state. According to meteorological data, this value is 17°C. Additionally, the dead state pressure is taken as the ambient pressure, which is 1 bar.
- Brine values are taken as water values.
- The mechanical efficiency of the turbine is assumed to be 99%.
- The mechanical efficiencies of the pump and fan are assumed to be 95%.
- The turbine exit pressure is assumed to be 0.2 bar higher than the condenser pressure.
6. Results
7. Discussion
- Traditional methods are limited in optimizing geothermal power plants due to difficulty in data analysis and slow response to dynamic data.
- Heuristic methods such as ANNs and GAs can create more effective optimization models, either separately or together.
- Innovative heuristic methods still rely on linear functions and regression analyses used in traditional methods.
- Models can be customized for different plants and problems, creating problem-specific algorithms.
- Heuristic methods can predict geothermal plant performance accurately, enabling dynamic monitoring and optimization.
- Modeling geothermal resources and wells with heuristic methods can develop plant operation strategies.
- GAs can work with large parametric data sets, creating potential solution sets and analyzing the most efficient operational parameters.
- Hybrid models developed using heuristic methods can produce fast, reliable, and consistent results for more complex problems.
- An innovative optimization method using a genetic algorithm with deep artificial neural networks as the fitness function has been developed.
- With the optimal operating conditions obtained through the developed innovative calculation method, a net power increase of 1,477 kW was achieved. This resulted in a net power increase of 39.41% for the examined geothermal plant.
- By optimizing the operating conditions with the calculation method, the reinjection temperature was reduced to 70.33°C, close to the design value, allowing for greater energy and exergy input to the plant.
- The exergy efficiencies of the equipment operating with low exergy efficiency under operational conditions were increased after optimization, resulting in overall plant exergy and energy efficiencies of 34.62% and 8.62%, respectively.
- As a result of the optimization, more efficient and balanced operating parameters were calculated under similar external and geothermal fluid conditions.
Author Contributions
Funding
Conflicts of Interest
References
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| State | Phase | Mass Flow Rate (kg/s) |
Temperature (0C) |
Pressure (bara) |
Enthalpy (kJ/kg) |
Entropy (kJ/kg) |
Exergy (kW) |
|---|---|---|---|---|---|---|---|
| 0geo | - | - | 17 | 1 1 11 |
71.45 | 0.2534 | - |
| 0orc | - | 17 | 239.9 | 1.1412 | - | ||
| J1 | Liquid | 228.8 | 144.2 | 607.64 | 1.7818 | 21,236.01 | |
| J2 | Liquid | 228.8 | 127.64 | 10.5 | 536.88 | 1.6089 | 16,524.32 |
| S1 | Steam | 6.97 | 152 | 2,748.3 | 6.8192 | 5,379.96 | |
| S2 | Liquid | 6,97 | 139 | 4.9 24.6 24 10 |
584.96 | 1.7287 | 596.23 |
| 6 | Liquid | 150 | 123 | 536.88 | 1.9927 | 7,484.89 | |
| 7 | Gas | 150 | 125 | 744.29 | 2.5139 | 15,915.16 | |
| J3 | Liquid | 228.8 | 115.24 | 484.23 | 1.4755 | 13,31334 | |
| 5 | Liquid | 150 | 98 | 25 9.5 |
455.46 | 1.7804 | 4,514.42 |
| J4 | Liquid | 228.8 | 102.94 | 432.23 | 1.3396 | 10,437.64 | |
| 10 | Liquid | 46.94 | 98 | 15.7 | 456.37 | 1.7881 | 1,350.56 |
| 11 | Gas | 46.94 | 100 | 15 | 720.89 | 2.4973 | 4,108.08 |
| J5 | Liquid | 228.8 | 70 | 8.5 | 293.73 | 0.9546 | 4,307.58 |
| 3 | Liquid | 196.94 | 41.11 | 27.6 | 300.57 | 1.327 | 1,331.34 |
| 4 | Liquid | 196.94 | 98 | 27 | 455.3 | 1.7788 | 5,987.05 |
| 8 | Gas | 196.94 | 58.21 | 4 | 675.93 | 2.5293 | 6,552.74 |
| 9 | Gas | 196.94 | 53.81 | 3.8 | 668.12 | 2.5123 | 5,986.06 |
| 2 | Liquid | 196.94 | 38 | 27.8 | 292.82 | 1.3021 | 1,227.89 |
| 1 | Liquid | 196.94 | 36.7 | 3.8 | 288.17 | 1.3010 | 374.98 |
| EQUIPMENT | Total Heat Transfer/Work (kW) | Total Exergy Destruction (kW) | Total Net Exergy Efficiency (%) |
Total Net Energy Efficiency (%) |
|---|---|---|---|---|
| HP EVAPORATOR | 31,269 | 1,049.62 | 88 | - |
| HP PREHEATER | 12,041.7 | 215.34 | 93.24 | - |
| LP EVAPORATOR | 11,897.6 | 118.18 | 95.89 | - |
| LPHP PREHEATER | 31,688.8 | 1,474.35 | 75.95 | - |
| REKUPERATOR | 1,538.1 | 456.2 | 17.91 | - |
| HP TURBINE | 10,254 | 661.26 | 93.86 | - |
| LP TURBINE | 2,110 | 1,561.82 | 82.86 | - |
| ORC PUMP | 915.77 | 62.86 | 93.14 | - |
| AC CONDENSER | 74,636 | 3,928.09 | 29.75 | - |
| POWER PLANT GROSS POWER | 12,240 | - | - | - |
| ORC CONSUMPTION | 1,920 | - | - | - |
| POWER PLANT NET POWER | 10,320 | - | - | - |
| OVERALL | 86,901.09 | - | 47.53 | 11.88 |
| State | Phase | Mass Flow Rate (kg/s) |
Temperature (0C) |
Pressure (bara) |
Enthalpy (kJ/kg) |
Entropy (kJ/kg) |
Exergy (kW) |
|---|---|---|---|---|---|---|---|
| 0geo | - | - | 17 | 1 1 11 |
71.45 | 0.2534 | - |
| 0orc | - | 17 | 239.9 | 1.1412 | - | ||
| J1 | Liquid | 160.75 | 149.6 | 630.45 | 1.8371 | 15,992.93 | |
| J2 | Liquid | 160.75 | 124 | 9 6.63 |
521.29 | 1.5702 | 10,894.1 |
| S1 | Steam | 2.69 | 167.4 | 2,771.9 | 6.7517 | 2,192.26 | |
| S2 | Liquid | 2.69 | 66 | 6.2 19.1 18.71 8.9 |
276.8 | 0.90567 | 43.3 |
| 6 | Liquid - Gas | 78.61 – 22.17 | 110.5 | 495.48 – 732.15 | 1.8898 – 2.5070 | 3,016.56 – 952.49 | |
| 7 | Gas | 100.78 | 112 | 736.02 | 2.5166 | 9,780.47 | |
| J3 | Liquid | 160.75 | 103 | 432.41 | 1.3404 | 7,324.88 | |
| 5 | Liquid | 100.78 | 81 | 19.2 8.36 |
406.21 | 1.6479 | 1,924.88 |
| J4 | Liquid | 160.75 | 88 | 369.2 | 1.1691 | 5.153.59 | |
| 10 | Liquid | 34.21 | 81 | 11.2 | 406.43 | 1.653 | 616.85 |
| 11 | Gas | 34.21 | 85 | 11.12 | 703.41 | 2.4838 | 2,529.99 |
| J5 | Liquid | 160.75 | 72.6 | 8 | 304.59 | 0.9863 | 3,293.62 |
| 3 | Liquid | 135 | 58 | 20 | 343.55 | 1.4645 | 1,329 |
| 4 | Liquid - Gas | 129.6 – 5.4 | 81 | 19.1 | 406.22 – 697.62 | 1.6479 – 2.4757 | 2,882.19 |
| 8 | Gas | 135 | 69 | 5.4 | 692.18 | 2.5388 | 6,313.18 |
| 9 | Gas | 135 | 60 | 5.38 | 673.89 | 2.4851 | 5,947.75 |
| 2 | Liquid | 135 | 52.5 | 20.5 | 329.22 | 1.4206 | 1,114.03 |
| 1 | Liquid | 135 | 52 | 5.35 | 327.33 | 1.4234 | 749.2 |
| EQUIPMENT | Total Heat Transfer/Work (kW) | Total Exergy Destruction (kW) | Total Net Exergy Efficiency (%) |
Total Net Energy Efficiency (%) |
|---|---|---|---|---|
| HP EVAPORATOR | 24,259.29 | 1,436.37 | 80.18 | - |
| HP PREHEATER | 14,287.46 | 1,544.32 | 57.85 | - |
| LP EVAPORATOR | 10,161 | 258.15 | 88.11 | - |
| LPHP PREHEATER | 10,386.05 | 306.78 | 83.51 | - |
| REKUPERATOR | 1,937.25 | 150.74 | 58.78 | - |
| HP TURBINE | 4,418.2 | 649.15 | 87.19 | - |
| LP TURBINE | 384.18 | 545.84 | 41.31 | - |
| ORC PUMP | 688 | - | - | - |
| AC CONDENSER | 46,785.6 | 3,773.37 | 27.41 | - |
| POWER PLANT GROSS POWER | 4,943 | - | - | - |
| ORC CONSUMPTION | 1,195 | - | - | - |
| POWER PLANT NET POWER | 3,748 | - | - | - |
| OVERALL | 59,093.82 | - | 25.24 | 6.34 |
| State | Phase | Mass Flow Rate (kg/s) |
Temperature (0C) |
Pressure (bara) |
Enthalpy (kJ/kg) |
Entropy (kJ/kg) |
Exergy (kW) |
|---|---|---|---|---|---|---|---|
| 0geo | - | - | 17 | 1 1 11 |
71.45 | 0.2534 | - |
| 0orc | - | 17 | 239.9 | 1.1412 | - | ||
| J1 | Liquid | 160.75 | 149.6 | 630.45 | 1.8387 | 15,992.93 | |
| J2 | Liquid | 160.75 | 123 | 9.5 6.63 |
517.07 | 1.5595 | 10,714.81 |
| S1 | Steam | 2.69 | 167.4 | 2,771.9 | 6.7517 | 2,192.26 | |
| S2 | Liquid | 2.69 | 66 | 6.2 22.5 22 9 |
276.8 | 0.90567 | 43.3 |
| 6 | Liquid | 115 | 119.7 | 525.9 | 1.9661 | 5,365.36 | |
| 7 | Gas | 115 | 120.4 | 742.79 | 2.5185 | 11,87564 | |
| J3 | Liquid | 160.75 | 102.76 | 431.39 | 1.3376 | 7,291.52 | |
| 5 | Liquid | 115 | 81 | 23 8.5 |
406.14 | 1.6455 | 2,290.49 |
| J4 | Liquid | 160.75 | 84.68 | 355.27 | 1.1302 | 4,728.7 | |
| 10 | Liquid | 40 | 81 | 13,5 | 406.37 | 1.6518 | 732.78 |
| 11 | Gas | 40 | 92.3 | 13 | 712.28 | 2.4911 | 3,228.26 |
| J5 | Liquid | 160.75 | 70.33 | 8 | 295.05 | 0.95862 | 3,051.1 |
| 3 | Liquid | 155 | 58 | 23.5 | 343.69 | 1.4627 | 1,628.55 |
| 4 | Liquid | 155 | 81 | 23.1 | 406.14 | 1.6455 | 3,087.19 |
| 8 | Gas | 155 | 69 | 5.4 | 692.18 | 2.5388 | 6,313.18 |
| 9 | Gas | 155 | 60 | 5.38 | 673.89 | 2.4851 | 5,947.75 |
| 2 | Liquid | 155 | 52.5 | 23.8 | 329.22 | 1.4206 | 1,114.03 |
| 1 | Liquid | 155 | 52 | 5.35 | 327.33 | 1.4234 | 749,2 |
| EQUIPMENT | Total Heat Transfer/Work (kW) | Total Exergy Destruction (kW) | Total Net Exergy Efficiency (%) |
Total Net Energy Efficiency (%) |
|---|---|---|---|---|
| HP EVAPORATOR | 24,937.65 | 916.99 | 87.65 | - |
| HP PREHEATER | 13,773.06 | 348.42 | 89.82 | - |
| LP EVAPORATOR | 12,236.29 | 67.34 | 97.37 | - |
| LPHP PREHEATER | 9,680.36 | 21.96 | 86.95 | - |
| REKUPERATOR | 2,224.25 | 150.74 | 58.78 | - |
| HP TURBINE | 5,820.15 | 677.36 | 89.58 | - |
| LP TURBINE | 804 | 553.61 | 59.22 | - |
| ORC PUMP | - | - | - | - |
| AC CONDENSER | 53,716.8 | 4,332.39 | - | - |
| POWER PLANT GROSS POWER | 6,624 | - | - | - |
| ORC CONSUMPTION | 1,399 | - | - | - |
| POWER PLANT NET POWER | 5,225 | - | - | - |
| OVERALL | 60,627.37 | - | 34.62 | 8.62 |
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