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21 pages, 8258 KiB  
Article
Study on the Deflagration Characteristics of Methane–Air Premixed Gas in Sudden Expansion Pipelines
by Ning Zhou, Zhuohan Shi, Xue Li, Bing Chen, Yiting Liang, Zhaoyu Li, Chunhai Yang, Xuanya Liu, Weiqiu Huang and Xiongjun Yuan
Energies 2025, 18(5), 1301; https://doi.org/10.3390/en18051301 - 6 Mar 2025
Viewed by 191
Abstract
This study employs both experimental and numerical simulation methods to systematically investigate the influence of sudden expansion diameter ratios on methane–air premixed flame propagation, explosion overpressure, and the evolution of turbulent structures. The results show that with the increase in the diameter ratio, [...] Read more.
This study employs both experimental and numerical simulation methods to systematically investigate the influence of sudden expansion diameter ratios on methane–air premixed flame propagation, explosion overpressure, and the evolution of turbulent structures. The results show that with the increase in the diameter ratio, the flame propagation velocity and explosion overpressure present a nonlinear trend of first increasing, then decreasing, and then increasing. Specifically, when the diameter ratio is 1.5, an optimal balance between turbulence enhancement and energy dissipation is achieved, and the overpressure attenuation rate is 47.61%. However, when the diameter ratio increases to 2.0, the turbulence intensity significantly escalates, the peak flame propagation speed increases by 81%, the peak explosion overpressure increases by 69%, and the overpressure attenuation efficiency decreases, which brings greater safety challenges. Moreover, when the diameter ratio is between 1.5 and 2.0, the turbulence intensity of the premixed gas explosion flow field is significantly increased, and the stable “tulip flame” propagation velocity range is extended from 16~35 m/s to 16~42 m/s. When the diameter ratio is 2.0, a distinctive four-vortex structure is formed, with strong turbulent mixing and fast energy dissipation. The vortex structure evolves with the diameter ratio, transitioning from a symmetric and stable double-vortex form to a complex multi-vortex system. The research results provide theoretical support for the prevention of explosions. Full article
(This article belongs to the Section K: State-of-the-Art Energy Related Technologies)
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<p>A schematic diagram of the experimental platform.</p>
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<p>Overpressure curve analysis under experimental conditions of 1.5 diameter ratio and 12% methane concentration.</p>
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<p>Schematic diagrams of the geometric and grid models of the experimental setup. (<b>a</b>) Schematic of the pipe setup; (<b>b</b>) Grid model.</p>
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<p>Curves of simulated and experimental overpressure with time for different grid resolutions.</p>
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<p>The evolution of the flame propagation process with time in the experiment (<b>left</b>) and simulation (<b>right</b>).</p>
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<p>A schematic diagram of the methane air premixed gas flame passing through a sudden expansion structure. (<b>I</b>) Finger-like, tulip, and distorted tulip shapes; (<b>II</b>) Shattered flame and flame fragmentation; (<b>III</b>) Backflow behavior and flame decoupling process.</p>
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<p>A schematic diagram of the sudden expansion structure of the flame of the premixed gas under different reducer ratios.</p>
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<p>Flame backflow phenomenon.</p>
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<p>Vortex structures under different expansion ratio conditions.</p>
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<p>The flame propagation process of methane–air explosion at the sudden expansion structure.</p>
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<p>Methane–air deflagration flame propagation process with different diameter reduction.</p>
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<p>Pressure variation diagram in sudden expansion pipeline at different methane concentrations.</p>
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<p>Overpressure and attenuation rate at different methane concentrations.</p>
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<p>Pressure variation diagram in sudden expansion pipeline at different diameter ratio.</p>
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<p>Overpressure and attenuation rate at different diameter ratios.</p>
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20 pages, 6698 KiB  
Article
Research on Injection Profile Interpretation Method Based on DTS Logging
by Haitao Huang, Hongwei Song, Ming Li and Xinlei Shi
Processes 2025, 13(3), 733; https://doi.org/10.3390/pr13030733 - 3 Mar 2025
Viewed by 227
Abstract
Distributed temperature sensing (DTS) has been widely used in downhole dynamic monitoring. How to analyze its data and accurately interpret the flow profile using DTS data are still great challenges. Quantitative interpretation of downhole temperature measurements requires the development of an integrated flow [...] Read more.
Distributed temperature sensing (DTS) has been widely used in downhole dynamic monitoring. How to analyze its data and accurately interpret the flow profile using DTS data are still great challenges. Quantitative interpretation of downhole temperature measurements requires the development of an integrated flow and thermal model capable of handling multi-phase flow. The model must strike a balance between computational efficiency and achieving the highest possible accuracy. The finite difference method can solve the relevant problems well. The flow model and thermal model of reservoirs and wellbores are established. Combined with the single-phase flow theory, the coupling prediction model of wellbore and reservoir temperature is established through appropriate boundary and constraint conditions. The problem was solved iteratively using the finite difference method, and the coupled temperature prediction model’s reliability was confirmed through comparison with numerical simulation results. Based on the forward model, the sensitivity analysis of the influencing factors is carried out in this study which provides a theoretical basis for the inversion model. Taking the flow rate as the inversion parameter, the injection profile interpretation model based on DTS logging data is constructed. Four optimization methods are used in the inversion model which can balance the computational efficiency and model accuracy. The DTS data are preprocessed by the Kalman filter, and the inversion and interpretation evaluation of X injection well is carried out by the LSO-MCMC combined optimization algorithm. The results show that the method has high reliability in the interpretation accuracy of injection profile, and the inverted flow profile meets practical application requirements, confirming the method’s accuracy and effectiveness. Full article
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<p>Steps for solving the coupling model of multi-phase flow well and reservoir in production wells.</p>
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<p>Reservoir fluid flow model.</p>
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<p>Reservoir fluid temperature profile. (<b>a</b>) Different fluid types; (<b>b</b>) different wellbore radii and reservoir thicknesses.</p>
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<p>Reservoir fluid temperature profile. (<b>a</b>) Different oil–water ratios; (<b>b</b>) different gas–water ratios.</p>
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<p>Numerical simulation and finite difference calculation of well temperature curve (where (<b>a</b>,<b>c</b>) are finite difference calculation results; (<b>b</b>,<b>d</b>) are numerical simulation results).</p>
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<p>Numerical simulation and finite difference calculation of well temperature curve (where (<b>a</b>,<b>c</b>) are finite difference calculation results; (<b>b</b>,<b>d</b>) are numerical simulation results).</p>
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<p>Temperature curves of wellbore with different injection flow rates. (<b>a</b>) The injection temperature is 20 °C; (<b>b</b>) the injection temperature is 50 °C.</p>
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<p>Temperature curves of wellbore with different injection temperature. (<b>a</b>) The injection temperatures are 5 °C, 15 °C, 25 °C; (<b>b</b>) the injection temperatures are 40 °C, 45 °C, 50 °C, 55 °C.</p>
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<p>Flowchart of LSO.</p>
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<p>Invert well temperature curve. (<b>a</b>) Is the MCMC algorithm; (<b>b</b>) is the L-M algorithm.</p>
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<p>LSO-MCMC algorithm inversion interpretation process.</p>
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<p>Inversion of well temperature curve: (<b>a</b>) Is the MCMC algorithm; (<b>b</b>) is the LSO-MCMC algorithm.</p>
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<p>DTS logging data wavelet transform filtering: (<b>a</b>) is before filtering; (<b>b</b>) is after filtering.</p>
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<p>Flow chart of Kalman filtering.</p>
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<p>DTS logging data Kalman filtering: (<b>a</b>) is before filtering; (<b>b</b>) is after filtering.</p>
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<p>DTS inversion interpretation result chart of X well.</p>
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17 pages, 410 KiB  
Article
Pre-Design Selection of the Rated Power of a Heaving Point Absorber Wave Energy Converter
by Guilherme Moura Paredes, Alexandra Tokat and Torbjörn Thiringer
Oceans 2025, 6(1), 13; https://doi.org/10.3390/oceans6010013 - 3 Mar 2025
Viewed by 101
Abstract
Wave energy converters (WECs) have significant potential for renewable energy generation, but early-stage design processes often require lengthy simulations. This study focuses on the pre-design selection of the rated power for a heaving point-absorber WEC. Addressing the gap in simplified methodologies, this study [...] Read more.
Wave energy converters (WECs) have significant potential for renewable energy generation, but early-stage design processes often require lengthy simulations. This study focuses on the pre-design selection of the rated power for a heaving point-absorber WEC. Addressing the gap in simplified methodologies, this study evaluates the wave energy resource, selects operational sea-states, and assesses device performance using time-domain simulations and linear potential flow theory. The results revealed that a WEC rated at 87% below peak power can capture 91% of the total available energy, achieving a balance between energy efficiency and cost-effectiveness. Furthermore, a simplified method to estimate rated power based on a constant ratio between mean and RMS power is proposed, offering significant potential for early-stage design applications. Future work should validate this approach across diverse WEC types and wave climates. Full article
(This article belongs to the Topic Control and Optimisation for Offshore Renewable Energy)
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<p>Set-up of the wave energy converter.</p>
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<p>Percentage of energy loss dependent on the peak power curtailment.</p>
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<p>Instantaneous and average power for curtailed peak power for <math display="inline"><semantics> <mrow> <msub> <mi>H</mi> <mi mathvariant="normal">s</mi> </msub> <mo>=</mo> <mn>3.25</mn> <mo> </mo> <mi mathvariant="normal">m</mi> </mrow> </semantics></math> and <math display="inline"><semantics> <mrow> <msub> <mi>T</mi> <mi mathvariant="normal">z</mi> </msub> <mo>=</mo> <mn>8.25</mn> <mo> </mo> <mi mathvariant="normal">m</mi> </mrow> </semantics></math>.</p>
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22 pages, 2571 KiB  
Article
Numerical Analysis of Steady-State Multi-Field Coupling in Electro-Fused Magnesia Furnace
by Cunjian Weng, Zhen Wang, Xianping Luo and Hui Li
Materials 2025, 18(5), 1049; https://doi.org/10.3390/ma18051049 - 27 Feb 2025
Viewed by 237
Abstract
The internal conditions of the high-temperature molten pool in an electro-fused magnesia furnace (EFMF) are difficult to measure, and the temperature distribution–energy conservation relationship in the EFMF cannot be effectively evaluated. Assuming that the feeding speed is constant, the heat absorbed by the [...] Read more.
The internal conditions of the high-temperature molten pool in an electro-fused magnesia furnace (EFMF) are difficult to measure, and the temperature distribution–energy conservation relationship in the EFMF cannot be effectively evaluated. Assuming that the feeding speed is constant, the heat absorbed by the newly added raw materials is equal to the rated power minus the heating power required to maintain thermal balance. Therefore, the EFMF can be approximately described by a steady-state model. In order to analyze the state of the molten pool of EFMF at different smelting stages, this study first constructed a three-dimensional steady-state multi-physics field numerical simulation model. The calculations show that the equivalent resistance of the molten pool varies approximately between 1 mΩ and 0.4 mΩ. Furthermore, the equivalent reactance produced by the whole conductive circuit is almost of the same order as the resistance. The Reynolds number of the convection inside the molten pool exceeds 105, which means that the flow inside the molten pool is forced convection dominated by the Lorentz force. Moreover, the turbulence makes the temperature uniformity of the molten pool (the temperature gradient near the solid–liquid interface is approximately within 300 K/m) far greater than that of the unmelted raw materials with very low thermal conductivity (the average temperature gradient reaches over 1000 K/m); the respective proportions of arc power and Joule heating power can be predicted by the model. When the molten pool size is small, the proportion of Joule heating power is high, reaching about 20% of the rated power (3700 kVA); as the molten pool size increases, the convection effect is relatively weakened, and the proportion of Joule heating power also decreases accordingly, only 5% to 10%; the model prediction and experimental estimation results are in good agreement, which makes it feasible to conduct a quantitative analysis of the power distribution in different smelting stages. Full article
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<p>Schematic diagram of EFMF: The figure illustrates the basic components of the EFMF system, including the power supply, electrode lifting system, electrodes, and furnace body. It highlights the fundamental operation process and the molten pool’s state, providing a clear overview of the system’s layout and functionality.</p>
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<p>The flowchart of a multi-physics simulation process for the EFMF: The flowchart outlines the multi-physics simulation process for the EFMF, highlighting the sequential steps to achieve a steady state. It streamlines the simulation setup, ensuring accurate and efficient convergence to steady-state conditions.</p>
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<p>Schematic diagram of calculation domain and boundary conditions for the EFMF (electro-fused magnesia furnace): The diagram illustrates the computational domain and boundary conditions for the electromagnetic field, providing a clear overview of the setup and facilitating accurate simulation.</p>
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<p>The top view and front view of the 1/6 simplified model: The figure shows the top and front views of the 1/6 simplified model, highlighting its symmetrical configuration. This visualization illustrates how the temperature and flow field calculations are simplified using the symmetrical 1/6 model, enhancing computational efficiency.</p>
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<p>Mesh sensitivity analysis and the location of the corresponding sampling points: Mesh sensitivity analysis shows that the electric field distribution stabilizes when the grid number exceeds 20,000. The analysis determines the appropriate mesh number and thus prevents the unnecessary consumption of excessive computational resources.</p>
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<p>Equivalent circuit diagram of molten pool and the electrodes: (<b>a</b>) star-connected load; (<b>b</b>) an equivalent single-phase circuit. In a three-phase balanced state, the molten pool and electrodes are simplified as a star-connected load and represented by an equivalent single-phase circuit. This diagram simplifies the understanding of key electrical concepts (voltage, current, power) for the molten pool and electrodes, facilitating discussions in subsequent sections.</p>
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<p>Variation in phase voltage <math display="inline"><semantics> <msub> <mi>U</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> and <math display="inline"><semantics> <mrow> <msub> <mi>P</mi> <mrow> <mi mathvariant="normal">m</mi> <mi mathvariant="normal">e</mi> <mi mathvariant="normal">l</mi> <mi mathvariant="normal">t</mi> </mrow> </msub> <mo>/</mo> <msub> <mi>P</mi> <mi mathvariant="normal">t</mi> </msub> </mrow> </semantics></math> with phase current <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math>: The figure shows the linear relationship between phase voltage <math display="inline"><semantics> <msub> <mi>U</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> and phase current <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math>, and indicates that the proportion of Joule heating power (<math display="inline"><semantics> <msub> <mi>P</mi> <mrow> <mi mathvariant="normal">m</mi> <mi mathvariant="normal">e</mi> <mi mathvariant="normal">l</mi> <mi mathvariant="normal">t</mi> </mrow> </msub> </semantics></math>) in the total power (<math display="inline"><semantics> <msub> <mi>P</mi> <mi mathvariant="normal">t</mi> </msub> </semantics></math>) is relatively small. This data highlight the importance of simulation and modeling for optimizing the smelting process, as critical parameters like voltage drop and absorbed Joule heating power are typically not directly measurable during operation.</p>
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<p>Analysis of electromagnetic field calculation results when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 14,000 A: (<b>a</b>) the electric field (V); (<b>b</b>) the magnetic field (T) in logarithmic coordinate system; (<b>c</b>) the Lorentz force density distributions (N/m<sup>3</sup>) in logarithmic coordinate system. The results show the electric field distribution, magnetic field distribution, and Lorentz force density under a constant current of 14,000 A, highlighting their dependence on molten pool size and current density. The above findings indicate that the Lorentz force is the primary driving force for melt convection, causing the turbulence phenomena discussed later.</p>
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<p>Shape of a MgO ingot (about 4 tons): The solidified MgO ingot has a pear-like shape, wider at the base and tapering towards the top. Although the molten pool in the smelting experiment cannot be directly measured, the smelting process can be inferred from the shape and structure of the solidified MgO ingot.</p>
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<p>Simulation results of small-scale pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 10,000 A: (<b>a</b>) temperature field of the 1/6 model (K); (<b>b</b>) temperature field of the pool (K); (<b>c</b>) flow field of the pool (m/s). The simulation results show steady-state temperature and flow fields in the EFMF system and the small-scale molten pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 10,000 A, highlighting the steady-state conditions achieved under this current.</p>
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<p>Simulation results of medium-scale pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 14,000 A: (<b>a</b>) temperature field of the 1/6 model (K); (<b>b</b>) temperature field of the pool (K); (<b>c</b>) flow field of the pool (m/s). The simulation results show steady-state temperature and flow fields in the EFMF system and the medium-scale molten pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 14,000 A, highlighting the steady-state conditions achieved under this current.</p>
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<p>Simulation results of large-scale pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 14,000 A: (<b>a</b>) temperature field of the 1/6 model (K); (<b>b</b>) temperature field of the pool (K); (<b>c</b>) flow field of the pool (m/s). The simulation results show steady-state temperature and flow fields in the EFMF system and the large-scale molten pool when <math display="inline"><semantics> <msub> <mi>I</mi> <mi mathvariant="normal">A</mi> </msub> </semantics></math> = 14,000 A, highlighting the steady-state conditions achieved under this current.</p>
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<p>Variation in heating power (<math display="inline"><semantics> <msub> <mi>P</mi> <mrow> <mi mathvariant="normal">h</mi> <mi mathvariant="normal">e</mi> <mi mathvariant="normal">a</mi> <mi mathvariant="normal">t</mi> <mi mathvariant="normal">i</mi> <mi mathvariant="normal">n</mi> <mi mathvariant="normal">g</mi> </mrow> </msub> </semantics></math>) with the volume of the molten pool: The total heating power required for different molten pool volumes (0.45 <math display="inline"><semantics> <msup> <mi mathvariant="normal">m</mi> <mn>3</mn> </msup> </semantics></math>, 1.45 <math display="inline"><semantics> <msup> <mi mathvariant="normal">m</mi> <mn>3</mn> </msup> </semantics></math>, and 2.9 <math display="inline"><semantics> <msup> <mi mathvariant="normal">m</mi> <mn>3</mn> </msup> </semantics></math>) closely matches experimentally estimated values. The agreement between experimental and model-calculated power highlights the model’s accuracy. This suggests that maintaining thermal balance with minimal power input after smelting can aid impurity removal and crystal growth.</p>
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19 pages, 8356 KiB  
Article
Study on Ecological Water Replenishment Calculation and Intelligent Pump Station Scheduling for Non-Perennial Rivers
by Zuohuai Tang, Junying Chu, Zuhao Zhou, Yunfu Zhang, Tianhong Zhou, Kangqi Yuan, Mingyue Ma and Ying Wang
Sustainability 2025, 17(5), 2032; https://doi.org/10.3390/su17052032 - 26 Feb 2025
Viewed by 283
Abstract
The Haidian District was, historically, rich in water resources. However, with urban development, the groundwater levels have declined, and most rivers have lost their ecological baseflows. To restore the aquatic ecosystems, the district has implemented a cyclic water network and advanced water replenishment [...] Read more.
The Haidian District was, historically, rich in water resources. However, with urban development, the groundwater levels have declined, and most rivers have lost their ecological baseflows. To restore the aquatic ecosystems, the district has implemented a cyclic water network and advanced water replenishment projects. Nonetheless, the existing replenishment strategies face challenges, such as an insufficient scientific basis, lack of data, and high energy consumption. There is an urgent need to develop a scientifically robust ecological water replenishment system and optimize pump station scheduling to enhance water resource management efficiency. This study addresses the ecological water replenishment needs of seasonal rivers by integrating the Literature method, Rainfall-Runoff method, and R2cross method to develop a comprehensive approach for calculating the ecological flow and water depth. The proposed method simultaneously meets the ecological functionality and landscape requirements of seasonal rivers. Additionally, the SWMM model is employed to design intelligent pump station scheduling rules, optimizing the replenishment efficiency and energy consumption. Through field measurements and data collection, the ecological water demands of the river channels in different areas are assessed. Using a hydrodynamic model, the dynamic variations in the ecological flow and water depth are simulated. For the Cuihu, Daoxianghu, and Yongfeng areas, this study reveals that the current replenishment volume is insufficient to meet the landscape and ecological needs of the rivers. Most rivers require a 20–30% increase in water levels, with the Dazhai qu needing a substantial rise from 0.17 m to 0.3 m, representing an increase of 76%. Additionally, the results demonstrate that intelligent pump station scheduling can significantly reduce operating costs and energy consumption by dynamically adjusting the replenishment timing and flow rates. This approach optimizes the intervals between equipment activation and deactivation, thereby balancing ecological and energy-saving goals. This research not only provides technical support for the precise calculation of ecological replenishment volumes and the intelligent management of pump stations, but also offers scientific references for water resource management in similar regions. The findings will enhance the ecological functions and landscape quality of the rivers in the Haidian District while promoting refined and intelligent regional water resource management. Moreover, this study presents innovative solutions and theoretical foundations for water resource regulation under the backdrop of climate change. Full article
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<p>Distribution of ecological water replenishment areas and replenishment pipelines in Haidian District.</p>
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<p>Flowchart for determining ecological flow based on the Rainfall-Runoff method.</p>
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<p>Conceptual diagram of the Daxianghu area model.</p>
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<p>Fitting of water level monitoring points at (<b>a</b>) Zhoujiaxianggou and (<b>b</b>) Dazhaiqu.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Cuihu area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Daoxianghu area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Daoxianghu area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Yongfeng area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Yuquanshan area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Yuanmingyuan area.</p>
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<p>Comparison of pump station flow, channel flow (<b>up</b>), and water level (<b>down</b>) in the Yuanmingyuan area.</p>
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27 pages, 17481 KiB  
Article
Enhancing Lane Change Safety and Efficiency in Autonomous Driving Through Improved Reinforcement Learning for Highway Decision-Making
by Zi Wang, Mingzuo Jiang, Shaoqiang Gu, Yunyang Gu and Jiaxia Wang
Electronics 2025, 14(5), 918; https://doi.org/10.3390/electronics14050918 - 25 Feb 2025
Viewed by 286
Abstract
Autonomous driving (AD) significantly reduces road accidents, providing safer transportation while optimizing traffic flow for greater efficiency and smoothness. However, ensuring safe decision-making in dynamic and complex highway environments, especially during lane-changing maneuvers, remains a challenge. Reinforcement Learning (RL) has become a promising [...] Read more.
Autonomous driving (AD) significantly reduces road accidents, providing safer transportation while optimizing traffic flow for greater efficiency and smoothness. However, ensuring safe decision-making in dynamic and complex highway environments, especially during lane-changing maneuvers, remains a challenge. Reinforcement Learning (RL) has become a promising method for developing decision-making systems in AD, particularly Deep Reinforcement Learning (DRL). In this study, we focus on highway lane-change behaviors and propose a novel DRL algorithm, called Huber-regularized Reward-threshold Adaptive Double Deep Q-Network (HRA-DDQN). First, a reward function optimally balances speed, safety, and the necessity of lane changes, ensuring efficient and safe maneuvering in highway scenarios. Second, the dynamic target network update strategy triggered by reward difference is introduced into HRA-DDQN, which enhances the model’s adaptability to varying traffic conditions. Finally, a hybrid loss function, combining Huber loss with L2 regularization, is implemented in HRA-DDQN to improve robustness against outliers and mitigate overfitting. Simulation results demonstrate that the proposed decision framework significantly enhances both driving efficiency and safety, outperforming other methods by yielding higher rewards, lower collision rates, and more stable lane-changing decisions. Full article
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<p>RL framework.</p>
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<p>The structure of DQN.</p>
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<p>The framework of Dueling DQN.</p>
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<p>The framework of DDQN.</p>
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<p>The HRA-DDQN input and output of the framework.</p>
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<p>Highway driving scenario for a decision-making task involving four lanes.</p>
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<p>Training curves of different performance indices. (<b>a</b>) The average reward values during the training process of the three methods. (<b>b</b>) The average number of steps during the training process of the three methods. (<b>c</b>) The average speed during the training process of the three methods. (<b>d</b>) The average action change frequency during the training process of the three methods.</p>
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<p>Comparison of lane changes for three methods.</p>
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<p>Average number of lane changes in the three methods.</p>
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<p>Control actions in one episode of three methods.</p>
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<p>Comparison of Q-value error trends during the training process.</p>
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<p>Performance evaluation of three methods using paired <span class="html-italic">t</span>-test. (<b>a</b>) The average reward values during the training process of the three methods. (<b>b</b>) The average number of lane changes during the training process of the three methods. (<b>c</b>) The collision rate during the training process of the three methods. The “****” marks indicate highly significant differences (<span class="html-italic">p</span> &lt; 0.0001) in the respective evaluations.</p>
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<p>Ego vehicle lane change simulation in a highway environment. (<b>a</b>) The ego vehicle is in the second lane of a four-lane highway. (<b>b</b>) The ego vehicle switches to the third lane. (<b>c</b>) The ego vehicle transitions back to the second lane without impeding the movement of surrounding vehicles. The green color represents the ego vehicle, and the blue color represents surrounding vehicles.</p>
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<p>Ego vehicle lane change simulation in a highway environment. (<b>a</b>) The ego vehicle is in the second lane of a four-lane highway. (<b>b</b>) The ego vehicle switches to the third lane. (<b>c</b>) The ego vehicle transitions back to the second lane without impeding the movement of surrounding vehicles. The green color represents the ego vehicle, and the blue color represents surrounding vehicles.</p>
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<p>Comparison of collision counts of the three methods.</p>
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<p>Collision conditions of the ego vehicle in each compared method.</p>
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<p>Number of collisions for different numbers of traffic vehicles after training.</p>
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<p>Effect of removing key Innovation points on collision counts.</p>
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16 pages, 5727 KiB  
Article
Numerical Analysis of Influence Mechanism of Orifice Eccentricity on Silo Discharge Rate
by Yinglong Wang, Yanlong Han, Anqi Li, Hao Li, Haonan Gao, Ze Sun, Shouyu Ji, Zhuozhuang Li and Fuguo Jia
Agriculture 2025, 15(5), 490; https://doi.org/10.3390/agriculture15050490 - 25 Feb 2025
Viewed by 209
Abstract
Eccentric silo is an extremely common type of silo, but it is still unclear how to accurately control the discharge by adjusting eccentric orifices, limiting the application and development of eccentric silo. In this study, the rice particle discharging process on silos with [...] Read more.
Eccentric silo is an extremely common type of silo, but it is still unclear how to accurately control the discharge by adjusting eccentric orifices, limiting the application and development of eccentric silo. In this study, the rice particle discharging process on silos with different eccentricities was simulated by the discrete element method (DEM), and the influence mechanism of orifice eccentricity on silo discharge rate was analyzed. The results show that eccentricity has a direct influence on the particle volume fraction and vertical velocity that determine the discharge rate of the silo. In fully eccentric silo, it is not easy for particle flow to achieve balance, particles will pass through outlet with more kinetic energy. Moreover, continuous force network cannot be formed between particles with shear resistance, resulting in weak interlocking action between particles. The orientation of particle in fully eccentric silo is more vertical, especially near the silo wall, which will produce larger local particle volume fraction above the orifice. When the eccentricity exceeds the critical eccentricity, the sparse flow area on the discharge orifice becomes larger, and the particle acceleration area increases accordingly. Research findings may offer valuable insights for the accurate control of discharge rate of eccentric silo, as well as for optimizing silo design. Full article
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<p>The rice particle modeling process: (<b>a</b>) photo of rice grains, (<b>b</b>) ellipsoid model of rice, and (<b>c</b>) 3D rice particle model in simulation.</p>
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<p>Silo modeling process: (<b>a</b>) the three-dimensional schematic diagram of eccentric silo and (<b>b</b>) the division of silo-monitoring area.</p>
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<p>Schematic diagram of self-built silo-unloading platform.</p>
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<p>Schematic diagram of rice particle flow pattern in silo during discharging process in simulation and experiment.</p>
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<p>Experimental and simulation comparison of particle discharge rate change under different orifice eccentricity.</p>
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<p>The volume fraction of particles at the discharge orifice of each eccentric silo.</p>
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<p>Vertical velocity distribution of particles at discharge orifices of different eccentric silos.</p>
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<p>The movement trajectories of particle in the steady state of flow: (<b>a</b>) concentric silo and (<b>b</b>) fully eccentric silo.</p>
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<p>The normal contact force network in concentric silo and fully eccentric silo at the same moment.</p>
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<p>Schematic diagram for determining orientation angle of long axis of rice grains.</p>
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<p>Changes trend of rice orientation angles at different heights above the orifice: (<b>a</b>) concentric silo and (<b>b</b>) fully eccentric silo.</p>
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<p>Shear rate nephogram in silos with different eccentricities (<span class="html-italic">e</span>): (<b>a</b>) 0; (<b>b</b>) 0.1; (<b>c</b>) 0.2; (<b>d</b>) 0.5; (<b>e</b>) 0.7; (<b>f</b>) 0.8; (<b>g</b>) 0.84; (<b>h</b>) 0.85; and (<b>i</b>) 0.857.</p>
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<p>Particle coordination number nephogram in silos with different eccentricities (<span class="html-italic">e</span>): (<b>a</b>) 0; (<b>b</b>) 0.1; (<b>c</b>) 0.2; (<b>d</b>) 0.5; (<b>e</b>) 0.7; (<b>f</b>) 0.8; (<b>g</b>) 0.84; (<b>h</b>) 0.85; and (<b>i</b>) 0.857.</p>
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11 pages, 2802 KiB  
Article
A Study on the Water Consumption Characteristics of Fraxinus pennsylvanica Marshall During the Growing and Non-Growing Seasons and Their Response to Microclimate Variables
by Yuehao Han, Yu Su, Fude Liu, Yan Zhang and Hailong Wu
Forests 2025, 16(3), 401; https://doi.org/10.3390/f16030401 - 24 Feb 2025
Viewed by 120
Abstract
Plant water use can have a profound impact on the regional water cycle and water balance. A great deal of research has been conducted in this area in recent years. However, plant nighttime sap flow and non-growing season water use have rarely been [...] Read more.
Plant water use can have a profound impact on the regional water cycle and water balance. A great deal of research has been conducted in this area in recent years. However, plant nighttime sap flow and non-growing season water use have rarely been addressed. These two components should not be neglected in accurately predicting the water use of urban landscape trees and large-scale plantation forests. In this study, the thermal diffusion probe (TDP) method was used to observe the water use of Fraxinus pennsylvanica Marshall, a common tree species in northern China. Continuous observations of sap flow were made from November 2020 to September 2021, while meteorological conditions in the region were recorded. We analyzed the sap flow changes in different months and their responses to environmental factors at the daily scale. The results showed a clear circadian rhythm phenomenon of sap flow during the growing season, with strong correlations between nighttime sap flow and daytime sap flow, as well as environmental factors. Transpiration and refilling stem water storage were also observed at night. In the non-growing season, the average whole day sap flow rate is less than 0.5 cm/h. The difference in average sap flow rate between daytime and nighttime is less than 0.3 cm/h. At the daily scale, temperature (Ta), relative humidity (RH), and vapor pressure deficit (VPD) were the main influences on nighttime sap flow. Solar radiation had a significant effect on the overall water use strategy of the trees. Full article
(This article belongs to the Section Forest Hydrology)
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<p>Sap flow velocity at different scales. (<b>A</b>,<b>C</b>) are the changes in daily sap flow velocity during the growing season and non-growing season, respectively. (<b>B</b>,<b>D</b>) are the average sap flow velocity during the whole day, daytime, and nighttime in different months, respectively. Please refer to <a href="#forests-16-00401-t0A1" class="html-table">Table A1</a> in the <a href="#app1-forests-16-00401" class="html-app">Appendix A</a> for specific data.</p>
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<p>Variation in meteorological factors by month. Rs: solar radiation; P: atmospheric pressure. Ta: temperature; Td: temperature dew point difference. RH: relative humidity; VPD: vapor pressure deficit.</p>
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<p>Daytime and nighttime water consumption. The bars indicate the water consumption corresponding to the left axis. The folded part shows the proportion of different periods corresponding to the right axis.</p>
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21 pages, 16169 KiB  
Article
Study on Flow and Settlement Performance Evaluation and Optimization of Coal Gangue Slurry Filling Material Based on Fractal Gradation
by Xiaoping Shao, Wei Wang, Bingchao Zhao, Jianbo Ning, Zhengchun Wang, Yibo Zhang, Xing Du and Renlong Tang
Appl. Sci. 2025, 15(5), 2405; https://doi.org/10.3390/app15052405 - 24 Feb 2025
Viewed by 139
Abstract
Coal gangue slurry filling technology is an effective way of utilizing coal gangue solid waste resources rationally, and its fluidity and sedimentation behavior have an essential influence on filling performance. However, evaluation and optimization methods for the fluidity and sedimentation performance of coal [...] Read more.
Coal gangue slurry filling technology is an effective way of utilizing coal gangue solid waste resources rationally, and its fluidity and sedimentation behavior have an essential influence on filling performance. However, evaluation and optimization methods for the fluidity and sedimentation performance of coal gangue slurry filling materials (CSFMs) are still scarce. In order to solve this problem, based on the fractal grading theory, this paper carried out an experimental study on the influence of the fractal dimension on the flow characteristics of CSFMs, revealed the impact of the fractal dimension on the flow performance of slurry, and constructed a CSFM flow performance evaluation and optimization model based on the fractal dimension. At the same time, the influence of the fractal dimension on solid mass fraction and particle distribution in the CSFM sedimentation process was analyzed using a sedimentation experiment. Combined with fitting analysis and model construction, a CSFM sedimentation performance evaluation method based on fractal dimension D was proposed. The results show that (1) the slump, expansion, and yield stress of CSFMs increased first and then decreased with the increase in the fractal dimension, and the bleeding rate of CSFMs decreased with the rise in the fractal dimension. The analysis of the consistency coefficient of CSFMs shows that the increase in the proportion of fine particles will increase the consistency coefficient. (2) The fitting analysis indicates that the fractal dimension D of CSFMs is negatively correlated with the sedimentation performance PS. The change in D is most significant in the range of 2.3 to 2.4, where the slurry’s stability is poor. When D exceeds 2.5, the slurry’s stability improves significantly. (3) Based on the evaluation of flow performance and settlement performance, the flow performance and settlement performance of CSFMs with fractal dimensions between 2.50 and 2.59 achieve the best balance, which ensures the reliability of long-distance transportation and construction quality. The research results can provide a reference for the pipeline transportation of whole gangue slurry and have important practical significance for realizing the large-scale disposal of gangue solid waste and green mining of coal mines. Full article
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<p>Material characteristics of gangue. (<b>a</b>) Gangue XRD pattern; (<b>b</b>) SEM image of gangue.</p>
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<p>Accumulative pass rate of gangue.</p>
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<p>Flow chart of the experiment.</p>
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<p>Schematic diagram of the settlement instrument.</p>
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<p>Effect of the fractal dimension on the slump, expansion, and bleeding rate of slurry.</p>
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<p>Relationship between shear rate and shear force.</p>
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<p>Relationship between shear rate and viscosity.</p>
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<p>Evaluation model of flow performance.</p>
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<p>Calculation of the flow characteristic evaluation model.</p>
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<p>The sinking force of single-particle gangue in static slurry.</p>
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<p>Particle distribution diagram during the process of slurry settlement.</p>
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<p>The change in the slurry solid mass fraction in the process of sedimentation. (<b>a</b>) The upper part of the settlement instrument; (<b>b</b>) The middle of the settlement instrument; (<b>c</b>) the Lower part of the settlement instrument.</p>
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<p>Variation of the fractal dimension ds of particle size distribution in slurry during the sedimentation process. (<b>a</b>) The upper part of the settlement instrument; (<b>b</b>) The middle of the settlement instrument; (<b>c</b>) the Lower part of the settlement instrument.</p>
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<p>Fitting analysis of the fractal dimension on settlement performance.</p>
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<p>Relationship between the fractal dimension and settlement performance.</p>
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<p>The relationship between the fractal dimension and flow and settlement performance.</p>
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27 pages, 14341 KiB  
Article
Investigation on Thermal Performance of a Battery Pack Cooled by Refrigerant R134a in Ribbed Cooling Channels
by Tieyu Gao, Jiadian Wang, Haonan Sha, Hao Yang, Chenguang Lai, Xiaojin Fu, Guangtao Zhai and Junxiong Zeng
Energies 2025, 18(4), 1011; https://doi.org/10.3390/en18041011 - 19 Feb 2025
Viewed by 266
Abstract
This study numerically investigates the thermal performance of a refrigerant-based battery thermal management system (BTMS) under various operating conditions. A validated numerical model is used to examine the effects of cooling channel rib configurations (rib spacing and rib angles) and refrigerant parameters (mass [...] Read more.
This study numerically investigates the thermal performance of a refrigerant-based battery thermal management system (BTMS) under various operating conditions. A validated numerical model is used to examine the effects of cooling channel rib configurations (rib spacing and rib angles) and refrigerant parameters (mass flow rate and saturation temperature) on battery thermal behavior. Additionally, the impact of discharge C-rates is analyzed. The results show that a rib spacing of 11 mm and a rib angle of 60° reduce the maximum battery temperature by 0.8 °C (cooling rate of 2%) and improve temperature uniformity, though at the cost of a 130% increase in pressure drop. Increasing the refrigerant mass flow rate lowers the maximum temperature by up to 10%, but its effect on temperature uniformity diminishes beyond 20 kg/h. A lower saturation temperature enhances cooling but increases internal temperature gradients, while a higher saturation temperature improves uniformity at the expense of a slightly higher maximum temperature. Under high discharge rates (12C), the system’s cooling capacity becomes limited, leading to significant temperature rises. These findings provide insights that can aid in optimizing BTMS design to balance cooling performance, energy efficiency, and temperature uniformity. Full article
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<p>Schematic diagram of (<b>a</b>) battery pack structure, (<b>b</b>) cooling plate, (<b>c</b>) rib arrangement, and (<b>d</b>) rib spacing and angle.</p>
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<p>Battery performance characteristics: (<b>a</b>) open circuit voltage as a function of SOC, and (<b>b</b>) internal resistance variation with SOC at different environmental temperatures.</p>
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<p>Time-dependent heat generation rate during battery discharge.</p>
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<p>Time step independence test.</p>
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<p>Grid independence test.</p>
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<p>Comparison of experiment and simulation results for maximum temperatures of cell, heater film, and cold plate.</p>
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<p>Influence of different rib spacings on heat transfer performance (rib angle = 90°).</p>
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<p>Temperature contour plots of the battery cross-section for different rib spacings (rib angle = 90°).</p>
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<p>Temperature contour plots of the battery module for different rib spacings (rib angle = 90°).</p>
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<p>Cross-sectional velocity distribution contour plots for different rib spacings (rib angle = 90°).</p>
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<p>Influence of different rib angles on heat transfer performance.</p>
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<p>Temperature contour plots of the battery cross-section for different rib angles (rib space = 11 mm).</p>
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<p>Temperature contour plots of the battery module for different rib angles (rib space = 11 mm).</p>
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<p>Cross-sectional velocity distribution contour plots for different rib angles (rib space = 11 mm).</p>
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<p>Battery thermal response to C-rate discharge conditions: (<b>a</b>) extreme temperature values, and (<b>b</b>) spatial temperature variation.</p>
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<p>Temperature contour plots of the battery cross-section for different discharge C-rates.</p>
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<p>Pressure Loss Characteristics Under Different Discharge C-Rates.</p>
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<p>Variation of temperature extremes with refrigerant mass flow rates: (<b>a</b>) maximum temperature, and (<b>b</b>) minimum temperature.</p>
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<p>(<b>a</b>) Variation in temperature difference, and (<b>b</b>) variation in pressure loss under different refrigerant mass flow rates.</p>
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<p>Temperature contour plots of the battery cross-section for different refrigerant mass flow rates.</p>
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<p>Variation of temperature extremes with refrigerant saturation temperatures: (<b>a</b>) maximum temperature, and (<b>b</b>) minimum temperature.</p>
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<p>(<b>a</b>) Variation in temperature difference, and (<b>b</b>) variation in pressure loss under different refrigerant saturation temperatures.</p>
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<p>Temperature contour plots of the battery cross-section for different refrigerant saturation temperatures.</p>
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17 pages, 4237 KiB  
Article
Prediction of Mine Waste Rock Drainage Quantity Using a Machine Learning Model with Physical Constraints
by Can Zhang, Liang Ma and Wenying Liu
Minerals 2025, 15(2), 194; https://doi.org/10.3390/min15020194 - 19 Feb 2025
Viewed by 216
Abstract
Mining activities generate substantial amounts of waste rock, which are often disposed of in waste rock piles. Drainage from these piles can pose serious environmental risks. It is crucial to reliably predict drainage properties in order to effectively manage them. In previous work, [...] Read more.
Mining activities generate substantial amounts of waste rock, which are often disposed of in waste rock piles. Drainage from these piles can pose serious environmental risks. It is crucial to reliably predict drainage properties in order to effectively manage them. In previous work, we developed a machine learning model to predict waste rock drainage quantity using weather monitoring data as the input and drainage flow rate as the output. However, this model lacked physical constraints, limiting its interpretability, reliability, and applicability. In this study, we introduced a new machine learning model designed with physical constraints to improve the predictions of drainage quantity. This new model incorporates a weather refining sub-model and integrates physical constraints to enhance the overall reliability of the model predictions. The weather refining sub-model transforms primary weather features (total precipitation and temperature) into secondary features (rainfall, snowmelt, and evaporation) through established mathematical relationships. These secondary features were then used as inputs for the machine learning model to predict drainage quantity. To embed physical principles within the machine learning model, we integrated a water balance equation into the neural network architecture and modified the loss function accordingly. In addition, we included an adjustable bias term to optimize the balance between model performance and interpretability. Compared with our previous model, the incorporation of physical constraints into the machine learning model improved the accuracy of the drainage quantity predictions. More importantly, this approach ensures that the model outputs adhere to physical laws, thereby enhancing its interpretability, reliability, and applicability. Full article
(This article belongs to the Section Environmental Mineralogy and Biogeochemistry)
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<p>A schematic of methodology developed in the present study for simulating waste rock drainage quantity.</p>
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<p>A schematic of the neural network structure design for the drainage quantity model.</p>
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<p>Comparison of model outputs and measured drainage flow rates during model training and testing for (<b>a</b>) Station 1; (<b>b</b>) Station 2; and (<b>c</b>) Station 3.</p>
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<p>Comparison of model outputs and measured drainage flow rates during model training and testing for (<b>a</b>) Station 1; (<b>b</b>) Station 2; and (<b>c</b>) Station 3.</p>
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<p>The monthly contribution of the bias term to the drainage quantity prediction for the three drainage monitoring stations studied.</p>
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<p>Comparison of the sensitivity test results (one involving increasing the temperature and the other involving increasing the total precipitation) with the original predictions of the test sets for (<b>a</b>) Station 1; (<b>b</b>) Station 2; and (<b>c</b>) Station 3.</p>
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<p>Non-negative monotonicity means that all data points are positioned along or above the diagonal line. (<b>a</b>) Monotonicity test results for the drainage quantity model with the physical loss term in the loss function; (<b>b</b>) Monotonicity test results for the drainage quantity model without the physical loss term in the loss function.</p>
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<p>The decrease in the NSE scores of the test sets with an increasing number of lag days for the three drainage monitoring stations.</p>
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<p>Comparison of the drainage flow rates predicted by the original model, predicted by the model with three lag days, and the observed values of the test set of Station 1.</p>
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18 pages, 2461 KiB  
Article
Improvement of Mass Transfer Characteristics for the Gas-Liquid System in a Vortex Counterflow Apparatus
by Vsevolod Sklabinskyi, Ivan Pavlenko, Maksym Skydanenko, Sylwia Włodarczak, Andżelika Krupińska, Marek Ochowiak and Izabela Kruszelnicka
Energies 2025, 18(4), 984; https://doi.org/10.3390/en18040984 - 18 Feb 2025
Viewed by 206
Abstract
This article aims to increase the intensity of mass transfer between gas and liquid in counterflow gas–liquid flow, one of the key problems in designing mass transfer equipment. For this purpose, analytical and experimental studies were carried out to evaluate the main features [...] Read more.
This article aims to increase the intensity of mass transfer between gas and liquid in counterflow gas–liquid flow, one of the key problems in designing mass transfer equipment. For this purpose, analytical and experimental studies were carried out to evaluate the main features of operating processes in a vortex counterflow apparatus. In particular, the presented research substantiates the possibility of achieving several theoretical stages of concentration change in a single atomizing stage of the vortex counterflow mass transfer apparatus. The corresponding experimental stand was developed to carry out experimental studies. Afterward, the efficiency of the vortex counterflow mass transfer apparatus was evaluated. The model was based on material balance and flow rate equations, allowing for the determination of mass transfer and intensity ratio. After comparing the analytical expressions with the experimental results, the regression dependence for evaluating the main parameter of the proposed mathematical model was obtained. An increase in steam consumption led to increased steam velocities, affecting the droplets. This fact proved an increase in the intensity of mass transfer processes. The studies substantiated the achievement of several theoretical stages of concentration change and increased the efficiency of a vortex counterflow mass transfer apparatus. From a practical viewpoint, the experimental studies confirmed that when the height and radius ratio is less than 0.6–0.7, it is possible to create a plane vortex countercurrent motion of gas and liquid flows with a significant increase in peripheral gas velocities along the radius of the vortex chamber. Full article
(This article belongs to the Section K: State-of-the-Art Energy Related Technologies)
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<p>Flows in a vortex apparatus with a counterflow of phases in the contact area: (<b>a</b>) design scheme of the vortex camera; (<b>b</b>) general view of the vortex apparatus without the top cover; (<b>c</b>) velocity components; (<b>d</b>) the effect of the gas flow on a droplet; <span class="html-italic">v</span>, <span class="html-italic">w</span>—velocities of gas and droplet, respectively; <span class="html-italic">ω</span>—angular velocity, rad/s; <span class="html-italic">r</span>, <span class="html-italic">φ</span>—radial and angular directions of the local coordinate system, respectively.</p>
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<p>A design scheme of the studied counterflow mass transfer apparatus: 1—mass transfer chamber; 2—gas outlet; 3—tangential slots; 4—container for gas removal; 5—gas outlet pipe; 6—gas supply pipe; 7—gas supply chamber; 8—nozzle for liquid supply to the atomizer; 9—atomizer; 10—fluid drainage slots; 11—container for collecting liquid; 12—nozzle for draining liquid.</p>
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<p>The design scheme of the experimental stand: 1—bottom; 2—lower vortex apparatus; 3—upper vortex apparatus; 4—condenser; 5—rotameters; 6—differential pressure gauges; 7—rotameter to control reflux flow into the bottom; 8—valve for dumping reflux into the bottom; 9—valve for supplying reflux to the lower vortex apparatus; 10—valve for removing reflux from the lower vortex apparatus; 11—vapor sampling refrigerators; 12—refrigerators for sampling the liquid phase.</p>
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<p>Experimental points and theoretical line for the dependence of the number of theoretical concentration stages on steam consumption.</p>
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23 pages, 1121 KiB  
Article
Deep Reinforcement Learning-Based Routing Method for Low Earth Orbit Mega-Constellation Satellite Networks with Service Function Constraints
by Yan Chen, Huan Cao, Longhe Wang, Daojin Chen, Zifan Liu, Yiqing Zhou and Jinglin Shi
Sensors 2025, 25(4), 1232; https://doi.org/10.3390/s25041232 - 18 Feb 2025
Viewed by 276
Abstract
Low-orbit satellite communication networks have gradually become the research focus of fifth-generation (5G) beyond and sixth generation (6G) networks due to their advantages of wide coverage, large communication capacity, and low terrain influence. However, the low earth orbit mega satellite network (LEO-MSN) also [...] Read more.
Low-orbit satellite communication networks have gradually become the research focus of fifth-generation (5G) beyond and sixth generation (6G) networks due to their advantages of wide coverage, large communication capacity, and low terrain influence. However, the low earth orbit mega satellite network (LEO-MSN) also has difficulty in constructing stable traffic transmission paths, network load imbalance and congestion due to the large scale of network nodes, a highly complex topology, and uneven distribution of traffic flow in time and space. In the service-based architecture proposed by 3GPP, the introduction of service function chain (SFC) constraints exacerbates these challenges. Therefore, in this paper, we propose GDRL-SFCR, an end-to-end routing decision method based on graph neural network (GNN) and deep reinforcement learning (DRL) which jointly optimize the end-to-end transmission delay and network load balancing under SFC constraints. Specifically, this method constructs the system model based on the latest NTN low-orbit satellite network end-to-end transmission architecture, taking into account the SFC constraints, transmission delays, and network node loads in the end-to-end traffic transmission, uses a GNN to extract node attributes and dynamic topology features, and uses the DRL method to design specific reward functions to train the model to learn routing policies that satisfy the SFC constraints. The simulation results demonstrate that, compared with graph theory-based methods and reinforcement learning-based methods, GDRL-SFCR can reduce the end-to-end traffic transmission delay by more than 11.3%, reduce the average network load by more than 14.1%, and increase the traffic access success rate and network capacity by more than 19.1% and two times, respectively. Full article
(This article belongs to the Special Issue 5G/6G Networks for Wireless Communication and IoT)
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<p>End-to-end traffic transmission model. Dashed arrows indicate wireless links and realized arrows indicate wired links.</p>
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<p>Model architecture of the proposed method.</p>
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<p>Access success rates of different data flows. The red curve is the result based on the reinforcement learning algorithm (DQR), the green curve is the result of the traditional graph theory algorithm (SFC-APS), the magenta curve is the result of the algorithm proposed in this paper (DQN-LBR), and the blue curve is the result of the algorithm proposed in this paper (GDRL-SFCR). FN represents the total number of functional nodes in the end-to-end path SFC constraint.</p>
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<p>Network average load of different data flows. The red curve is the result based on the reinforcement learning algorithm (DQR), the green curve is the result of the traditional graph theory algorithm (SFC-APS), the magenta curve is the result of the algorithm proposed in this paper (DQN-LBR), and the blue curve is the result of the algorithm proposed in this paper (GDRL-SFCR). FN represents the total number of functional nodes in the end-to-end path SFC constraint.</p>
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<p>Average path delay of different data flows. The red curve is the result based on the reinforcement learning algorithm (DQR), the green curve is the result of the traditional graph theory algorithm (SFC-APS), the magenta curve is the result of the algorithm proposed in this paper (DQN-LBR), and the blue curve is the result of the algorithm proposed in this paper (GDRL-SFCR). FN represents the total number of functional nodes in the end-to-end path SFC constraint.</p>
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<p>Network capacity of different data flows. The red curve is the result based on the reinforcement learning algorithm (DQR), the green curve is the result of the traditional graph theory algorithm (SFC-APS), the magenta curve is the result of the algorithm proposed in this paper (DQN-LBR), and the blue curve is the result of the algorithm proposed in this paper (GDRL-SFCR). FN represents the total number of functional nodes in the end-to-end path SFC constraint.</p>
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<p>Impact of weight <math display="inline"><semantics> <msub> <mi>θ</mi> <mn>1</mn> </msub> </semantics></math> on performance metrics. The green curve is the result of KPI variation with weights. The blue curve is the path delay variance as a function of weight. The blue curve is the result of network load variance variation with weights.</p>
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<p>Average running time of different data flows for all algorithms. The red curve is the result based on the reinforcement learning algorithm (DQR), the green curve is the result of the traditional graph theory algorithm (SFC-APS), the magenta curve is the result of the algorithm proposed in this paper (DQN-LBR), and the blue curve is the result of the algorithm proposed in this paper (GDRL-SFCR). FN represents the total number of functional nodes in the end-to-end path SFC constraint.</p>
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22 pages, 2305 KiB  
Article
Impact of Supercritical CO2 Treatment on Lupin Flour and Lupin Protein Isolates
by Rubén Domínguez-Valencia, Roberto Bermúdez, Mirian Pateiro, Laura Purriños, Jose Benedito and José M. Lorenzo
Foods 2025, 14(4), 675; https://doi.org/10.3390/foods14040675 - 17 Feb 2025
Viewed by 357
Abstract
Global population growth is putting pressure on the food supply, necessitating the exploration of new, alternative, and sustainable protein sources. Lupin, an underutilized legume in human nutrition, has the potential to play a significant role in addressing this challenge. However, its incorporation into [...] Read more.
Global population growth is putting pressure on the food supply, necessitating the exploration of new, alternative, and sustainable protein sources. Lupin, an underutilized legume in human nutrition, has the potential to play a significant role in addressing this challenge. However, its incorporation into the human diet requires thorough investigation, including exploring and optimizing functionalization processes to maximize its potential. This study aimed to optimize the parameters (pressure, time, and CO2 flow) for extracting anti-technological factors (ATFs) from lupin using supercritical CO2 (SC-CO2) and to evaluate the effects of this extraction on both the flour and the protein isolate derived from it. Optimization revealed that the optimal SC-CO2 conditions were a CO2 flow rate of 4 kg/h at 400 bar for 93 min. Under these conditions, significant changes were observed in the flour composition, including a reduction in oil, polyphenols, and moisture content, along with an increase in ash content. Improved color parameters were also noted. These variations were attributed to the removal of oil and phenolic compounds during processing. Furthermore, this research demonstrated that SC-CO2 treatment improved lupin protein isolate (LPI) purity (93.81 ± 0.31% vs. 87.42 ± 0.48%), significantly reduced oil content (8.31 ± 0.09% vs. 14.31 ± 0.32%), and enhanced color parameters. The SC-CO2 procedure also resulted in a higher protein extraction yield (56.95 ± 0.45% vs. 53.29 ± 2.37%). However, the total extraction yield (g LPI/100 g of flour) was not affected by SC-CO2 treatment, remaining at 24.30 ± 0.97% for the control sample and 24.21 ± 0.26% for the treated sample. The extracted oil (2.71 ± 0.11 g/100 g of flour), a co-product of the SC-CO2 step, exhibited a fatty acid profile characterized by high levels of unsaturated fatty acids (62.8 ± 0.74 g/100 g oil), oleic acid (27.76 ± 0.77 g/100 g oil), linoleic acid (25.98 ± 0.73 g/100 g oil), and α-linolenic acid (5.32 ± 0.16 g/100 g oil), as well as a balanced ratio of essential fatty acids (n-6/n-3 = 4.89). The treatment had minimal to no effect on amino acid content or chemical score, and the protein was characterized by high amounts of essential amino acids (334 ± 3.12 and 328 ± 1.05 mg/g protein in LPI-control and LPI-SF, respectively). These findings demonstrate that both the LPI and the oil extracted using SC-CO2 possess high nutritional quality and are suitable for human food applications. Full article
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<p>Visual aspect of the different lupin flours obtained during BBD runs (<b>a</b>) and visual aspect of lupin flour treated with supercritical CO<sub>2</sub> under optimal conditions and extracted oil (<b>b</b>).</p>
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<p>Profiles for predicted values and desirability.</p>
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<p>Response surface plots (<b>a</b>) and contour plots (<b>b</b>) (desirability) as function of pressure, flow, and extraction time.</p>
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<p>Visual aspect of lupin protein isolate obtained from untreated flour (Co1 and Co2) and from supercritical CO<sub>2</sub>-treated flour under optimal conditions (SF1 and SF2).</p>
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22 pages, 2068 KiB  
Article
Determination of the Total Phosphorus Decay Coefficient Based on Hydrological Models in an Artificial Reservoir in the Brazilian Semi-Arid Region
by Francisco Josivan de Oliveira Lima, Fernando Bezerra Lopes, Daniel Antônio Camelo Cid, Iran Eduardo Lima Neto, Renan Vieira Rocha, Alyson Brayner Sousa Estácio, Isabel Cristina da Silva Araújo, Nayara Rochelli de Sousa Luna, Michele Cunha Pontes, Arthur Costa Tomaz de Souza and Eunice Maia de Andrade
Hydrology 2025, 12(2), 36; https://doi.org/10.3390/hydrology12020036 - 16 Feb 2025
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Abstract
Phosphorus input into surface water is a global concern due to its role in eutrophication, which is especially critical in semi-arid regions with their challenging climatic conditions. This study evaluated the best model for estimating the phosphorus decay coefficient (k) in semi-arid lakes, [...] Read more.
Phosphorus input into surface water is a global concern due to its role in eutrophication, which is especially critical in semi-arid regions with their challenging climatic conditions. This study evaluated the best model for estimating the phosphorus decay coefficient (k) in semi-arid lakes, using flows from the Soil Moisture Accounting Procedure (SMAP), model of Génie Rural à 4 paramètres Journalier (GR4J), and reverse water balance hydrological models. Conducted at the Orós reservoir with 37 sampling campaigns from 2008 to 2017, it compared decay rates for temperate, tropical, and semi-arid climates. Some analyses also used phosphorus concentrations measured at the reservoir inlet. Model efficiency was assessed with bias, mean relative error, mean squared error, root mean squared error, and standard deviation. from the best models, water quality classes were classified based on phosphorus concentrations with the use of a confusion matrix to calculate accuracy, precision, recall, and F1 score. The findings demonstrated that the decay rate tailored for semi-arid regions, when combined with GR4J flow data, offered the highest accuracy in estimating phosphorus concentrations (bias = 0.0012, RMSE = 0.0326, EMR = 60.6134, STD = 0.0312). In contrast, the decay rate calibrated for tropical conditions with SMAP-derived flows proved superior for classifying water quality categories (classes defined by CONAMA Resolution 357/05). Therefore, the GR4J model for semi-arid conditions stands out for concentration estimation, while the tropical decay rate with SMAP flows is preferable for effective classification of water quality status. Full article
(This article belongs to the Special Issue Hydrodynamics and Water Quality of Rivers and Lakes)
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<p>Location of the Orós Reservoir and water sampling points.</p>
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<p>Detailed flow of research steps.</p>
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<p>Relationship between total phosphorus, volume variation, and rainfall.</p>
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<p>Boxplot of total phosphorus concentrations.</p>
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<p>Total phosphorus modelling with the SMAP (<b>A</b>), GR4J (<b>B</b>) and RWB (<b>C</b>) hydrological models and the classes of CONAMA resolution 357/05.</p>
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<p>Total phosphorus modelling with the SMAP (<b>A</b>), GR4J (<b>B</b>) and RWB (<b>C</b>) hydrological models adjusted by measured inflow concentration and the classes of CONAMA resolution 357/05.</p>
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