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Search Results (12,074)

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19 pages, 5735 KiB  
Article
AQbD-Based UPLC-ELSD Method for Quantifying Medium Chain Triglycerides in Labrafac™ WL 1349 for Nanoemulsion Applications
by Alessio Gaggero, Viktoria Marko, Dalibor Jeremic, Carolin Tetyczka, Philippe Caisse and Jesús Alberto Afonso Urich
Molecules 2025, 30(3), 486; https://doi.org/10.3390/molecules30030486 - 22 Jan 2025
Abstract
In response to recent regulatory guidelines, including ICH (International Council for Harmonisation) Q2 (R2) and Q14, we developed a UPLC-ELSD method to quantify Medium-Chain Triglycerides (MCTs) in Labrafac™ WL 1349 for nanoemulsion applications. This procedure, crafted using Analytical Quality by Design (AQbD) principles, [...] Read more.
In response to recent regulatory guidelines, including ICH (International Council for Harmonisation) Q2 (R2) and Q14, we developed a UPLC-ELSD method to quantify Medium-Chain Triglycerides (MCTs) in Labrafac™ WL 1349 for nanoemulsion applications. This procedure, crafted using Analytical Quality by Design (AQbD) principles, addresses not only the validation of the methodology but also the lifecycle management challenges associated with the analysis of lipid-based excipients. Key parameters such as mobile phase composition, organic modifier, column type, flow rate, diluent, and column temperature were optimized to meet regulatory standards and ensure robustness in MCT quantification. Optimal conditions were achieved with a Waters Acquity HSS T3 (100 × 2.1 mm i.d., 1.8 μm) column at 33 °C, using a mixture of methanol (97.5%) and water (2.5%) containing 0.4% of formic acid at a flow rate of 0.41 mL/min. The method demonstrated an excellent fit on a cubic modelization for MCTs over a broad range of concentrations. Forced degradation studies, including hydrolytic (acidic and basic), oxidative, and thermal stress, confirmed the method’s suitability for possible stability scenarios. This validated UPLC method was successfully applied to quantitative analyses of bulk and formulation prototype samples containing MCTs. This AQbD-driven method enhances not only knowledge but also regulatory-compliant and cost-effective excipient control. Full article
(This article belongs to the Special Issue Applied Analytical Chemistry: Second Edition)
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<p>Labrafac structure, including possible combinations of triglyceride fatty acid mixtures.</p>
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<p>Analytical Quality by Design workflow for the development of the Labrafac procedure.</p>
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<p>Ishikawa Fishbone Diagram for the assessment of CMeAs and CMePs.</p>
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<p>Prediction Profiler showing the impact of each factor setting on the overall desirability. The red cross indicates the final method setting. Factor coding: A = column temperature (°C), B = injection volume (µl), C = flow (ml/min), D = water amount in mobile phase (%), E = formic acid amount in mobile phase (%), F = diluent, G = column, H = organic solvent.</p>
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<p>Contour plot of the desirability for the final factor settings according to the legend. Factor coding: A = column temperature (°C), B = injection volume (µl), C = flow (ml/min), D = water amount in mobile phase (%), E = formic acid amount in mobile phase (%), F = diluent, G = column, H = organic solvent.</p>
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<p>Exemplary chromatogram of a Labrafac injection. (1) tricaprylin, (2) 1,2-caprate-3-caprylate, (3) 1,2-caprylate-3-caprate, (4) tricaprin.</p>
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<p>Chromatograms of specificity studies. (1) mobile phase injection; (2) blank injection; (3) nanoemulsion matrix injection.</p>
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<p>Chromatogram of forced degradation studies on Labrafac. (1) control sample, (2) RapidOxy stress, (3) thermal stress, (4) oxidative stress, (5) basic stress, (6) acidic stress.</p>
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<p>Comparison of Mono- and Diglycerides chromatograms. (1) Mono- and Diglycerides standard injection, (2) acidic stress condition. The blue circle identifies the same RT region.</p>
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<p>Combined regression data showing the model, the resulting equation, R<sup>2</sup>, and the 95% confidence intervals.</p>
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<p>Standardized residuals for combined regression data.</p>
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<p>Exemplary chromatogram of the tested nanoemulsion prototype.</p>
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26 pages, 23622 KiB  
Article
CPS-RAUnet++: A Jet Axis Detection Method Based on Cross-Pseudo Supervision and Extended Unet++ Model
by Jianhong Gan, Kun Cai, Changyuan Fan, Xun Deng, Wendong Hu, Zhibin Li, Peiyang Wei, Tao Liao and Fan Zhang
Electronics 2025, 14(3), 441; https://doi.org/10.3390/electronics14030441 - 22 Jan 2025
Abstract
Atmospheric jets are pivotal components of atmospheric circulation, profoundly influencing surface weather patterns and the development of extreme weather events such as storms and cold waves. Accurate detection of the jet stream axis is indispensable for enhancing weather forecasting, monitoring climate change, and [...] Read more.
Atmospheric jets are pivotal components of atmospheric circulation, profoundly influencing surface weather patterns and the development of extreme weather events such as storms and cold waves. Accurate detection of the jet stream axis is indispensable for enhancing weather forecasting, monitoring climate change, and mitigating disasters. However, traditional methods for delineating atmospheric jets are plagued by inefficiency, substantial errors, and pronounced subjectivity, limiting their applicability in complex atmospheric scenarios. Current research on semi-supervised methods for extracting atmospheric jets remains scarce, with most approaches dependent on traditional techniques that struggle with stability and generalization. To address these limitations, this study proposes a semi-supervised jet stream axis extraction method leveraging an enhanced U-Net++ model. The approach incorporates improved residual blocks and enhanced attention gate mechanisms, seamlessly integrating these enhanced attention gates into the dense skip connections of U-Net++. Furthermore, it optimizes the consistency learning phase within semi-supervised frameworks, effectively addressing data scarcity challenges while significantly enhancing the precision of jet stream axis detection. Experimental results reveal the following: (1) With only 30% of labeled data, the proposed method achieves a precision exceeding 80% on the test set, surpassing state-of-the-art (SOTA) baselines. Compared to fully supervised U-Net and U-Net++ methods, the precision improves by 17.02% and 9.91%. (2) With labeled data proportions of 10%, 20%, and 30%, the proposed method outperforms the MT semi-supervised method, achieving precision gains of 9.44%, 15.58%, and 19.50%, while surpassing the DCT semi-supervised method with improvements of 10.24%, 16.64%, and 14.15%, respectively. Ablation studies further validate the effectiveness of the proposed method in accurately identifying the jet stream axis. The proposed method exhibits remarkable consistency, stability, and generalization capabilities, producing jet stream axis extractions closely aligned with wind field data. Full article
(This article belongs to the Special Issue Application of Machine Learning in Graphics and Images, 2nd Edition)
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<p>Unet Architecture.</p>
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<p>Wind speed mapping to R channel pixel values function. The deeper the red, the more sensitive the mapping of wind speed to changes in the R channel pixel values.</p>
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<p>Overall architecture of the CPS-RAUnet++ semi-supervised learning model. The two RAUnet++ in the consistency learning phase have the same structure and are initialized independently. Weak augmentation is performed for labeled data for each model input and strong augmentation is used for each unlabeled data. The red arrow in the figure represents unsupervised loss, the green dashed arrow represents supervised loss, the yellow arrow represents self-training phase loss, and the purple arrow represents the data processing process.</p>
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<p>Unet++ backbone.We proposed Residual block with DropConnect.</p>
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<p>We proposed SCAG architecture.</p>
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<p>RAUnet++ architecture.</p>
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<p>Detailed analysis of layer 1 dense skip paths in RAUnet++.</p>
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<p>RAUNet++ can be pruned to RAUNet++ L1,RAUNet++ L2,RAUNet++ L3 and RAUNet++ L4 if trained with deep supervision. The cyan circles represent the input or feature maps. The blue circles represent the intermediate states of the model. The gray circles represent the network layers that can be pruned.</p>
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<p>Improved results of jet stream axis plotting. The green dashed box contains the unmodified visualization result, while the blue dashed box contains the improved visualization result.</p>
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<p>Loss and IoU trends in the training and validation sets during the self-training phase (the left figure shows the Loss trend, while the right figure shows the IoU trend; the red line represents the training set, and the blue line represents the validation set).</p>
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<p>The comparison between CPS-RAUNet++ and other methods on Dice after multiple experiments for the test dataset, all experiments were conducted using 30% labeled data.</p>
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<p>Improvement of our proposed method on the supervised baseline RAUnet++ regarding DR (<b>left image</b>) and Pre (<b>right image</b>) metrics at 30%, 20%, 10%, and 5% labeled data ratios.</p>
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<p>Comparison of segmentation results of different models in the ablation experiment. The red circles represent missed cases, and the green circles represent false detection cases.</p>
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<p>The comparison between CPS-RAUNet++ and other methods on Pre after multiple experiments for the test dataset.</p>
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<p>Inference time, IoU, and Parameters of CPS-RAUNet++ L<math display="inline"><semantics> <mrow> <mn>1</mn> <mo>−</mo> <mn>4</mn> </mrow> </semantics></math> for the test dataset.</p>
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<p>Visualization results of the jet axis ablation experiment segmentation generated by MICAPS 4.0 software. The black and purple dashed boxes represent missed cases, and the yellow dashed box represents false detection areas.</p>
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27 pages, 4157 KiB  
Review
Review of Thermal Management Techniques for Prismatic Li-Ion Batteries
by Nasim Saber, Christiaan Petrus Richter and Runar Unnthorsson
Energies 2025, 18(3), 492; https://doi.org/10.3390/en18030492 - 22 Jan 2025
Abstract
This review presents a comprehensive analysis of battery thermal management systems (BTMSs) for prismatic lithium-ion cells, focusing on air and liquid cooling, heat pipes, phase change materials (PCMs), and hybrid solutions. Prismatic cells are increasingly favored in electric vehicles and energy storage applications [...] Read more.
This review presents a comprehensive analysis of battery thermal management systems (BTMSs) for prismatic lithium-ion cells, focusing on air and liquid cooling, heat pipes, phase change materials (PCMs), and hybrid solutions. Prismatic cells are increasingly favored in electric vehicles and energy storage applications due to their high energy content, efficient space utilization, and improved thermal management capabilities. We evaluate the effectiveness, advantages, and challenges of each thermal management technique, emphasizing their impact on performance, safety, and the lifespan of prismatic Li-ion batteries. The analysis reveals that while traditional air and liquid cooling methods remain widely used, 80% of the 21 real-world BTMS samples mentioned in this review employ liquid cooling. However, emerging technologies such as PCM and hybrid systems offer superior thermal regulation, particularly in high-power applications. However, both PCM and hybrid systems come with significant challenges; PCM systems are limited by their low thermal conductivity and material melting points. While hybrid systems face complexity, cost, and potential reliability concerns due to their multiple components nature. This review underscores the need for continued research into advanced BTMSs to optimize energy efficiency, safety, and longevity for prismatic cells in electric vehicle applications and beyond. Full article
(This article belongs to the Special Issue Challenges and Opportunities towards Lithium-Ion Batteries)
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<p>Types of Li-ion battery cells [<a href="#B29-energies-18-00492" class="html-bibr">29</a>].</p>
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<p>A block diagram of the control scheme and battery module configuration with dummy cells for energy-efficient on-off cooling in prismatic Li-ion BTMSs [<a href="#B62-energies-18-00492" class="html-bibr">62</a>].</p>
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<p>(<b>a</b>) Schematic of an innovative liquid cooling system with enhanced flow distribution, (<b>b</b>) exploded view, and (<b>c</b>) top view of cover plate with bifurcation channels for uniform coolant distribution [<a href="#B73-energies-18-00492" class="html-bibr">73</a>].</p>
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<p>Schematic of cold plate with airfoil fins for improved heat transfer and turbulence enhancement [<a href="#B72-energies-18-00492" class="html-bibr">72</a>].</p>
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<p>Improved cooling efficiency with UMHP and forced convection: (<b>a</b>) the UMHP cooling system demonstration; (<b>b</b>) the shape of the battery cell; and (<b>c</b>) the UMHP group geometry [<a href="#B88-energies-18-00492" class="html-bibr">88</a>].</p>
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<p>Configuration of the battery test bench with flat micro heat pipe arrays (MHPAs) for enhanced surface contact and thermal management under high-discharge conditions [<a href="#B89-energies-18-00492" class="html-bibr">89</a>].</p>
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<p>Dual bionic cold plate cooling system with nasturtium vein and honeycomb patterns: enhanced heat dissipation and reduced weight compared to traditional systems [<a href="#B107-energies-18-00492" class="html-bibr">107</a>].</p>
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<p>Hybrid BTMS with micro heat pipes, air cooling, and intermittent water spraying for enhanced thermal management [<a href="#B112-energies-18-00492" class="html-bibr">112</a>].</p>
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14 pages, 3737 KiB  
Article
Parametric Optimization of Concentrated Photovoltaic-Phase Change Material as a Thermal Energy Source for Buildings
by Ali Hasan Shah, Ahmed Hassan, Shaimaa Abdelbaqi, Hamza Alnoman, Abbas Fardoun, Mahmoud Haggag, Mutassim Noor and Mohammad Shakeel Laghari
Buildings 2025, 15(3), 327; https://doi.org/10.3390/buildings15030327 - 22 Jan 2025
Abstract
A concentrated photovoltaic system is evaluated as a thermal energy source employing phase change material to meet the domestic water heating demand. A paraffin wax-based phase change material is selected with a 58 °C melting point to store enough thermal energy to match [...] Read more.
A concentrated photovoltaic system is evaluated as a thermal energy source employing phase change material to meet the domestic water heating demand. A paraffin wax-based phase change material is selected with a 58 °C melting point to store enough thermal energy to match the hot water demand in the buildings. The energy performance of the concentrated photovoltaics containing phase change materials is compared to that of the reference to determine the increased energy outputs due to the heat removal by the material. The concentrated photovoltaics-phase change material achieved 30% higher energy output compared to the reference concentrated photovoltaic, thus providing a strong justification for the improved thermal management design. An enthalpy-based thermal model is developed to compare the experimental results with model predictions, confirming a reasonable agreement between the results. The model is used determine the optimum melting point and container size for different phase change materials under different radiation concentrations for the hot climate of the United Arab Emirates. Full article
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<p>Experimental setup of the CPV-PCM system.</p>
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<p>The schematics of the numerical setup showing the heat transfer boundaries in the control domain.</p>
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<p>Solar radiation intensity received at the front surface of static PV, tracked PV, and tracked CPV measured for three days in 21–23 July at UAE University Al Ain.</p>
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<p>The total energy gain per day by the static PV, PV tracked and CPV measured on the 2nd day of test duration, 22nd July representative of extremely hot weather in Al Ain, UAE.</p>
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<p>The temperature rise of the static PV, tracked PV, CPV and CPV-PCM systems using paraffin wax with a melting point of 58 °C measured on the 2nd day of test duration, 22 July representative of extremely hot weather in Al Ain, UAE.</p>
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<p>Comparison of measured temperatures of the PCM, paraffin wax, RT-60, with the temperatures predicted by the model at the front layer, middle layer, and back layer of the melting PCM for a typical summer day in Al Ain, UAE employing the onsite measured weather data.</p>
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<p>Time required by the solid PCM to completely melt by the solar thermal energy available at CPV (blue line) and return to solid form (orange line) by heat dissipation to cooler ambient for various container depths.</p>
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<p>The optimal amount of PCM required under optical concentration ratios (OCRs).</p>
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<p>The numerically predicted melting fraction as a function of time of PCM (paraffin wax, RT 60) at various melting points between 35 °C and 65 °C to evaluate the time taken to complete melting and solidification cycle.</p>
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<p>The numerically predicted maximum and average temperature drop (°C) achievable by PCM with different melting points from 35 °C to 65 °C.</p>
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<p>The optimal amount of various PCMs under optical concentration ratio (OCR) of 3.</p>
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22 pages, 3513 KiB  
Article
Isothermal Pyrolysis of Bamboo and Pinewood Biomass: Product Characterization and Comparative Study in a Fluidized Bed Reactor
by Manqoba Shezi and Sammy Lewis Kiambi
Bioengineering 2025, 12(2), 99; https://doi.org/10.3390/bioengineering12020099 - 22 Jan 2025
Abstract
Fast pyrolysis of biomass is crucial for sustainable biofuel production, necessitating thorough characterization of feedstocks to optimize thermal conversion technologies. This study investigated the isothermal pyrolysis of bamboo and pinewood biomass in a sand-fluidized bed reactor, aiming to assess biomass suitability for commercial [...] Read more.
Fast pyrolysis of biomass is crucial for sustainable biofuel production, necessitating thorough characterization of feedstocks to optimize thermal conversion technologies. This study investigated the isothermal pyrolysis of bamboo and pinewood biomass in a sand-fluidized bed reactor, aiming to assess biomass suitability for commercial bio-oil production. The pyrolysis products and biomass species were characterized through proximate and ultimate analyses, along with GCMS, FTIR, SEM/EDX, and structural analysis to assess their chemical and physical properties. Results indicated that pine bio-oil possesses superior energy density, with a higher calorific value (20.38 MJ/kg) compared to bamboo (18.70 MJ/kg). Pine biomass yielded greater organic phase bio-oil (BOP) at 13 wt%, while bamboo produced 9 wt%. Energy yields were also notable, with pine exhibiting an energy yield of 15% for bio-oil organic phase (EBOP), compared to 11% for bamboo. The fibrous nature of bamboo biomass resulted in less-reacted biomass at constant reaction time due to flow resistance during pyrolysis. Pine bio-oil organic phase (P-BOP) demonstrated a higher heating value (23.90 MJ/kg) than bamboo (B-BOP). The findings suggest that while both biomass types are viable renewable energy sources, pine biomass is more favorable for commercialization due to its superior energy properties and efficiency in pyrolysis. Full article
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<p>Schematic diagram for fast pyrolysis in a fluidized bed reactor (FBR).</p>
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<p>Absorbance peaks of pine and bamboo biomass after acid hydrolysis.</p>
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<p>FTIR profiles of pine and bamboo biomass.</p>
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<p>Fast pyrolysis product yields [BOP: bio-oil organic phase, BAP: bio-oil aqueous phase, BO: bio-oil, BC: biochar, and BG: pyrolysis gas].</p>
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<p>Biomass balance for fast pyrolysis in a fluidized bed reactor.</p>
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<p>GCMS analysis of bio-oil organic phase for pine (P-BOP) and bamboo (B-BOP).</p>
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<p>FTIR spectra of bio-oil organic phase for pine (P-BOP) and bamboo (B-BOP).</p>
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<p>Van Krevelen plot of pine (P) and bamboo (B) for biomass (BM), biochar (BC), and bio-oil organic phase (BOP).</p>
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<p>SEM/EDX of bamboo biochar (biochar-B) and pine biochar (Biochar-P).</p>
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<p>Biogas analysis and energy yields for bio-oil organic phase (EBOP), biogas (EBG), biochar (EBC), and losses.</p>
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29 pages, 4808 KiB  
Article
Multi-Baseline Bistatic SAR Three-Dimensional Imaging Method Based on Phase Error Calibration Combining PGA and EB-ISOA
by Jinfeng He, Hongtu Xie, Haozong Liu, Zhitao Wu, Bin Xu, Nannan Zhu, Zheng Lu and Pengcheng Qin
Remote Sens. 2025, 17(3), 363; https://doi.org/10.3390/rs17030363 - 22 Jan 2025
Abstract
Tomographic synthetic aperture radar (TomoSAR) is an advanced three-dimensional (3D) synthetic aperture radar (SAR) imaging technology that can obtain multiple SAR images through multi-track observations, thereby reconstructing the 3D spatial structure of targets. However, due to system limitations, the multi-baseline (MB) monostatic SAR [...] Read more.
Tomographic synthetic aperture radar (TomoSAR) is an advanced three-dimensional (3D) synthetic aperture radar (SAR) imaging technology that can obtain multiple SAR images through multi-track observations, thereby reconstructing the 3D spatial structure of targets. However, due to system limitations, the multi-baseline (MB) monostatic SAR (MonoSAR) encounters temporal decorrelation issues when observing the scene such as forests, affecting the accuracy of the 3D reconstruction. Additionally, during TomoSAR observations, the platform jitter and inaccurate position measurement will contaminate the MB SAR data, which may result in the multiplicative noise with phase errors, thereby leading to the decrease in the imaging quality. To address the above issues, this paper proposes a MB bistatic SAR (BiSAR) 3D imaging method based on the phase error calibration that combines the phase gradient autofocus (PGA) and energy balance intensity-squared optimization autofocus (EB-ISOA). Firstly, the signal model of the MB one-stationary (OS) BiSAR is established and the 3D imaging principle is presented, and then the phase error caused by platform jitter and inaccurate position measurement is analyzed. Moreover, combining the PGA and EB-ISOA methods, a 3D imaging method based on the phase error calibration is proposed. This method can improve the accuracy of phase error calibration, avoid the vertical displacement, and has the noise robustness, which can obtain the high-precision 3D BiSAR imaging results. The experimental results are shown to verify the effectiveness and practicality of the proposed MB BiSAR 3D imaging method. Full article
(This article belongs to the Section Engineering Remote Sensing)
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<p>Observation model of the MB OS BiSAR imaging.</p>
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<p>Geometric relationship of the target projection in the MB OS BiSAR imaging.</p>
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<p>Geometric diagram of measurement.</p>
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<p>Flowchart of the proposed 3D BiSAR imaging method based on the phase error calibration.</p>
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<p>Schematic diagram of the point targets. The blue circle in the figure represents the point target.</p>
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<p>Three-dimensional imaging results. The blue circle represents the point cloud. (<b>a</b>) Imaging results before the coordinate transformation. (<b>b</b>) Imaging results after the coordinate transformation.</p>
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<p>Three perspective display of 3D imaging results after coordinate transformation. The blue circle represents the point cloud. (<b>a</b>) XY section. (<b>b</b>) XZ section. (<b>c</b>) YZ section.</p>
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<p>Tomographic profiles of imaging results of point targets. The blue line is the profile formed by the sampling points in the tomographic direction. (<b>a</b>) Target A; (<b>b</b>) Target B; (<b>c</b>) Target C; (<b>d</b>) Target D; (<b>e</b>) Target E.</p>
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<p>Target setting and imaging results. (<b>a</b>) Schematic diagram of the target <math display="inline"><semantics> <mrow> <mi>T</mi> <mi>a</mi> <msub> <mi>r</mi> <mi>z</mi> </msub> </mrow> </semantics></math>. The blue circle represents the point target. (<b>b</b>) Imaging results of the target <math display="inline"><semantics> <mrow> <mi>T</mi> <mi>a</mi> <msub> <mi>r</mi> <mi>z</mi> </msub> </mrow> </semantics></math> without phase errors. Different colors represent different amplitudes of pixels.</p>
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<p>Two-dimensional imaging result and the selected PS. (<b>a</b>) Two-dimensional imaging result. Different colors represent different amplitudes of pixels. (<b>b</b>) The selected PS.</p>
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<p>Imaging results of the target <math display="inline"><semantics> <mrow> <mi>T</mi> <mi>a</mi> <msub> <mi>r</mi> <mi>z</mi> </msub> </mrow> </semantics></math> obtained by different methods. Different colors represent different amplitudes of pixels. (<b>a</b>) Imaging results with the phase error; (<b>b</b>) PGA method; (<b>c</b>) ISOA method; (<b>d</b>) BF-PGA method; (<b>e</b>) Proposed method.</p>
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<p>Tomographic profile of the selected PS.</p>
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<p>Monte Carlo experiments conducted using four methods under the influence of Gaussian phase noise. The variation curve and standard deviation of image indicators with the SNR after the calibration. (<b>a</b>) IE; (<b>b</b>) IC; (<b>c</b>) standard deviation of IE; (<b>d</b>) standard deviation of IC.</p>
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<p>Monte Carlo experiments conducted using four methods under the influence of uniform distributed phase noise. The variation curve and standard deviation of image indicators with the SNR after the calibration. (<b>a</b>) IE; (<b>b</b>) IC; (<b>c</b>) standard deviation of IE; (<b>d</b>) standard deviation of IC.</p>
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<p>Target structure diagram. The blue circle represents the scattering point. (<b>a</b>) Three-dimensional perspective display. (<b>b</b>) XY perspective diagram. (<b>c</b>) XZ perspective diagram. (<b>d</b>) YZ perspective diagram.</p>
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<p>SAR images before and after 2D autofocus processing. Different colors represent different amplitudes of pixels. (<b>a</b>) Before 2D autofocus processing. (<b>b</b>) After 2D autofocus processing.</p>
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<p>Imaging results of the complex target obtained by different methods. Different colors represent different amplitudes of pixels. The red circles and letters are the circled lines and names of the highlighted areas. (<b>a</b>) Imaging results with the phase error; (<b>b</b>) PGA method; (<b>c</b>) ISOA method; (<b>d</b>) BF-PGA method; (<b>e</b>) Proposed method.</p>
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<p>Observation of 3D imaging results from three perspectives. Different colors represent different amplitudes of pixels. (<b>a</b>–<b>c</b>) Processed by PGA method. (<b>d</b>–<b>f</b>) Processed by ISOA method. (<b>g</b>–<b>i</b>) Processed by BF-PGA method. (<b>j</b>–<b>l</b>) Processed by proposed method.</p>
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<p>Projection of the MonoSAR and BiSAR configurations. (<b>a</b>) MonoSAR; (<b>b</b>) BiSAR.</p>
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34 pages, 11386 KiB  
Article
Sustainable Emulsified Acid Treatments for Enhanced Oil Recovery in Injection Wells: A Case Study in the Qusahwira Field
by Charbel Ramy, Razvan George Ripeanu, Salim Nassreddine, Maria Tănase, Elias Youssef Zouein, Alin Diniță and Constantin Cristian Muresan
Sustainability 2025, 17(3), 856; https://doi.org/10.3390/su17030856 - 22 Jan 2025
Viewed by 68
Abstract
Emulsified acid treatments present an innovative and environmentally sustainable alternative to conventional hydrochloric acid (HCl) methods in enhancing oil recovery. This study investigates the application of a stable emulsified acid formulation in matrix acidizing operations to improve injectivity in four wells within the [...] Read more.
Emulsified acid treatments present an innovative and environmentally sustainable alternative to conventional hydrochloric acid (HCl) methods in enhancing oil recovery. This study investigates the application of a stable emulsified acid formulation in matrix acidizing operations to improve injectivity in four wells within the Qusahwira Field. Compared to traditional 15% HCl treatments, the emulsified acid demonstrates deeper acid penetration and retardation effect leading to enhanced injection rate. By delivering deep worm holing effects against calcium carbonate formation, this dual-phase system enhances injectivity by 14 times while minimizing the environmental and material impacts associated with spent acid volumes. The methodology integrates advanced neural network modeling to predict stimulation outcomes based on 15 operational and reservoir factors. This model reduces the trial-and-error approach, cutting operational costs and time for carbonate reservoir. Field trials reveal significant improvements in injection pressure and a marked reduction in circulation pressure during stimulation, underscoring the treatment’s efficiency. Developed in a Superior Abu Dhabi laboratory, the emulsified acid achieves high-temperature stability (200 °F) and deep acid penetration, further reducing the ecological footprint of acid stimulation by enhancing operational precision and reducing chemical use. This paper highlights a sustainable approach to optimizing reservoir productivity, aligning with global efforts to minimize environmental impacts in oil recovery processes. Full article
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<p>The aspect of obtained emulsion: (<b>a</b>) 20% Emulsified Acid Recipe Stable Emulsion; (<b>b</b>) snack test performed using beaker full of fresh water to simulate the actual case of emulsified acid injection into the reservoir.</p>
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<p>Emulsified acid recipe tests at high temperature: (<b>a</b>) Emulsified acid recipe; (<b>b</b>) Homogenous mixture; (<b>c</b>) Corrosion test cell for high temperature.</p>
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<p>Stability of emulsified acid recipe: (<b>a</b>) Separation acid–diesel (unstable); (<b>b</b>) Corrosion test cell at high temperature 94 °C (200 F); (<b>c</b>) Stable emulsion after testing for 6 h at 94 °C (200 F).</p>
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<p>Corrosion tester machine for testing: (<b>a</b>) OFITE HTHP corrosion tester; (<b>b</b>) 4 specimens to run four tests.</p>
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<p>Corrosion testing bottles containing low carbon steel L-80 coupons: (<b>a</b>) corrosion test bottle containing low carbon steel L-80 coupon profile view; (<b>b</b>) corrosion test bottle containing low carbon steel L-80 coupon top view.</p>
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<p>Corrosion rate vs. corrosion inhibitor dosage.</p>
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<p>Carbon steel coupons surface behavior: (<b>a</b>) Low carbon steel L-80 surface before performing corrosion test; (<b>b</b>) Low carbon steel L-80 surface before performing corrosion test.</p>
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<p>Simulation Run for acid stimulation using Emulsified Acid.</p>
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<p>Skin damage profile after stimulation.</p>
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<p>Acid invasion profile within the rock properties.</p>
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<p>Permeability results.</p>
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<p>Post-injectivity result for 4 cases tested in the field: (<b>a</b>) Post-injectivity result for case 1; (<b>b</b>) Post-injectivity result for case 2; (<b>c</b>) Post-injectivity result for case 3; (<b>d</b>) Post-injectivity result for case 4.</p>
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<p>Real-time data monitoring from the field during acid stimulation.</p>
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<p>Abrasive Jetting Tool used in Emulsified Acid Job.</p>
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<p>Acid injection profile with the formation through abrasive jetting tool.</p>
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<p>Real-time data monitoring of pumping emulsified acid.</p>
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<p>Injection rate and pressure performance during emulsified acid: (<b>a</b>) Pumping emulsified acid treatment within the formation; (<b>b</b>) Pumping emulsified acid treatment within the formation.</p>
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<p>Real-time post-injectivity test recorded on field.</p>
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<p>Pair plots and correlation matrix using the input data.</p>
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<p>Prediction result using SVM in comparison with actual.</p>
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<p>Prediction result using GB in comparison with actual.</p>
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<p>Prediction result using Ridge in comparison with actual.</p>
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8 pages, 1440 KiB  
Proceeding Paper
Development of Lentil Aquafaba-Based Food Emulsions with Xanthan Gum or Pregelatinized Corn Starch as Stabilizers
by Valentyna Dehtiar, Anastasiia Sachko, Anna Radchenko, Olha Hrynchenko and Sergey Gubsky
Biol. Life Sci. Forum 2024, 40(1), 17; https://doi.org/10.3390/blsf2024040017 - 22 Jan 2025
Viewed by 10
Abstract
Currently, there is an increasing trend towards the use of legumes aquafaba-based emulsions for food applications. In this study, emulsions containing 30 and 60% sunflower oil with lentil aquafaba (LA) were developed, and xanthan or pregelatinized corn starch were added as stabilizers. Preliminary [...] Read more.
Currently, there is an increasing trend towards the use of legumes aquafaba-based emulsions for food applications. In this study, emulsions containing 30 and 60% sunflower oil with lentil aquafaba (LA) were developed, and xanthan or pregelatinized corn starch were added as stabilizers. Preliminary studies of lentil technological properties enabled the optimization of aquafaba production, achieving a dry matter content of 5.5% and a protein concentration of 1.1%. Emulsions with 0.5 and 0.8% aquafaba lentil protein without and with the addition of xanthan gum (0.1 and 0.2%) or starch (1 and 2%) were studied. Increasing the xanthan and starch content resulted in an increase in the average droplet size for emulsions with 30% oil and a decrease in the values for emulsions with 60% oil. For emulsions with a lower oil content, there was a visual instability over time with the addition of starch, which led to emulsion degradation. Rheological studies made it possible to classify the samples as a non-Newtonian fluid with a pseudoplastic flow pattern. The stability of the emulsions was observed due to an increase in the viscosity of the continuous phase due to the inclusion of the stabilizer. The influence of the nature of the stabilizer on this process is confirmed by calculations using various rheological models. Food emulsions obtained using lentil aquafaba are a promising ingredient in the development of emulsion food formulations. Full article
(This article belongs to the Proceedings of The 5th International Electronic Conference on Foods)
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<p>The particle volume-weighted size distribution: fresh lentil aquafaba, E30 and E60 emulsions.</p>
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<p>Viscosity of emulsion samples: viscosity curve in double logarithmic coordinates.</p>
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24 pages, 5157 KiB  
Article
Ceramic-Rich Composite Separators for High-Voltage Solid-State Batteries
by Kevin Vattappara, Martin Finsterbusch, Dina Fattakhova-Rohlfing, Idoia Urdampilleta and Andriy Kvasha
Batteries 2025, 11(2), 42; https://doi.org/10.3390/batteries11020042 - 21 Jan 2025
Viewed by 364
Abstract
Composite solid electrolytes are gaining interest regarding their use in Li-metal solid-state batteries. Although high ceramic content improves the electrochemical stability of ceramic-rich composite separators (C-SCE), the polymeric matrix also plays a vital role. In the first generation of C-SCE separators with a [...] Read more.
Composite solid electrolytes are gaining interest regarding their use in Li-metal solid-state batteries. Although high ceramic content improves the electrochemical stability of ceramic-rich composite separators (C-SCE), the polymeric matrix also plays a vital role. In the first generation of C-SCE separators with a PEO-based matrix, the addition of 90–95 wt% of Li6.45Al0.05La3Zr1.6Ta0.4O12 (LLZO) does not make C-SCE stable for cell cycling with high-voltage (HV) cathodes. For the next iteration, the objective was to find an HV-stable polymeric matrix for C-SCEs. Herein, we report results on optimizing C-SCE separators with different ceramics and polymers which can craft the system towards better stability with NMC622-based composite cathodes. Both LLZO and Li1.3Al0.3Ti1.7(PO4)3 (LATP) were utilized as ceramic components in C-SCE separators. Poly(diallyldimethylammonium) bis(trifluoromethanesulfonyl)imide (PDDA-TFSI) and poly (vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP) were used as polymers in the “polymer/LiTFSI/plasticizer”-based matrix. The initial phase of the selection criteria for the separator matrix involved assessing mechanical stability and ionic conductivity. Two optimized separator formulations were then tested for their electrochemical stability with both Li metal and HV composite cathodes. The results showed that Li/NMC622 cells with LP70_PVDF_HFP and LZ70_PDDA-TFSI separators exhibited more stable cycling performance compared to those with LZ90_PEO300k-based separators. Full article
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<p>Schematic description of strategy employed for development of high-voltage stable ceramic-rich solid separators. Note: abbreviations used in the scheme: LLZO—Li<sub>6.45</sub>Al<sub>0.05</sub>La<sub>3</sub>Zr<sub>1.6</sub>Ta<sub>0.4</sub>O<sub>12</sub>, LATP—Li<sub>1.3</sub>Al<sub>0.3</sub>Ti<sub>1.7</sub>(PO<sub>4</sub>)<sub>3</sub>, PVDF-HFP—poly (vinylidene fluoride-co-hexafluoropropylene), PDDA-TFSI—poly(diallyldimethylammonium)bis(trifluoromethanesulfonyl)imide, PBA—poly (1,4-butylene adipate), LiTFSI—lithium bis(trifluoromethanesulfonyl)imide, PYR<sub>14</sub>TFSI—1-butyl-1-methylpyrrolidinium bis(trifluoromethanesulfonyl)imide, and SCN—succinonitrile.</p>
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<p>Cross-sectional SEM images of fabricated C-SCEs comparing microstructures of different polymeric matrix groups, starting from PEO-matrix-based separators [<a href="#B32-batteries-11-00042" class="html-bibr">32</a>]: (<b>a</b>) LZ90_PEO300k and (<b>b</b>) LZ95_PEO300k; PVDF-HFP-matrix-based separators (<b>c</b>) LP70_PVDF-HFP and (<b>f</b>) LP70_PVDF-HFP without SCN, PBA-matrix-based separators (<b>d</b>) LZ70_PBA and (<b>e</b>) LZ80_PBA, and PDDA-TFSI-matrix-based separators (<b>g</b>) LZ70_PDDA-TFSI, (<b>h</b>) LZ80_PDDA-TFSI, and (<b>i</b>) LZ90_PDDA-TFSI.</p>
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<p>(<b>a</b>) Temperature-dependent ionic conductivity values for all the separators and (<b>b</b>) ionic conductivity of the investigated separators at 60 °C.</p>
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<p>(<b>a</b>) Critical current density test: voltage versus time profiles for different current densities in symmetric Li/Li cells for LP70_PVDF-HFP, LZ70_PDDA-TFSI, LZ90_PEO300k [<a href="#B32-batteries-11-00042" class="html-bibr">32</a>], and LZ95_PEO300k [<a href="#B32-batteries-11-00042" class="html-bibr">32</a>]; (<b>b</b>) voltage versus time profiles for long-term galvanostatic cycling of symmetric Li/Li cells with LP70_PVDF-HFP, LZ70_PDDA-TFSI, LZ90_PEO300k, and LZ95_PEO300k at current a density of 0.1 mA/cm<sup>2</sup> and half cycle step of 1 h with inset showing cycling profile shape of all separators. All measurements were performed at 60 °C.</p>
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<p>Results of floating test of Li/NMC622 cells with LP70_PVDF-HFP, LZ70_PDDA-TFSI, LZ90_PEO300k, and LZ95_PEO300k separators. The calculated NMC622 electrode area was 2.16 cm<sup>2</sup>. Conditions: 0.05C charge till 4.2 V, 1 h hold after each voltage increment of 0.1 V, 60 °C.</p>
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<p>Discharge profiles for discharge C-rate test for Li/NMC622 cells with (<b>a</b>) LZ90_PEO300k, (<b>b</b>) LP70_PVDF-HFP, and (<b>c</b>) LZ70_PDDA-TFSI separators. A summary of the discharge capacity values in Li/NMC622 cells with different separators after cycling (<b>d</b>) versus all cycle numbers to see the evolution of discharge capacity and (<b>e</b>) versus the C-rates used in the test without data from recovery cycle.</p>
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<p>(<b>a</b>) Discharge capacity and (<b>b</b>) coulombic efficiency versus cycle number of Li/NMC622 cells with all investigated separators. (<b>c</b>) Average voltage of both charge and discharge step for Li/NMC622 cells with different separators. Voltage versus capacity curves for Li/NMC622 cells with GEN 1 and GEN 2 separators after long-term galvanostatic cycling (<b>d</b>) LZ90_PEO300k for 35 cycles, (<b>e</b>) LZ70_PDDA-TFSI for 50 cycles and (<b>f</b>) LP70_PVDF-HFP for 50 cycles. dQ/dV versus voltage curves of the 1st and 10th cycles for Li/NMC622 cells with (<b>g</b>) LZ90_PEO300k, (<b>h</b>) LZ70_PDDA-TFSI, and (<b>i</b>) LP70_PVDF-HFP separators (red circle marking a peak with increased intensity).</p>
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<p>Comparative diagram of essential properties of GEN 1 and GEN 2 ceramic-rich composite electrolytes.</p>
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17 pages, 7457 KiB  
Article
Experimental Study of the Application of Calcined Shield Muck Powder as a Substitute for Fly Ash in Synchronous Tunnel Grouting Materials
by Wei Liu, Enfeng Wu, Hangyu Du, Hu Liu, Suyun Liu, Kangqi Chang and Yongqiang Li
Materials 2025, 18(3), 482; https://doi.org/10.3390/ma18030482 - 21 Jan 2025
Viewed by 245
Abstract
During shield tunnel construction, waste mud is a significant source of urban construction waste. However, the disposal of waste mud has always been a challenge in engineering. Addressing the challenge of harmlessly disposing of, or repurposing, mud cakes formed after pressure filtration of [...] Read more.
During shield tunnel construction, waste mud is a significant source of urban construction waste. However, the disposal of waste mud has always been a challenge in engineering. Addressing the challenge of harmlessly disposing of, or repurposing, mud cakes formed after pressure filtration of shield mud remains a pressing issue for many cities. To address the challenge of shield mud disposal and explore the utilization technology of this resource, this study focuses on shield mud obtained from the Shenzhen subway tunnel. Calcined shield mud powder (CSMP) was prepared by activating its potential pozzolanic properties through a calcination process. Compressive strength tests revealed that, while CSMP exhibits some pozzolanic activity, its performance is limited. When 30% of the cement is replaced, the mortar’s maximum strength activity index (SAI) is only 82.6%, which makes it unsuitable as a supplementary cementitious material for concrete applications. At the same time, CSMP was also evaluated as a partial replacement for fly ash in the formulation of synchronous grouting materials, with performance metrics including fluidity, bleeding rate, hardening rate, setting time, and compressive strength systematically tested. The experimental results showed that, while CSMP reduces the fluidity of grouting, it significantly improves volumetric stability, shortens setting time, and enhances mechanical performance. Compared to the fly ash used in the study, CSMP exhibited better pozzolanic reactivity, promoting the formation of C-S-H and C-A-S-H phases, optimizing the pore structure, and increasing the density and overall performance of the grouting material. When the substitution rate is below 60%, the performance of grouting meets standard requirements, indicating the strong feasibility of utilizing CSMP to replace fly ash in synchronous grouting materials. Full article
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<p>(<b>a</b>) Shield mud filtering production line; and (<b>b</b>) filtered muck cake.</p>
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<p>(<b>a</b>) Thermogravimetric analysis of SMP; and (<b>b</b>) XRD patterns.</p>
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<p>Appearance of shield muck and shield muck powder after grinding and calcination. (<b>a</b>) After grinding; (<b>b</b>) After calcination.</p>
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<p>Morphology of shield muck powder before and after calcination. (<b>a</b>) Before calcination; (<b>b</b>) After calcination.</p>
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<p>Preparation process of synchronous grouting materials.</p>
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<p>(<b>a</b>) Compressive strength; and (<b>b</b>) Flexural strength of mortar.</p>
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<p>SAI of mortars with different CSMP dosages and at different curing ages.</p>
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<p>RSI of mortar at different CSMP dosages and at different curing ages.</p>
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<p>Relation curve of fluidity with replacement of fly ash.</p>
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<p>Relation curve of volume stability with replacement of fly ash: (<b>a</b>) Bleeding rate; and (<b>b</b>) Hardening rate.</p>
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<p>Relation curve of: (<b>a</b>) setting time; and (<b>b</b>) compressive strength with replacement of fly ash.</p>
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<p>XRD patterns of 28 d Control and CSMP40% samples.</p>
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<p>Microscopic morphology of 28 d samples of (<b>a</b>) Control and (<b>b</b>) CSMP40%.</p>
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<p>Distribution of pore size of 28 d samples of (<b>a</b>) control and (<b>b</b>) CSMP40% by MIP technology.</p>
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<p>Proportion of different types of pores of 28 d samples of Control and CSMP40% observed by MIP technology.</p>
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27 pages, 1555 KiB  
Article
Easy and Straightforward FPGA Implementation of Model Predictive Control Using HDL Coder
by Marziye Purraji, Elyas Zamiri and Angel de Castro
Electronics 2025, 14(3), 419; https://doi.org/10.3390/electronics14030419 - 21 Jan 2025
Viewed by 299
Abstract
Model Predictive Control (MPC) is widely adopted for power electronics converters due to its ability to optimize system performance under dynamic constraints. However, its FPGA implementation remains challenging due to the complexity of Hardware Description Language (HDL) programming. This paper addresses this challenge [...] Read more.
Model Predictive Control (MPC) is widely adopted for power electronics converters due to its ability to optimize system performance under dynamic constraints. However, its FPGA implementation remains challenging due to the complexity of Hardware Description Language (HDL) programming. This paper addresses this challenge by introducing a straightforward methodology that simplifies FPGA implementation using MATLAB Simulink HDL Coder. It is shown that HDL Coder yields favorable synthesis outcomes, both in terms of area and time, compared to hand-coded HDL. Notably, the proposed method achieves a significantly reduced sampling step for the MPC algorithm—down to 32 ns—marking a substantial improvement over state-of-the-art implementations. The Integrated Logic Analyzer (ILA) IP available in the Vivado tool is used during the HIL testing phase to facilitate the real-time observation and analysis required for debugging and confirming the FPGA-implemented controller performance. Additionally, this paper discusses the advantages of utilizing HDL Coder for simplifying the FPGA programming process in power electronics applications and addresses the design challenges encountered using this methodology. Full article
(This article belongs to the Section Industrial Electronics)
18 pages, 1212 KiB  
Review
Advancing Nutritional Care Through Bioelectrical Impedance Analysis in Critical Patients
by Ana Maria Dumitriu, Cristian Cobilinschi, Bogdan Dumitriu, Sebastian Vâlcea, Raluca Ungureanu, Angela Popa, Rǎzvan Ene, Radu Țincu, Ioana Marina Grințescu and Liliana Mirea
Nutrients 2025, 17(3), 380; https://doi.org/10.3390/nu17030380 - 21 Jan 2025
Viewed by 358
Abstract
Nutritional support in critically ill patients has been acknowledged as a pillar of ICU care, playing a pivotal role in preserving muscle mass, supporting immune function, and promoting recovery during and after critical illness. Providing effective nutritional support requires adapting it to the [...] Read more.
Nutritional support in critically ill patients has been acknowledged as a pillar of ICU care, playing a pivotal role in preserving muscle mass, supporting immune function, and promoting recovery during and after critical illness. Providing effective nutritional support requires adapting it to the patient’s diagnosis, unique characteristics, and metabolic state to minimize the risks of overfeeding or underfeeding while mitigating muscle loss. This level of care requires a comprehensive nutritional assessment and the establishment of a nutrition-focused protocol. Regular, consistent and detailed nutritional evaluation can influence both therapeutic decisions and clinical interventions, thus ensuring that the specific needs of critically ill patients are met from the acute phase through their entire recovery process. Bioelectrical impedance analysis (BIA) is increasingly recognized as a valuable tool for enhancing nutritional care in critically ill patients. By delivering precise, real-time insights into key aspects of body composition, BIA is thought to provide clinicians with a more comprehensive understanding of the complex physiological changes that occur during critical illness. This narrative review highlights the potential of BIA in offering these precise assessments, facilitating the development of more accurate and personalized nutritional strategies for critically ill patients. If BIA can reliably assess dynamic shifts in hydration and tissue integrity, it holds the promise of further advancing individualized care and optimizing clinical outcomes in this vulnerable population. Full article
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<p>Multicompartment body composition model. FFM: fat-free mass, SLM: soft lean mass, BCM: body cell mass, ICW: intracellular water, ECW: extracellular water, TBW: total body water.</p>
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<p>Low-frequency currents do not penetrate cell membranes and measure extracellular water impedance. High-frequency currents also penetrate wall cells and measured impedance reflects total body water (TBW).</p>
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<p>Impedance components in bioelectrical impedance analysis (BIA): resistance, reactance, and phase angle.</p>
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27 pages, 984 KiB  
Article
Holistic Electric Powertrain Component Design for Battery Electric Vehicles in an Early Development Phase
by Nico Rosenberger, Silvan Deininger, Jan Koloch and Markus Lienkamp
World Electr. Veh. J. 2025, 16(2), 61; https://doi.org/10.3390/wevj16020061 - 21 Jan 2025
Viewed by 380
Abstract
As battery electric vehicles (BEVs) gain significance in the automotive industry, manufacturers must diversify their vehicle portfolios with a wide range of electric vehicle models. Electric powertrains must be designed to meet the unique requirements and boundary conditions of different vehicle concepts to [...] Read more.
As battery electric vehicles (BEVs) gain significance in the automotive industry, manufacturers must diversify their vehicle portfolios with a wide range of electric vehicle models. Electric powertrains must be designed to meet the unique requirements and boundary conditions of different vehicle concepts to provide satisfying solutions for their customers. During the early development phases, it is crucial to establish an initial powertrain component design that allows the respective divisions to develop their components independently and minimize interdependencies, avoiding time- and cost-intensive iterations. This study presents a holistic electric powertrain component design model, including the high-voltage battery, power electronics, electric machine, and transmission, which is meant to be used as a foundation for further development. This model’s simulation results and performance characteristics are validated against a reference vehicle, which was torn down and tested on a vehicle dynamometer. This tool is applicable for an optimization approach, focusing on achieving optimal energy consumption, which is crucial for the design of battery electric vehicles. Full article
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<p>Simulation framework of the electric powertrain component design process.</p>
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<p>The four most common single-speed transmission topologies [<a href="#B51-wevj-16-00061" class="html-bibr">51</a>]. The numbers reference the shaft number, and the letters represent the differential (D), sun gear (s), planet gears (p), and the ring gear (r).</p>
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<p>Electric machine layout concepts from Motor-CAD. (<b>a</b>) asynchronous motor and (<b>b</b>) permanent magnet synchronous motor layout.</p>
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<p>SOC behavior between the dynamometer test and simulation on vehicle level.</p>
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<p>Efficiency behavior between the dynamometer test and simulation of the battery module.</p>
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<p>Simulation results of single parameter configurations evaluated against the energy consumption on vehicle level. (<b>a</b>) shows the achieved range, in (<b>b</b>) different gear ratios are displayed, (<b>c</b>) evaluates the vehicle mass, and in (<b>d</b>) the achieved top speed is considered.</p>
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<p>Efficiency maps of vehicle concepts designed within the simulation framework with the load points converted of the selected WLTC. (<b>a</b>) Efficiency map of vehicle 1 and (<b>b</b>) of vehicle 4.</p>
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12 pages, 5451 KiB  
Article
Thermal Analysis Kinetics and Luminescence Properties of Y2O3-Coated MgO: Ce+3 Particles
by Quanqing Zhang, Weimin Ma, Lijie He, Guanglei Tan, Yang Lu and Nan Wu
Coatings 2025, 15(2), 122; https://doi.org/10.3390/coatings15020122 - 21 Jan 2025
Viewed by 332
Abstract
Y2O3-coated MgO: Ce+3 particles with different precipitants were prepared by the co-precipitation method; the phase and morphology of the sample were characterized by XRD, TEM, and DTA-TG, and the apparent activation energy of the coated particles was studied [...] Read more.
Y2O3-coated MgO: Ce+3 particles with different precipitants were prepared by the co-precipitation method; the phase and morphology of the sample were characterized by XRD, TEM, and DTA-TG, and the apparent activation energy of the coated particles was studied by thermal analysis kinetics. The results showed that the precursors synthesized by single-phase and multi-phase precipitants were calcined at 1000 °C for 1.5 h to obtain Y2O3-coated MgO: Ce+3 particles with coating thicknesses of about 2.5 nm and 5 nm. The apparent activation energies of the precursor phase change in three stages were calculated using the Doyle–Ozawa method and the Kissinger method. The average values for single-phase samples were 95.61, 74.90, and 275.27 kJ/mol, while those for multi-phase samples were 74.90, 56.06, and 240.14 kJ/mol. The activation energies for the grain growth of the two samples were 30.56 kJ/mol and 26.27 kJ/mol. Due to the differences in activation energies at each reaction stage, the reason for the influence on the thickness of the coating layer of the two precipitants is that the smaller the activation energy, the lower the required synthesis energy. An increase in coating thickness indicates an improvement in the surface activity of the coated particles. Moreover, the luminescence intensity of the composite sample is significantly higher than that of the single-phase sample, and the luminescence performance is optimal when the Ce+3 ion in the composite sample is 0.3 mol%. Full article
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<p>XRD patterns of samples prepared with single-phase (<b>a</b>) and composite (<b>b</b>) precipitants at different calcination temperatures for 1.5 h.</p>
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<p>TEM morphology of single-phase precipitant (<b>a</b>) and composite precipitant (<b>b</b>) samples calcined at 1000 °C for 1.5 h.</p>
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<p>DTA-TG curves of precursors of single-phase (<b>a</b>,<b>b</b>) and composite (<b>c</b>,<b>d</b>) precipitants at different heating rates.</p>
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<p>(<b>a</b>–<b>c</b>) <span class="html-italic">lgβ</span> − 1/T plot of endothermic peak of single-phase precipitant sample calculated by the Doyle–Ozawa method.</p>
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<p>(<b>a</b>–<b>c</b>) The <span class="html-italic">lgβ</span> − 1/T plot of the endothermic peak of the composite precipitant sample calculated by the Doyle–Ozawa method.</p>
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<p>ln (β/T<sub>m</sub><sup>2</sup>) − 1/T<sub>m</sub> plots of the endothermic peaks of the precursors of single-phase (<b>a</b>) and composite (<b>b</b>) precipitants at different heating rates.</p>
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<p>ln<span class="html-italic">D</span> and 1/<span class="html-italic">T</span> relationship curves of MgO:Ce<sup>+3</sup> particles obtained from two precipitants.</p>
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<p>Excitation and emission spectra of composite precipitant sample (<b>a</b>) and single-phase precipitant sample (<b>b</b>).</p>
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<p>Excitation spectrum curves (<b>a</b>) and characteristic peak intensity curves (<b>b</b>) of composite precipitant samples with different Ce<sup>3+</sup> mol% contents.</p>
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<p>Emission spectra of composite precipitant samples with different Ce<sup>+3</sup> mol% contents under excitation at 393 nm (<b>a</b>) and 445 nm (<b>b</b>) wavelengths.</p>
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27 pages, 7928 KiB  
Article
A Novel Solar Rooftop Agriculture System Integrated with CNT Nanofluid Spectral Splitter for Efficient Food Production
by Wei Wei, Jiayi Luo, Yiyu Shi, Chenlei Yu, Niansi Li, Jie Ji and Bendong Yu
Buildings 2025, 15(3), 314; https://doi.org/10.3390/buildings15030314 - 21 Jan 2025
Viewed by 276
Abstract
Traditional rooftop greenhouses offer a promising solution for urban vegetable supply but have the disadvantages of overheating during the daytime and supercooling during the nighttime. To address these issues, a novel solar greenhouse system using nanofluid spectral splitting and phase change materials (NSS-PCMs) [...] Read more.
Traditional rooftop greenhouses offer a promising solution for urban vegetable supply but have the disadvantages of overheating during the daytime and supercooling during the nighttime. To address these issues, a novel solar greenhouse system using nanofluid spectral splitting and phase change materials (NSS-PCMs) was developed. In this study, a 75-day thermal environment test experiment was conducted on the novel solar greenhouse, and the growth status and nutrient composition of three typical plants were evaluated. By optimizing the greenhouse structure parameters through the model, over 80% of 300–800 nm wavelengths for vegetable photosynthesis were transmitted to the greenhouse, while the remaining spectrum was used for heat storage to maintain warmth during nighttime. The novel solar greenhouse reduced daytime temperatures by 5.2 °C and increased nighttime temperatures by 6.9 °C, reaching a maximum thermal efficiency of 53.4% compared to traditional greenhouses. The 75-day temperature detection showed that optimal temperature ranges were maintained for approximately 60 days, both during daytime and nighttime, with an 80% assurance rate. The growth rates of three vegetables in the novel solar greenhouse improved by 55%, 35%, and 40%, and the nutrient composition doubled compared to the control group. Full article
(This article belongs to the Section Building Energy, Physics, Environment, and Systems)
Show Figures

Figure 1

Figure 1
<p>The concept and structure diagram of a solar greenhouse with NSS-PCMs.</p>
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<p>The thermal model of the NSS-PCM system during daytime (<b>a</b>) and nighttime (<b>b</b>), the temperature difference during the daytime (<b>c</b>), and the increase in temperature difference during nighttime (<b>d</b>).</p>
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<p>The model (<b>a</b>), the digital representation (<b>b</b>) and the side (<b>c</b>) and front (<b>d</b>) of the solar greenhouse with NSS-PCMs.</p>
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<p>Model for the thermal model system.</p>
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<p>The calculation process for the thermal model system.</p>
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<p>The weather parameters (<b>a</b>), comparison of greenhouse indoor air and outside ambient temperature (<b>b</b>), the temperature of PCMs (<b>c</b>), the photothermal conversion efficiency and thermal efficiency (<b>d</b>), the heat gain of nanofluids and PCMs during daytime (<b>e</b>), and the light intensity distribution inside the greenhouse (<b>f</b>).</p>
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<p>The average transmittance of light (<b>a</b>) and transmittance at 9:00 (<b>b</b>), 12:00 (<b>c</b>), and 17:00 (<b>d</b>).</p>
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<p>The temperature of the glass cover (<b>a</b>), glass plate (<b>b</b>), aluminum plate on the inner wall of the PCM container (<b>c</b>), and the R<sup>2</sup> of other parts (<b>d</b>).</p>
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<p>Comparison of indoor air temperature (<b>a</b>), PCM temperature (<b>b</b>), thermal efficiency (<b>c</b>), and heat gain (<b>d</b>) of three different PCM layer thicknesses after optimization.</p>
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<p>Comparison of indoor air (<b>a</b>) and PCM temperature (<b>b</b>) after optimization and thermal efficiency (<b>c</b>) of the system of three different phase transition temperatures and comparison of indoor air in two solar greenhouse systems (<b>d</b>).</p>
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<p>The outdoor parameters (<b>a</b>) and comparison of indoor and outdoor air temperature of the novel greenhouse (<b>b</b>).</p>
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<p>The indoor and outdoor temperature changes of the novel rooftop greenhouse during daytime and nighttime from 16 March to 20 March (<b>a</b>), 9 April to 13 April (<b>b</b>), 29 April to 3 May (<b>c</b>), and 12 May to 16 May (<b>d</b>).</p>
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<p>Comparison of growth status (<b>a</b>) and height of purslane (<b>b</b>), asparagus (<b>c</b>), and lettuce (<b>d</b>) between experimental and control groups.</p>
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<p>The content of trace elements of purslane (<b>a</b>) and lettuce (<b>b</b>) and the organic content of purslane (<b>c</b>) and lettuce (<b>d</b>) in vegetables of the experimental and control groups.</p>
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<p>Experimental diagram of each part of the vegetable (<b>a</b>) and comparison of fresh weight (<b>b</b>), dry weight (<b>c</b>), and solid content (<b>d</b>) of each part of vegetables in the experimental and control groups.</p>
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