Implementation of Artificial Intelligence in Modeling and Control of Heat Pipes: A Review
Abstract
:1. Introduction
2. Background
3. Current Progress and Discussion
3.1. Optimal ANN Structure for Heat Pipe Modeling
3.2. Overfitting of Trained Prediction Models without Validation Sets
3.3. Prediction Models’ Input and Output Parameters
3.4. Dimensionless Numbers as Input Parameters
3.5. AI-Based Prediction Models for Heat Pipe Applications
3.6. Hybrid AI Methods for Working Condition Optimization
3.7. Intelligent Control Methods for Heat Pipes
3.8. Summary
4. Conclusions and Future Research Directions
- Most of the work on AI in heat pipes involves pulsating/oscillating heat pipes. This is mainly due to the difficulty of experimentally analyzing the effects of different parameters on the performance of a heat pipe, since its performance depends on several parameters. Furthermore, the numerical modeling of PHPs using computational fluid dynamics (CFD) is relatively complex due to the chaotic nature of PHPs, which shows the potential of AI-based modeling methods.
- ANN is the most widely used AI technology in predicting the performance of heat pipes and has proven its ability to be one of the most effective techniques for predicting performance accurately. As a result, it can be used for the efficient design of heat pipes.
- Multilayer perceptron neural networks (MLPNNs) achieved the highest accuracy in predicting the performance of heat pipe systems compared to other similar models.
- The AI model structure (number of hidden layers and neurons) is an important factor that influences the model’s prediction accuracy.
- The most common influencing input parameters are heat flux, filling ratio, and length of each heat pipe section (evaporator and condenser sections). In the case of nanofluid-filled heat pipes, nanofluid properties (such as concentration and thermal conductivity of nanofluid) are the most common input parameters that should be considered, as they most significantly influence the operation.
- Optimization algorithms and a combination of optimization algorithms and AI models can identify the optimum operating conditions of heat pipe systems.
- Fuzzy (and hybrid fuzzy) controllers are the most widely used controllers for heat pipes and heat pipe systems.
- Hybrid models combining metaheuristic optimization algorithms with AI-based models have shown excellent performance in modeling heat pipe systems. However, the current progress on hybridizing AI models with optimization algorithms is very limited, and further research on this topic is highly recommended. Optimization algorithms that were not hybridized previously with AI models for heat pipe modeling include grey wolf optimizer [74], ant colony optimization (ACO) [75], and the whale optimization algorithm (WOA) [76].
- Several recent AI models have performed superior tasks that were not previously applied for modeling heat pipe systems. These models include the recurrent neural networks (RNN) [77,78] and transformer networks [79,80] that showed excellent performance in sequential data prediction and modeling tasks, as well as generative adversarial networks (GAN) [81,82] that showed excellent performance in various AI tasks in general and modeling tasks in specific. Further works discussing the applications of these state-of-the-art models for modeling various aspects of heat pipe systems are highly recommended and are expected to improve the currently achieved limits of the AI-based modeling of heat pipes.
- The progress made on the AI-based control of heat pipe systems is very limited, and various types of intelligent control algorithms and target parameters have not previously been discussed in the literature. Most importantly, ANN showed excellent performance in different system control tasks and has not previously been used to control heat pipe systems’ operation. Thus, developing ANN-based methods for the operational control of heat pipe systems is highly recommended and expected to achieve higher performance compared to the currently applied techniques.
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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---|---|---|---|
Artificial Neural Network (ANN) | Easy to implement. Excellent capacity to predict several parameters together. It can be used to predict complex systems. | Training of the network is required. Larger network sizes require more data and longer training and processing time. | Optimizing photovoltaic systems [47], and modeling hydrogen production [25]. |
Fuzzy Logic | Flexible and allows modifications. Output decisions can be interpreted easily. Can handle multiple different inputs at the same time. | Mainly dependent on the expertise of the designer. Inaccurate designs result in wrong outputs. Requires extensive testing with equipment. | Water resource prediction [48], control of fuel cell vehicles [29]. |
Adaptive Neuro-Fuzzy Inference System (ANFIS) | Capable of modeling highly nonlinear processes. Achieves superior performance on tasks with a small number of inputs. | High computational cost. The trade-off between output accuracy and interpretability. Generated intermediate representations could be hard to interpret. | Analysis of concrete structures [49], medical imaging analysis [50]. |
Metaheuristic Optimization | Faster convergence speed compared to the classical optimization algorithm. Lower computational cost. Broad applicability. Easy to hybridize with other algorithms. | Not guaranteed to perform effectively on all tasks. Some problems could result in significantly longer processing times. It could be trapped in a local maxima. Requires careful parameter tuning. | Robot path planning [51], temperature control [45]. |
Control Method | Target Parameter | Ref. |
---|---|---|
PID | Temperature | [45] |
Nonlinear adaptive fuzzy controller | Energy (heat) wastage in the heat pipe radiator | [70] |
Fuzzy incremental control | LHP temperatures, condensing pressure, and mass flow rate | [71] |
Dual intelligent model (fuzzy fusing rules) | Temperature control and heat flux tracking effects | [72] |
AI Method | Type of Heat Pipe | Input Parameters | Output Parameters | Dataset Split | Accuracy | Ref. | |
---|---|---|---|---|---|---|---|
Training/Testing/Validation | MSE (*) RMSE (**) | R | |||||
MLPNN | Tube heat pipe and flat heat pipe solar collectors | Solar radiation, ambient temperature, inlet gas temperature, inlet water temperature, evaporator length, condenser length, gas mass flow rate, and water mass flow rate. | Collector efficiency and heat output | 70%/15%/15% | 0.0050 * | 0.9460 | [66] |
MLPNN | 0.0002 * | 0.9995 | |||||
GA-MLPNN | PHP | Filling ratio, inclined angle, and input heat flux to the evaporator | Thermal resistance | 70%/30%/x | x | x | [69] |
MLPNN | PHP | Heat flux, number of turns, filling ratio, length ratio of evaporation section, and inner diameter | Thermal resistance | 70%/15%/15% | 0.0025 * | 0.9962 | [60] |
MLPNN | PHP | Heat input and fill ratio | Overall thermal resistance | 64%/18%/18% | x | x | [57] |
MLPNN | Heat pipe solar collector | Total length/ inner diameter of heat pipe (L/di), condenser length/evaporator length (Lc/Le), water inlet temperature, collector tilt angle, and solar intensity | Water outlet temperature | 72%/28%/x | 0.9234 * | x | [56] |
MLPNN | CLPHP | Heat input and filling ratio | Thermal resistance | 70%/15%/15% | [52] | ||
MLPNN | PHP | Filling ratio, thermal conductivity of tube, inclination angle, lengths of adiabatic, condenser and evaporator sections, heat input, and inner and outer diameters | Thermal resistance | 80%/20%/x | 0.1121 ** | 0.9838 | [59] |
GA-RBFNN | 0.065 ** | 0.9946 | |||||
CHPSO ANFIS | 0.1455 ** | 0.9726 | |||||
MLPNN | Heat pipe heat exchanger | Filling ratio, nanofluid concentration, and input power | Heat exchanger efficiency | x/x/x | x | 0.99388 | [63] |
MLPNN | PHP | Kutateladze number (Ku), Bond number (Bo), Morton number (Mo), Prandtl number (Pr), Jacob number (Ja), number of turns (N), and the ratio of the evaporation section length to the diameter (Le/d) | Thermal resistance | 70%/15%/15% | 0.0138 * | 0.9824 | [24] |
MLPNN | Evacuated tube heat pipe | The radiation (I), mass (m), and ambient temperature (Tair) | Exergy | 55%/30%/15% | x | x | [67] |
RBFNN | Heat sink heat pipe | Nanofluid mass fraction, the coolant flow rate, and the heat flux of the PCB | PCB steady-state temperature | 80%/20%/x | 0.6357 ** | 0.9983 | [33] |
MLPNN | 70%/15%/15% | 0.7223 ** | 0.9978 | ||||
MLPNN | PHP | Inner diameter (Di), outer diameter (Do), evaporator length (Le), condenser length (Lc), number of turns (N), working fluids (WFs), orientation (θ), filling ratio (FR), and heat input (Q) | Thermal resistance | 70%/15%/15% | x | 0.9434 | [53] |
NARX neural network | PHP | Wall temperature measured by thermocouple T7 at evaporator | Temperature T1 at condenser | x/x/x | [55] | ||
MLPNN | Heat pipe solar collectors | Inlet temperature of the HPSC, ambient temperature, and solar radiation | Outlet temperature | 80%/x/20% | 0.00525 ** | 0.9960 | [34] |
ANFIS | x/x/x | 0.00461 ** | 0.9706 | ||||
fuzzy method | x/x/x | x | x | ||||
GMDH | PHP | Inner and outer diameters, tube thermal conductivity, turns, length of each section, heat input, filling ratio, and (sine of) inclination angle | Thermal resistance | x/x/x | 0.9779 | [35] | |
Thermal conductivity | 0.9906 | ||||||
Function chain NN (3 inputs) | OHP | Charging ratio, inclination angle, and heat input | Heat transfer rate | x/x/x | x | x | [58] |
Function chain NN (4 inputs) | Charging ratio, inclination angle, heat input, and number of turns | Heat transfer rate | x/x/x | x | x | ||
GA-ANN | Two-phase closed thermosyphon | Heat input, number of fins, and filling ratio | Thermal resistance | 80%/x/20% | x | 0.9950 | [36] |
MLPNN | Wickless heat pipe (WHP) | Input power, volume concentration of nanofluid, filling ratio and mass rate in condenser section | Thermal efficiency | 75%/25%/x | 0.00994 * (for testing dataset) | 0.9911 | [37] |
MLPNN | OHP | Heat input, thermal conductivity of working fluids, and ratio of inner diameter to the length of OHP | Thermal resistance | 70%/30%/x | 0.0025 * | 0.9966 | [38] |
ANFIS | 0.0031 * | 0.9953 | |||||
GMDH | 0.0032 * | 0.9862 | |||||
GA-MLPNN (2-layer) | PHP | Solar radiation, inlet temperature of the water tank, the evaporator length, filling ratio, and inclination angle | Gained heat | 70%/30%/x | x | x | [68] |
GA-MLPNN (3-layer) | x | x | |||||
MLPNN | Two-layer screen mesh-type cylindrical heat pipe | Heat load, size of silver nanoparticles, concentration of silver nanoparticles in water, inclination angle, average evaporator temperature, and average condenser temperature | Thermal resistance, thermal conductivity, and overall heat transfer coefficient | 70%/15%/15% | x | [39] | |
Cascade MLPNN | x | ||||||
RBFNN | x | ||||||
Generalized regression | x | ||||||
GA-MLPNN | Miniature revolving heat pipe (MRVHP) | Bo, Ja, Pr, Fr, and filling ratio | Ku (Kutateladze number) | 70%/30%/x | x | 0.9623 | [64] |
XGBoost | OHP | Ku (Kutateladze number), Ja (Jacob number), Prliq (Prandtl number), Mo (Morton number), heat flux, target evaporator temperature, and geometric parameters (Di/Le and Do/Di) | Effective heat transfer coefficient | 93%/7%/x | x | x | [65] |
MLPNN | Nanofluid-filled heat pipe | Heating power and nanofluid concentration | Thermal resistance | x/x/x | x | x | [73] |
MLPNN | OHP | Heat load, filling ratio, lengths of different sections, inner and outer diameters, and number of turns | Thermal resistance | 70%/15%/15% | 0.0045 * | 0.9946 | [40] |
GMDH | 70%/30%/x | 0.0144 * | 0.9824 | ||||
GA-MLPNN | Two-phase closed thermosyphon | Magnetic field strength, volume fraction of nanofluid in water, and inlet power | Thermal efficiency | 80%/20%/x | 0.0000315 * | 0.9800 | [54] |
Thermal resistance | 0.001 * | 0.999 | |||||
MLPNN | Two-phase closed thermosyphon | Heat input, concentration of nanofluid, and type of nanofluid | Temperature difference between evaporator and condenser | 75%/25%/x | 0.333757843 ** | 0.9999 | [61] |
Temperature difference between the input and the output water streams of condenser section (ΔT) | 0.001891019 ** | 0.9997 | |||||
ANFIS | Two-phase closed thermosyphon | Type of nanofluid, concentration of nanofluid, input power, length, and temperature difference | Thermal resistance | 70%/15%/15% | 4.175 × 10−12 * | 0.9999 | [62] |
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Olabi, A.G.; Haridy, S.; Sayed, E.T.; Radi, M.A.; Alami, A.H.; Zwayyed, F.; Salameh, T.; Abdelkareem, M.A. Implementation of Artificial Intelligence in Modeling and Control of Heat Pipes: A Review. Energies 2023, 16, 760. https://doi.org/10.3390/en16020760
Olabi AG, Haridy S, Sayed ET, Radi MA, Alami AH, Zwayyed F, Salameh T, Abdelkareem MA. Implementation of Artificial Intelligence in Modeling and Control of Heat Pipes: A Review. Energies. 2023; 16(2):760. https://doi.org/10.3390/en16020760
Chicago/Turabian StyleOlabi, Abdul Ghani, Salah Haridy, Enas Taha Sayed, Muaz Al Radi, Abdul Hai Alami, Firas Zwayyed, Tareq Salameh, and Mohammad Ali Abdelkareem. 2023. "Implementation of Artificial Intelligence in Modeling and Control of Heat Pipes: A Review" Energies 16, no. 2: 760. https://doi.org/10.3390/en16020760
APA StyleOlabi, A. G., Haridy, S., Sayed, E. T., Radi, M. A., Alami, A. H., Zwayyed, F., Salameh, T., & Abdelkareem, M. A. (2023). Implementation of Artificial Intelligence in Modeling and Control of Heat Pipes: A Review. Energies, 16(2), 760. https://doi.org/10.3390/en16020760