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17 pages, 19751 KiB  
Article
Mo-Doped Co3O4 Nanostructures for Enhanced N-Butanol Sensing Performance
by Yanping Chen, Guangfeng Zhang, Jing Ren, Haoyang Xu and Yonghui Jia
Chemosensors 2025, 13(2), 61; https://doi.org/10.3390/chemosensors13020061 (registering DOI) - 8 Feb 2025
Abstract
In this work, Mo-doped Co3O4 nanostructures were synthesized through a simple solvothermal method. To characterize the structures of the pure Co3O4 and Mo-doped Co3O4 samples, a variety of analytical techniques, such as XRD, SAED, [...] Read more.
In this work, Mo-doped Co3O4 nanostructures were synthesized through a simple solvothermal method. To characterize the structures of the pure Co3O4 and Mo-doped Co3O4 samples, a variety of analytical techniques, such as XRD, SAED, TEM, SEM and XPS, were utilized. The analysis of the gas sensing performance indicated that the 1 at% Mo-doped Co3O4 sensor exhibited optimal sensing performance for low concentrations of n-butanol, achieving a notable Rg/Ra ratio of 9.53 at 10 ppm at a lower operating temperature of 150 °C. This performance was approximately four times that of pure Co3O4, with a response time of 81 s and a recovery time of 66 s. Additionally, the sensor also exhibited outstanding gas selectivity and repeatability. The incorporation of Mo significantly improved the catalytic activity and sensitivity of Co3O4, primarily due to the increased formation of oxygen vacancies and the modification of the electronic structure. These changes facilitated more efficient gas adsorption and faster response times. Therefore, the Mo-doped Co3O4 sensor exhibits considerable potential for detecting n-butanol gas. Full article
(This article belongs to the Special Issue Nanomaterial-Based Chemosensors and Biosensors for Smart Sensing)
28 pages, 26850 KiB  
Article
Deep Learning Utilization for In-Line Monitoring of an Additive Co-Extrusion Process Based on Evaluation of Laser Profiler Data
by Valentin Lang, Christian Thomas Ernst Herrmann, Mirco Fuchs and Steffen Ihlenfeldt
Appl. Sci. 2025, 15(4), 1727; https://doi.org/10.3390/app15041727 (registering DOI) - 8 Feb 2025
Viewed by 91
Abstract
Additive manufacturing is gaining importance in a number of application areas, and there is an increased demand for mechanically resilient components. A way to improve the mechanical properties of parts made of thermoplastics is by using reinforcing material. The study demonstrates the development [...] Read more.
Additive manufacturing is gaining importance in a number of application areas, and there is an increased demand for mechanically resilient components. A way to improve the mechanical properties of parts made of thermoplastics is by using reinforcing material. The study demonstrates the development of a monitoring procedure for a fused filament fabrication-based co-extrusion process for manufacturing wire-reinforced thermoplastic components. Test components in two variants are produced, and data acquisition is carried out with a laser line scanner. The collected data are employed to train deep neural networks to classify the printed layers, aiming for the deep neural networks to be able to classify four different classes and identify layers with insufficient quality. A dedicated convolutional neural network is designed taking into account various factors such as layer architecture, data pre-processing and optimization methods. Several network architectures, including transfer learning (based on VGG16 and ResNet50), with and without fine-tuning, are compared in terms of their performance based on the F1 score. Both the transfer learning model with ResNet50 and the fine-tuning model achieve an F1 score of 84% and 83%, respectively, for the decisive class ‘wire bad’ classifying inadequate reinforcement. Full article
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Figure 1
<p>Setup of the experimental equipment consisting of a 3-axis machine platform with a co-extrusion head for wire-reinforced thermoplastics strand deposition.</p>
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<p>Flowchart of an in situ monitoring routine based on classification of height information of printed layers using convolutional neural networks.</p>
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<p>Display of all part configurations of the components in the four distinguished classes ‘solid’, ‘infill’, ‘wire good’ and ‘wire bad’ (visualization based on scanned, unprocessed data).</p>
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<p>(<b>a</b>) Raw data file: all height measurement values recorded with laser line scanner in a CSV. (<b>b</b>) Area of interest: area specified via the interface. (<b>c</b>) Pre-processed data: output file before splitting into patches. (<b>d</b>) Processed output: split patches (numbers 1–9) in format 224 × 224 pixels appropriate for model learning.</p>
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<p>(<b>a</b>) Serial color coding of the normalized CSV data using the height information. (<b>b</b>) Coding of the height information in two channels parallel to each other. (<b>c</b>) Example image output dataset, (<b>d</b>) Example image serial coding. (<b>e</b>) Example image parallel coding.</p>
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<p>Top-layer architecture of the employed transfer learning models.</p>
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<p>Training progress for learning rates <math display="inline"><semantics> <mrow> <mn>1</mn> <mo>×</mo> <msup> <mn>10</mn> <mrow> <mo>−</mo> <mn>4</mn> </mrow> </msup> </mrow> </semantics></math>, <math display="inline"><semantics> <mrow> <mn>1</mn> <mo>×</mo> <msup> <mn>10</mn> <mrow> <mo>−</mo> <mn>5</mn> </mrow> </msup> </mrow> </semantics></math>, and <math display="inline"><semantics> <mrow> <mn>1</mn> <mo>×</mo> <msup> <mn>10</mn> <mrow> <mo>−</mo> <mn>6</mn> </mrow> </msup> </mrow> </semantics></math> for the ResNet50 model with (<b>a</b>) dataset 1 (seed 456) and (<b>b</b>) with dataset 2 (seed 456).</p>
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<p>(<b>a</b>) Validation accuracy and (<b>b</b>) validation loss as metrics for the training progress of the fine-tuning models.</p>
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<p>Confusion matrix of the FT3 model for seed 42.</p>
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<p>Misclassifications regarding the corresponding images from the dataset illustrating deficiencies in effectiveness of proposed method: (<b>a</b>) true: infill, prediction: wire bad, (<b>b</b>) true: wire bad, prediction: infill, (<b>c</b>) true: wire good, prediction: infill, (<b>d</b>) true: wire good, prediction: infill, (<b>e</b>) true: infill, prediction: wire good, (<b>f</b>) true: wire good, prediction: infill, (<b>g</b>) true: infill, prediction: wire good, and (<b>h</b>) true: wire bad, prediction: infill.</p>
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23 pages, 4213 KiB  
Review
Li-Ion Batteries for Electric Vehicle Applications: An Overview of Accurate State of Charge/State of Health Estimation Methods
by Adolfo Dannier, Gianluca Brando, Mattia Ribera and Ivan Spina
Energies 2025, 18(4), 786; https://doi.org/10.3390/en18040786 (registering DOI) - 8 Feb 2025
Viewed by 143
Abstract
Road transport significantly contributes to greenhouse gas emissions in all places where it is used and therefore also in Europe, prompting the EU to set ambitious objectives for CO2 reduction. In order to reach these objectives, the automotive industry is transitioning to [...] Read more.
Road transport significantly contributes to greenhouse gas emissions in all places where it is used and therefore also in Europe, prompting the EU to set ambitious objectives for CO2 reduction. In order to reach these objectives, the automotive industry is transitioning to electric vehicles, utilizing electric powertrains powered by battery packs. However, the longevity and reliability of these batteries are critical concerns. This review paper focuses on the advanced diagnostic techniques for effective battery State of Charge (SoC) and State of Health (SoH) monitoring. Accurate SoC/SoH estimation is crucial for optimizing battery performance, avoiding premature degradation, and ensuring driver safety. By investigating these areas, this paper aims to contribute to the development of more sustainable and durable electric vehicles, supporting the transition to cleaner transportation systems. Full article
(This article belongs to the Collection "Electric Vehicles" Section: Review Papers)
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<p>Block scheme of a pure EV powertrain.</p>
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<p>BMS block diagram.</p>
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<p>N-time constant models.</p>
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<p>Randles model.</p>
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<p>Partnership for a New Generation of Vehicles (PNGV) model.</p>
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<p>Schematic of a DFN model.</p>
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<p>Schematic of an SPM.</p>
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<p>Overview of the primary SoC/SoH estimation methodology.</p>
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<p>Step-by-step illustration of the Coulomb Counting estimation method.</p>
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<p>Overview of model-based methods for SoC estimation.</p>
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<p>General scheme of data-driven SoC estimation using pre-trained models.</p>
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<p>List of common data-driven methods tested for SoC and SoH estimation.</p>
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20 pages, 1991 KiB  
Article
Heuristic Guidelines for Developing Polymer/Ionic Liquid Blend Membranes
by Paola Bernardo and Gabriele Clarizia
Polymers 2025, 17(4), 439; https://doi.org/10.3390/polym17040439 - 7 Feb 2025
Viewed by 228
Abstract
In the search of increasingly effective materials for enhancing gas transport in membranes, the incorporation of ionic liquids within a polymeric matrix is attracting a lot of interest in the development of advanced membranes to be applied to CO2 separation. An analysis [...] Read more.
In the search of increasingly effective materials for enhancing gas transport in membranes, the incorporation of ionic liquids within a polymeric matrix is attracting a lot of interest in the development of advanced membranes to be applied to CO2 separation. An analysis of the open literature focusing on polymer/IL blend membranes, in which a polymer matrix hosts an ionic liquid, was carried out, showing the effects of different composition dependences on CO2 permeability. The peculiar permeability profiles were attributed to the specific interactions established between the ionic liquid and the polymer matrix rather than to the state of the polymer matrix. Hansen’s solubility parameters were considered to represent CO2 transport in polymer/IL blend membranes by linking them to interactions between the ionic liquid and the polymer matrix. Through an appropriate rearrangement of the solubility parameters, 2D maps were utilized as an immediate and easy tool to identify the best polymer/ionic liquid combination before even performing laboratory experiments. Full article
(This article belongs to the Section Polymer Applications)
20 pages, 3628 KiB  
Article
In Vitro Investigation of the Effects of Bacillus subtilis-810B and Bacillus licheniformis-809A on the Rumen Fermentation and Microbiota
by Raphaële Gresse, Bruno Ieda Cappellozza, Didier Macheboeuf, Angélique Torrent, Jeanne Danon, Lena Capern, Dorthe Sandvang, Vincent Niderkorn, Giuseppe Copani and Evelyne Forano
Animals 2025, 15(4), 476; https://doi.org/10.3390/ani15040476 - 7 Feb 2025
Viewed by 314
Abstract
Direct-fed microbials (DFMs) have shown the potential to improve livestock performance and overall health. Extensive research has been conducted to identify new DFMs and understand their mechanisms of action in the gut. Bacillus species are multifunctional spore-forming bacteria that exhibit resilience to harsh [...] Read more.
Direct-fed microbials (DFMs) have shown the potential to improve livestock performance and overall health. Extensive research has been conducted to identify new DFMs and understand their mechanisms of action in the gut. Bacillus species are multifunctional spore-forming bacteria that exhibit resilience to harsh conditions, making them ideal candidates for applications in the feed industry and livestock production. This study investigates the mode of action of B. licheniformis and B. subtilis in the rumen using diverse in vitro techniques. Our results revealed that both strains germinated and grew in sterile rumen and intestinal contents from dairy cows and bulls. Gas composition analysis of in vitro cultures in a medium containing 40% rumen fluid demonstrated that germination of B. licheniformis and B. subtilis strains reduced oxygen levels, promoting an anaerobic environment favorable to rumen microbes. Enzymatic activity assays showed that B. licheniformis released sugars from complex substrates and purified polysaccharides in filtered rumen content. Additionally, the combination of B. licheniformis and B. subtilis survived and grew in the presence of a commercial monensin dose in rumen fluid media. The effects of B. licheniformis and B. subtilis on rumen fermentation activity and microbiota were studied using an in vitro batch fermentation assay. In fermenters that received a combination of B. licheniformis and B. subtilis, less CO2 was produced while dry matter degradation and CH4 production was comparable to the control condition, indicating better efficiency of dry matter utilization by the microbiota. The investigation of microbiota composition between supplemented and control fermenters showed no significant effect on alpha and beta diversity. However, the differential analysis highlighted changes in several taxa between the two conditions. Altogether, our data suggests that the administration of these strains of Bacillus could have a beneficial impact on rumen function, and consequently, on health and performance of ruminants. Full article
(This article belongs to the Section Cattle)
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<p>Growth of <span class="html-italic">B. subtilis</span> and <span class="html-italic">B. licheniformis</span> in digestive content, rumen juice and a rich medium containing 40% of rumen fluid (Mean OD 600 nm ± standard deviation).</p>
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<p>Co-incubation of <span class="html-italic">B. licheniformis</span> and <span class="html-italic">B. subtilis</span> (Bovacillus) with an in-feed commercial dose of monensin (“CTRL” = control condition without bacterial treatment) (Mean OD 600 nm ± standard deviation).</p>
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<p>Oxygen percentage in the rumen-containing medium before inoculation (t = 0) and after 24 h incubation (t = 24) of spores of <span class="html-italic">B. licheniformis</span> (green bars) and <span class="html-italic">B. subtilis</span> (blue bars) (Mean percentage of oxygen ± standard deviation).</p>
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<p>Concentration of released reducing sugars after consumption of complex and purified substrates by <span class="html-italic">Bacillus</span> strains cultivated in rich medium containing 40% rumen fluid.</p>
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<p>Short fatty acids relative abundance (%) produced by fermentation activity of the in vitro rumen microbiota in the control and <span class="html-italic">Bacillus</span> condition after 8 or 24 h of fermentation (“CTRL” = control condition without bacterial treatment).</p>
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<p>(<b>a</b>) Relative abundance of neutral detergent fibers (NDF) remaining in the fermentation media, (<b>b</b>) total “TOT” gas produced in the atmosphere of batch rumen fermenters after 8 h of fermentation, (<b>c</b>) hydrogen “H<sub>2</sub>” in the atmosphere of batch rumen fermenters after 8 h of fermentation, (<b>d</b>) carbon dioxide “CO<sub>2</sub>” in the atmosphere of batch rumen fermenters after 8 h of fermentation (“CTRL” = control condition without bacterial treatment). The conditions sharing the same letters are not significantly different from each other (<span class="html-italic">p</span> &gt; 0.05).</p>
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<p>Significantly differentially abundant ASVs after 8 h (<b>a</b>) and 24 h (<b>b</b>) of fermentation in the <span class="html-italic">Bacillus</span> treatments compared to the control condition highlighted using the METACODER R package. “Bovacillus” corresponds to the cocktail of <span class="html-italic">B. subtilis</span> and <span class="html-italic">B. licheniformis.</span> Positive values relate to taxa more abundant in the <span class="html-italic">Bacillus</span> treatment while negative values relate to taxa more abundant in the control condition (“CTRL”).</p>
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<p>Count of <span class="html-italic">S</span>. Typhimurium after 24 h of co-incubation with a mixture of <span class="html-italic">B. licheniformis</span> and <span class="html-italic">B. subtilis</span> (Bovacillus) or alone as a control condition (“CTRL”). *** <span class="html-italic">p</span> value &lt; 0.0001.</p>
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23 pages, 9524 KiB  
Article
Novel AlCo2O4/MWCNTs Nanocomposites for Efficient Degradation of Reactive Yellow 160 Dye: Characterization, Photocatalytic Efficiency, and Reusability
by Junaid Ahmad, Amir Ikhlaq, Muhammad Raashid, Uzma Ikhlaq, Umair Yaqub Qazi, Hafiz Tariq Masood, Tousif Hussain, Mohsin Kazmi, Naveed Ramzan, Asma Naeem, Ashraf Aly Hassan, Fei Qi and Rahat Javaid
Catalysts 2025, 15(2), 154; https://doi.org/10.3390/catal15020154 - 7 Feb 2025
Viewed by 264
Abstract
The purpose of this work was to consider the decolorization efficiency of reactive yellow 160 (Ry-160) dye utilizing cobalt aluminum oxide (AlCo2O4)-anchored Multi-Walled Carbon Nanotubes (AlCo2O4/MWCNTs) nanocomposites as catalysts for the first time in a [...] Read more.
The purpose of this work was to consider the decolorization efficiency of reactive yellow 160 (Ry-160) dye utilizing cobalt aluminum oxide (AlCo2O4)-anchored Multi-Walled Carbon Nanotubes (AlCo2O4/MWCNTs) nanocomposites as catalysts for the first time in a photocatalytic process under natural sunlight irradiation. The compositional, morphological, and functional group analyses of AlCo2O4 and AlCo2O4/MWCNTs were performed by utilizing Energy Dispersive Spectroscopy (EDS), Field Emission Scanning Electron Microscopy (FE-SEM), and Fourier Transform Infrared (FTIR) Spectroscopy, respectively. A UV-Vis (UV-Vis) spectrophotometer was used to investigate degradation efficiency. The results exhibited a reduction in the optical bandgap for AlCo2O4/MWCNTs nanocomposites as catalysts from 1.5 to 1.3 eV compared with pure spinel AlCo2O4 nanocomposites. AlCo2O4/MWCNTs nanocomposites showed excellent photocatalytic behavior, and around 96% degradation of Ry-160 dye was observed in just 20 min under natural sunlight, showing first-order kinetics with rate constant of 0.151 min−1. The results exhibited outstanding stability and reusability for AlCo2O4/MWCNTs by maintaining more than 90% photocatalytic efficiency even after seven successive operational cycles. The betterment of the photocatalytic behavior of AlCo2O4/MWCNTs nanocomposites as compared to AlCo2O4 nanocomposites owes to the first-rate storage capacity of electrons in MWCNTs, due to which the catalyst became an excellent electron acceptor. Furthermore, the permeable structure of MWCNTs results in a greater surface area leading to the onset of more active sites, and, in turn, it also boosts conductivity and reduces the formation of agglomerates on the surface of catalysts, which inhibits e−/h+ pair recombination. Concisely, the synthesis of a novel AlCo2O4/MWCNTs catalyst with excellent and fast photocatalytic activity was the aim of this study. Full article
(This article belongs to the Special Issue Photocatalysis towards a Sustainable Future)
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Figure 1
<p>Steps in the coprecipitation method for the synthesis of spinal AlCo<sub>2</sub>O<sub>4</sub> nanocomposites.</p>
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<p>EDX analysis of (<b>a</b>) AlCo<sub>2</sub>O<sub>4</sub> and (<b>b</b>) AlCo<sub>2</sub>O<sub>4</sub>/MWCNs nanocomposites.</p>
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<p>FESEM images for (<b>a</b>,<b>c</b>) pristine spinel AlCo<sub>2</sub>O<sub>4</sub> nanocomposite and (<b>b</b>,<b>d</b>) AlCo<sub>2</sub>O<sub>4</sub>-anchored MWCNTs nanocomposites.</p>
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<p>FTIR spectra for (<b>a</b>) aluminum cobaltite and (<b>b</b>) aluminum cobaltite-anchored MWCNTs.</p>
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<p>UV-Vis absorption spectra for (<b>a</b>) AlCo<sub>2</sub>O<sub>4</sub> and (<b>b</b>) AlCo<sub>2</sub>O<sub>4</sub>/MWCNTs.</p>
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<p>Tauc plot for (<b>a</b>) AlCo<sub>2</sub>O<sub>4</sub> nanocomposite and (<b>b</b>) AlCo<sub>2</sub>O<sub>4</sub>/MWCNTs nanocomposite.</p>
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<p>Photodegradation spectra of (<b>a</b>) spinel AlCo<sub>2</sub>O<sub>4</sub> nanocomposite annealed at 300 °C and (<b>b</b>) spinel AlCo<sub>2</sub>O<sub>4</sub>/MWCNs nanocomposite annealed at 300 °C.</p>
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<p>Photodegradation results of AlCo<sub>2</sub>O<sub>4</sub> as compared with AlCo<sub>2</sub>O<sub>4</sub>/MWCNs nanocomposite.</p>
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<p>(<b>a</b>) Effect of different pH values on the color removal efficiency of catalyst (dye concentration: 20 ppm, AlCo<sub>2</sub>O<sub>4</sub> amount: 125 mg) and (<b>b</b>) effect of different pH values on the color removal efficiency of catalyst (dye concentration: 20 ppm, AlCo<sub>2</sub>O<sub>4</sub>/MWCNs amount: 125 mg).</p>
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<p>Effect of temperature on removal efficiency of color for (<b>a</b>) AlCo<sub>2</sub>O<sub>4</sub> and (<b>b</b>) AlCo<sub>2</sub>O<sub>4</sub>/MWCNs (dye concentration = 20 ppm, pH = 6).</p>
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<p>(<b>a</b>) Effect of AlCo<sub>2</sub>O<sub>4</sub> dose on color removal efficiency (dye concentration: 20 ppm, pH = 6). (<b>b</b>) Effect of AlCo<sub>2</sub>O<sub>4</sub>/MWCNs dose on color removal efficiency (dye concentration: 20 ppm, pH = 6).</p>
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<p>Effect of initial dye concentration on degradation of dye using (<b>a</b>) AlCo<sub>2</sub>O<sub>4</sub> (amount: 150 mg, pH = 6) and (<b>b</b>) AlCo<sub>2</sub>O<sub>4</sub>/MWCNs (amount: 150 mg, pH = 6).</p>
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<p>Effect of using NaHCO<sub>3</sub> quencher on degradation of dye.</p>
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<p>−ln C/Co vs. time plot for pseudo first order kinetics.</p>
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<p>(<b>a</b>) Proposed mechanism of photocatalysis in combined catalyst AlCo<sub>2</sub>O<sub>4</sub>/MWCNTs, (<b>b</b>) energy level model of AlCo<sub>2</sub>O<sub>4</sub>/MWCNTs for the explanation of better electron transfer, (<b>c</b>) existence and direction of electric field between NiCo<sub>2</sub>O<sub>4</sub> and MWCNTs.</p>
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<p>Cyclic photodegradation of Ry-160 irradiated under sunlight by seven separate-wash-dry cycles for reprocessing the same catalyst.</p>
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20 pages, 3963 KiB  
Article
NE-MTOC Formation in Skeletal Muscle Is Mbnl2-Dependent and Occurs in a Sequential and Gradual Manner
by Payel Das, Robert Becker, Silvia Vergarajauregui and Felix B. Engel
Cells 2025, 14(4), 237; https://doi.org/10.3390/cells14040237 - 7 Feb 2025
Viewed by 841
Abstract
Non-centrosomal microtubule-organizing centers (ncMTOCs) are important for the function of differentiated cells. Yet, ncMTOCs are poorly understood. Previously, several components of the nuclear envelope (NE)-MTOC have been identified. However, the temporal localization of MTOC proteins and Golgi to the NE and factors controlling [...] Read more.
Non-centrosomal microtubule-organizing centers (ncMTOCs) are important for the function of differentiated cells. Yet, ncMTOCs are poorly understood. Previously, several components of the nuclear envelope (NE)-MTOC have been identified. However, the temporal localization of MTOC proteins and Golgi to the NE and factors controlling the switch from a centrosomal MTOC to a ncMTOC remain elusive. Here, we utilized the in vitro differentiation of C2C12 mouse myoblasts as a model system to study NE-MTOC formation. We find based on longitudinal co-immunofluorescence staining analyses that MTOC proteins are recruited in a sequential and gradual manner to the NE. AKAP9 localizes with the Golgi to the NE after the recruitment of MTOC proteins. Moreover, siRNA-mediated depletion experiments revealed that Mbnl2 is required for proper NE-MTOC formation by regulating the expression levels of AKAP6β. Finally, Mbnl2 depletion affects Pcnt isoform expression. Taken together, our results shed light on how mammals post-transcriptionally control the switch from a centrosomal MTOC to an NE-MTOC and identify Mbnl2 as a novel modulator of ncMTOCs in skeletal muscle cells. Full article
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Figure 1
<p>Nesprin-1α is observed at the NE before AKAP6. (<b>a</b>) Immunofluorescence analysis of C2C12 differentiated for 2 days showing co-staining for nesprin-1 (red) and AKAP6 (green). Note that nesprin-1<sup>+</sup>/AKAP6<sup>+</sup> nuclei are indicated by yellow arrows and nesprin-1<sup>+</sup>/AKAP6<sup>−</sup> nuclei are indicated by yellow asterisks. Scale bar: 20 µm. (<b>b</b>) Quantitative analysis of (<b>a</b>). <span class="html-italic">n</span> = 3 per <span class="html-italic">n</span> &gt; 500 nuclei. Data: mean ± SD. (<b>c</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing a gradient in the signal intensity of nesprin-1 and AKAP6. The edges of the surface covered by each protein are indicated with a colored line: red: nesprin-1; green: AKAP6. Scale bar: 10 µm.</p>
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<p>PCM1 is recruited to the NE after the anchor platform is established. (<b>a</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing two examples of co-staining for AKAP6 (green) and PCM1 (red). The yellow arrow represents the higher signal intensity of AKAP6 at the NE where PCM1 is recruited. Scale bar: 10 µm. (<b>b</b>) Quantitative analysis of (<b>a</b>). <span class="html-italic">n</span> = 3 per <span class="html-italic">n</span> &gt; 500 nuclei. Data: mean ± SD.</p>
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<p>MTOC proteins do not appear to be localized to the NE in a complex with PCM1. (<b>a</b>,<b>c</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing two examples of co-staining of PCM1 (red) with Pcnt (green) (<b>a</b>) or CDKRAP2 (green) (<b>c</b>). Yellow asterisk: nuclear region proximal to the centrosome. (<b>b</b>,<b>d</b>) Quantitative analysis of (<b>a</b>,<b>c</b>). <span class="html-italic">n</span> = 3 per <span class="html-italic">n</span> &gt; 500 (<b>b</b>) or &gt;300 (<b>d</b>) nuclei. Data: mean ± SD. (<b>e</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing two examples of co-staining of Pcnt (red) and CDK5RAP2 (green). Scale bars: 10 µm.</p>
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<p>AKAP9 and GM130 co-localize at the NE. (<b>a</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing co-staining of AKAP9 with the MTOC proteins PCM1 (red), Pcnt (red), or CDK5RAP2 (green). (<b>b</b>) Immunofluorescence analysis of C2C12 differentiated for 3 days illustrating different examples of the gradient localization of AKAP9 (green) at the NE of PCM1<sup>+</sup> nuclei. Categories include the following: (1) PCM1<sup>+</sup> nuclei without AKAP9, (2) localization at one side of the nucleus (arrow), (3) greater coverage of the NE than in (3), and (4) full coverage. (<b>c</b>) Quantitative analysis of (<b>b</b>), where PCM1<sup>+</sup>/AKAP9<sup>+</sup> represents categories 2–4. <span class="html-italic">n</span> = 3 per <span class="html-italic">n</span> &gt; 200 nuclei. (<b>d</b>) Immunofluorescence analysis of C2C12 differentiated for 1 day showing co-staining of AKAP9 (green) with the Golgi marker GM130 (red). Scale bar: 10 µm.</p>
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<p>PCM1 is mislocalized in siMbnl2- and siMbnl1/2-treated C2C12 cells. (<b>a</b>) Immunofluorescence analysis of siControl- and siMbnl-treated C2C12 cells showing co-staining for myogenin (red) and PCM1 (green). Yellow arrows: myogenin<sup>+</sup>/PCM1<sup>+</sup> nuclei. Yellow asterisks: myogenin<sup>+</sup>/PCM1<sup>−</sup> nuclei. Scale bar: 20 µm. (<b>b</b>,<b>c</b>) Quantitative analysis of the number of PCM1<sup>+</sup> nuclei in myogenin<sup>+</sup> cells and total number of myogenin<sup>+</sup> cells (%). Data are shown as individual biological replicates with the mean ± SD. <span class="html-italic">n</span> = 3, n.s.: not significant (<span class="html-italic">p</span> &gt; 0.05), *: <span class="html-italic">p</span> &lt; 0.05. (<b>b</b>,<b>c</b>): One-way ANOVA/Bonferroni.</p>
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<p>Mbnl2 regulates the expression levels of AKAP6β but not those of nesprin-1α. (<b>a</b>) Immunofluorescence analysis of siControl- and siMbnl2-treated C2C12 cells showing nesprin-1 staining (red). Scale bar = 20 µm. (<b>b</b>) Quantitative analysis of the number of nesprin-1α+ nuclei in siControl- and siMbnl2-treated C2C12 cells. (<b>c</b>) qPCR analysis of the level of <span class="html-italic">nesprin-1α</span> mRNA expression in siControl- and siMbnl2-treated C2C12 cells. (<b>d</b>) Immunofluorescence analysis of siControl- and siMbnl2-treated C2C12 showing co-staining of myogenin (red) and AKAP6 (green). Yellow asterisks: myogenin<sup>+</sup>/AKAP6<sup>−</sup> nuclei. Scale bar = 20 µm. (<b>e</b>) Quantification of AKAP6/myogenin-positive nuclei in control and treated cells. (<b>f</b>,<b>g</b>) qPCR analysis of <span class="html-italic">AKAP6β</span> and <span class="html-italic">myogenin</span> mRNA levels in siControl- and siMbnl2-treated C2C12 cells ((<b>f</b>): <span class="html-italic">n</span> = 4). Data are shown as individual biological replicates with the mean ± SD. <span class="html-italic">n</span> = 3 if not stated otherwise. n.s.: not significant (<span class="html-italic">p</span> &gt; 0.05), *: <span class="html-italic">p</span> &lt; 0.05, ***: <span class="html-italic">p</span> &lt; 0.001. (<b>b</b>,<b>c</b>,<b>e</b>–<b>g</b>): Student’s <span class="html-italic">t</span>-test/F-test.</p>
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<p>Mbnl2 depletion affects the level of <span class="html-italic">Pcnt S</span> in differentiated C2C12 cells. (<b>a</b>) Agarose gel showing the RNA levels of <span class="html-italic">Pcnt B</span> and <span class="html-italic">Pcnt S</span> 72 h post-siRNA-transfection as indicated. <span class="html-italic">Gapdh</span> is used as a loading control. (<b>b</b>) Quantification of the relative amount of <span class="html-italic">Pcnt S</span> present in the total <span class="html-italic">Pcnt</span> [%], normalized to siControl. Data are shown as individual biological replicates with the mean ± SD. <span class="html-italic">n</span> = 3. n.s.: not significant (<span class="html-italic">p</span> &gt; 0.05), **: <span class="html-italic">p</span> &lt; 0.01. (<b>b</b>): One-way ANOVA/Bonferroni.</p>
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<p>Schematic model of the spatiotemporal NE-MTOC component recruitment during skeletal muscle differentiation. In proliferating myoblasts, the outer nuclear membrane of the nucleus (n) expresses the giant isoform of nesprin-1. As differentiation (d) begins, nesprin-1α is specifically upregulated in skeletal muscle, and its expression appears before AKAP6’s localization to the NE. AKAP6 shows a gradient with a higher signal intensity proximal to the centrosome. Once the NE-MTOC anchor platform is established, PCM1 is the first MTOC protein to be recruited to the NE, followed by Pcnt and CDK5RAP2. Pcnt and CDK5RAP2 cover the same nuclear domain, in contrast to PCM1, which has a higher nuclear coverage area. Finally, AKAP9 localizes to the NE via the Golgi, whereby both of the components show a patchy distribution around the NE during the early stages of differentiation.</p>
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20 pages, 1509 KiB  
Review
L-Theanine Metabolism in Tea Plants: Biological Functions and Stress Tolerance Mechanisms
by Qianying Wang, Jingbo Yu, Wenchao Lin, Golam Jalal Ahammed, Wenli Wang, Ruihong Ma, Mengyao Shi, Shibei Ge, Ahmed S. Mohamed, Liyuan Wang, Qingyun Li and Xin Li
Plants 2025, 14(3), 492; https://doi.org/10.3390/plants14030492 - 6 Feb 2025
Viewed by 445
Abstract
L-theanine, a unique non-protein amino acid predominantly found in tea plants (Camellia sinensis), plays a pivotal role in plant responses to abiotic stress and significantly influences tea quality. In this review, the metabolism and transport mechanisms of L-theanine are comprehensively discussed, [...] Read more.
L-theanine, a unique non-protein amino acid predominantly found in tea plants (Camellia sinensis), plays a pivotal role in plant responses to abiotic stress and significantly influences tea quality. In this review, the metabolism and transport mechanisms of L-theanine are comprehensively discussed, highlighting its spatial distribution in tea plants, where it is most abundant in young leaves and less so in roots, stems, and older leaves. The biosynthesis of L-theanine occurs through the enzymatic conversion of glutamate and ethylamine, catalyzed by theanine synthase, primarily in the roots, from where it is transported to aerial parts of the plant for further catabolism. Environmental factors such as temperature, light, drought, elevated CO2, nutrient unavailability, and heavy metals significantly affect theanine biosynthesis and hydrolysis, with plant hormones and transcription factors playing crucial regulatory roles. Furthermore, it has been demonstrated that applying L-theanine exogenously improves other crops’ resistance to a range of abiotic stresses, suggesting its potential utility in improving crop resilience amid climate change. This review aims to elucidate the physiological mechanisms and biological functions of L-theanine metabolism under stress conditions, providing a theoretical foundation for enhancing tea quality and stress resistance in tea cultivation. Full article
(This article belongs to the Section Plant Physiology and Metabolism)
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Figure 1
<p>Metabolism and transport of theanine in tea plants. The roots of the tea plant are the primary site for synthesizing and storing theanine. Theanine is then transported upwards through transport proteins. Theanine is catabolized to Glu and EA in the shoots. [Thea, theanine; Glu, glutamate; Ala, alanine; Gln, glutamine; EA, ethylamine; TCA, tricarboxylic acid cycle; CO<sub>2</sub>, Carbon dioxide; <span class="html-italic">CsGGT2</span>, <span class="html-italic">Camellia sinensis</span> γ-glutamyl-transpeptidase; AAP, amino acid permease; ABCG, ATP-binding cassette sub-family G; LHT, lysine-histidine-like transporter; CsCAT, <span class="html-italic">Camellia sinensis</span> cationic amino acid transporter; <span class="html-italic">CsPDX</span>, <span class="html-italic">Camellia sinensis</span> pyridoxine biosynthesis; <span class="html-italic">CsTS</span>, <span class="html-italic">Camellia sinensis</span> theanine synthetase; <span class="html-italic">CsAlaDC</span>, <span class="html-italic">Camellia sinensis</span> alanine decarboxylase; <span class="html-italic">CsGS</span>, <span class="html-italic">Camellia sinensis</span> glutamine synthetase; <span class="html-italic">CsGOGAT</span>, <span class="html-italic">Camellia sinensis</span> glutamine-2-oxoglutarate aminotransferase].</p>
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<p>Metabolism of theanine as influenced by environmental factors. Theanine metabolism is affected by abiotic stresses such as temperature, light, drought, and carbon dioxide concentration, as well as nutrient elements and heavy metal stresses. This is manifested by the production of reactive oxygen species (ROS), changes in enzyme activity, and alterations in gene expression. ROS, reactive oxygen species; <span class="html-italic">CAATs</span>, amino acid transporters; <span class="html-italic">AAPs</span>, amino acid permease; <span class="html-italic">GOGAT</span>, glutamine-2-oxoglutarate aminotransferase; <span class="html-italic">AlaDC</span>, alanine decarboxylase; <span class="html-italic">GS</span>, glutamine synthetase; <span class="html-italic">TS</span>, theanine synthetase; <span class="html-italic">LHT</span>, lysine-histidine-like transporter; <span class="html-italic">GGTs</span>, γ-glutamyl-transpeptidases; <span class="html-italic">HY5</span>, ELONGATED HYPOCOTYL 5; <span class="html-italic">GDHs</span>, glutamate dehydrogenases; <span class="html-italic">PDXs</span>, pyridoxine bio-synthesists; <span class="html-italic">GSTs</span>, Glutathione S-transferases; <span class="html-italic">ThYD</span>, theanine hydrolase.</p>
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<p>The application of theanine in other crops. Theanine plays a key role in plant production by enhancing stress tolerance. This is specifically manifested in enhancing the activity of antioxidant enzymes, promoting the production of glutathione, facilitating the conversion of other amino acids, and stimulating the phenyl–propanoid pathway. Low concentrations of theanine can reduce the accumulation of reactive oxygen species (ROS), thereby significantly enhancing the stress resistance of crops [GSH, glutathione].</p>
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30 pages, 5563 KiB  
Review
Advances in Ceramic–Carbonate Dual-Phase Membrane Reactors for Direct CO2 Separation and Utilization
by Xue Kang, Qing Yang, Jiajie Ma, Qiangchao Sun and Hongwei Cheng
Membranes 2025, 15(2), 53; https://doi.org/10.3390/membranes15020053 - 6 Feb 2025
Viewed by 351
Abstract
Excessive (carbon dioxide) CO2 emissions are a primary factor contributing to climate change. As one of the crucial technologies for alleviating CO2 emissions, carbon capture and utilization (CCU) technology has attracted considerable global attention. Technologies for capturing CO2 in extreme [...] Read more.
Excessive (carbon dioxide) CO2 emissions are a primary factor contributing to climate change. As one of the crucial technologies for alleviating CO2 emissions, carbon capture and utilization (CCU) technology has attracted considerable global attention. Technologies for capturing CO2 in extreme circumstances are indispensable for regulating CO2 levels in industrial processes. The unique separation characteristics of the ceramic–carbonate dual-phase (CCDP) membranes are increasingly employed for CO2 separation at high temperatures due to their outstanding chemical, thermal durability, and mechanical strength. This paper presents an overview of CO2 capture approaches and materials. It also elaborates on the research progress of three types of CCDP membranes with distinct permeation mechanisms, concentrating on their principles, materials, and structures. Additionally, several typical membrane reactors, such as the dry reforming of methane (DRM) and reverse water–gas shift (RWGS), are discussed to demonstrate how captured CO2 can function as a soft oxidant, converting feedstocks into valuable products through oxidation pathways designed within a single reactor. Finally, the future challenges and prospects of high-temperature CCDP membrane technologies and their related reactors are proposed. Full article
(This article belongs to the Section Membrane Applications for Gas Separation)
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<p>A schematic summary of the main components in this review. Global carbon neutral pledge-related projects and pathways, CO<sub>2</sub> capture and utilization technologies, and membrane reactor-based materials for post-combustion technology.</p>
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<p>(<b>a</b>) Flow sheet of the chemical absorption. (<b>b</b>) Mechanism diagram of adsorption. (<b>c</b>) Flow sheet of the cryogenic distillation. (<b>d</b>) Mechanism diagram of the membrane separation method.</p>
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<p>Membrane separation technology. (<b>a</b>) The preparation scheme of the crosslinked polymer membrane [<a href="#B58-membranes-15-00053" class="html-bibr">58</a>]. (<b>b</b>) The palladium-based metal membrane for H<sub>2</sub> separation [<a href="#B60-membranes-15-00053" class="html-bibr">60</a>]. (<b>c</b>) The activation mechanism of the N-doped CNTs membrane [<a href="#B61-membranes-15-00053" class="html-bibr">61</a>]. (<b>d</b>) The illustration of the homogeneous hollow-fiber membranes [<a href="#B62-membranes-15-00053" class="html-bibr">62</a>]. (<b>e</b>) The structure of a metal–organic framework membrane [<a href="#B64-membranes-15-00053" class="html-bibr">64</a>]. (<b>f</b>) The schematic drawing of the setup and CCDP membrane for CO<sub>2</sub> permeation [<a href="#B67-membranes-15-00053" class="html-bibr">67</a>]. (<b>g</b>) The schematic illustration of the CCDP membrane for CO<sub>2</sub> separation [<a href="#B68-membranes-15-00053" class="html-bibr">68</a>].</p>
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<p>Schematic diagram of CO<sub>2</sub> separation mechanism in (<b>a</b>) MOCC, (<b>b</b>) MECC, and (<b>c</b>) MEOCC.</p>
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<p>(<b>a</b>) Schematic diagram of penetration of YSZ [<a href="#B80-membranes-15-00053" class="html-bibr">80</a>]. (<b>b</b>) Views of MC on the dense ScCeSZ pellet at a different temperature, reproduced from Ref. [<a href="#B56-membranes-15-00053" class="html-bibr">56</a>] with permission from the American Chemical Society, 2021. (<b>c</b>) The CO<sub>2</sub> permeability of Ce<sub>1−<span class="html-italic">x</span></sub>Gd<span class="html-italic"><sub>x</sub></span>O<sub>2−<span class="html-italic">δ</span></sub>-MC (<span class="html-italic">x</span> = 0.00–0.30) dual-phase membranes at different temperatures [<a href="#B79-membranes-15-00053" class="html-bibr">79</a>]. (<b>d</b>) SEM-EDS image of SDC matrix and SDC-MC membrane [<a href="#B89-membranes-15-00053" class="html-bibr">89</a>]. (<b>e</b>) SEM of Ce<sub>0.8</sub>Gd<sub>0.2</sub>O<sub>2−<span class="html-italic">δ</span></sub> supports prepared using pore formers with different particle sizes, and the particle size distribution of the pore former [<a href="#B79-membranes-15-00053" class="html-bibr">79</a>]. (<b>f</b>) CO<sub>2</sub> flux of BZY-20C-MC membrane with different H<sub>2</sub>O partial pressure [<a href="#B98-membranes-15-00053" class="html-bibr">98</a>]. (<b>g</b>) H<sub>2</sub>O-enhanced CO<sub>2</sub> transport mechanism in the CCDP membranes under wet sweeping gas condition, reproduced from Ref. [<a href="#B56-membranes-15-00053" class="html-bibr">56</a>] with permission from the American Chemical Society, 2021. (<b>h</b>) CO<sub>2</sub> permeation stability of SDC–carbonate membranes with H<sub>2</sub>/CO<sub>2</sub>/N<sub>2</sub> feed containing various concentrations of H<sub>2</sub>S at 750 °C [<a href="#B99-membranes-15-00053" class="html-bibr">99</a>].</p>
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<p>(<b>a</b>) Illustration of CO<sub>2</sub> permeation through a dense mixed ionic–electronic-conducting (MIEC) carbonate dual-phase membrane [<a href="#B100-membranes-15-00053" class="html-bibr">100</a>]. (<b>b</b>) Schematic drawing of preparation of thin SDC layers on SDC/BYS supports by co-pressing method [<a href="#B101-membranes-15-00053" class="html-bibr">101</a>]. (<b>c</b>) Schematic diagram of the ALD chamber and the relationship between the surface grain size of the selective layer and the number of ALD cycles. (<b>d</b>) Schematic diagram of pore size tailoring of ceramic membranes of sintered nanoparticles by ALD. (<b>e</b>) High-magnification SEM images of the layer and the correlation between the thickness of the layer and the number of ALD cycles. (<b>f</b>) Microstructure of a porous Ag matrix overcoated with ZrO<sub>2</sub>. (<b>g</b>) Schematic diagram of conventional infiltration method and new two-step coating method [<a href="#B71-membranes-15-00053" class="html-bibr">71</a>]. (<b>h</b>) Schematic representation for making dead-end tubes by CIP method [<a href="#B67-membranes-15-00053" class="html-bibr">67</a>].</p>
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<p>(<b>a</b>) Microstructures of Ag50Al50 and 48 h-Ag50Al50 [<a href="#B115-membranes-15-00053" class="html-bibr">115</a>]. (<b>b</b>) Schematic illustration of the proposed bi-pathway transport mechanism [<a href="#B113-membranes-15-00053" class="html-bibr">113</a>]. (<b>c</b>) The effect of H<sub>2</sub> concentration in the sweep gas on CO<sub>2</sub> and O<sub>2</sub> flux densities [<a href="#B115-membranes-15-00053" class="html-bibr">115</a>]. (<b>d</b>) The microstructure of a porous Ag matrix and a porous Ag matrix coated with 5% Al<sub>2</sub>O<sub>3</sub> colloidal [<a href="#B117-membranes-15-00053" class="html-bibr">117</a>]. (<b>e</b>) A schematic illustration of the self-forming NiO-MECC membrane. (<b>f</b>) The CO<sub>2</sub> densities of the MECC membrane as a function of the reciprocal of thickness at 550 °C and 600 °C. (<b>g</b>) The CO<sub>2</sub>/O<sub>2</sub> flux density and selectivity of the NiO–MC membrane measured at 850 °C [<a href="#B118-membranes-15-00053" class="html-bibr">118</a>].</p>
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<p>(<b>a</b>) Effects of different gas flow directions on CO<sub>2</sub> permeation in LSCF hollow-fiber membranes and its schematic diagram. (<b>b</b>) Elemental mapping images of the cross-section before and after long-term stability testing [<a href="#B90-membranes-15-00053" class="html-bibr">90</a>]. (<b>c</b>) Structural schematic of La<sub>1.5</sub>Sr<sub>0.5</sub>NiO<sub>4+<span class="html-italic">δ</span></sub>. (<b>d</b>) CO<sub>2</sub> permeation flux at different temperatures [<a href="#B77-membranes-15-00053" class="html-bibr">77</a>]. (<b>e</b>) CO<sub>2</sub> flux under the MOCC model and the transmission ratio between MOCC and MECC pathways [<a href="#B122-membranes-15-00053" class="html-bibr">122</a>]. (<b>f</b>) Schematic diagram of SrFe<sub>0.8</sub>Nb<sub>0.2</sub>O<sub>3−<span class="html-italic">δ</span></sub> four-channel hollow-fiber membrane. (<b>g</b>) Thermal shock resistance [<a href="#B109-membranes-15-00053" class="html-bibr">109</a>]. (<b>h</b>,<b>i</b>) Conductivity of different GDC and LN ratios at varying temperatures and Nyquist plots of CG80-LN20 [<a href="#B123-membranes-15-00053" class="html-bibr">123</a>]. (<b>j</b>) Permeation mechanism of the SDC-SSFA-MC membrane. (<b>k</b>) CO<sub>2</sub> permeation of the SDC-SSFA-MC membrane [<a href="#B124-membranes-15-00053" class="html-bibr">124</a>].</p>
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<p>(<b>a</b>) Schematic diagram of the CP-PSFC-MC membrane coupled with DRM. (<b>b</b>) DRM performance of the CP-PSFC-MC membrane at different temperatures [<a href="#B40-membranes-15-00053" class="html-bibr">40</a>]. (<b>c</b>) Schematic diagram of the SDC-NiO-MC membrane used in DRM. (<b>d</b>) Long-term stability test of the SDC-NiO-MC membrane coupled with DRM [<a href="#B125-membranes-15-00053" class="html-bibr">125</a>]. (<b>e</b>–<b>g</b>) Ethane-to-ethylene conversion using a GDC-MC membrane reactor: (<b>e</b>) mechanism diagram, (<b>f</b>) long-term stability, and (<b>g</b>) SEM image of the surface after testing [<a href="#B126-membranes-15-00053" class="html-bibr">126</a>]. (<b>h</b>) SDC-MC tubular membrane for hydrogen production via the WSG mechanism [<a href="#B127-membranes-15-00053" class="html-bibr">127</a>]. (<b>i</b>) Numerical simulation of ceramic–MC membrane for hydrogen production via WSG and the influence of membrane thickness [<a href="#B128-membranes-15-00053" class="html-bibr">128</a>].</p>
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23 pages, 881 KiB  
Article
Optimization of Biomass to Bio-Syntetic Natural Gas Production: Modeling and Assessment of the AIRE Project Plant Concept
by Emanuele Di Bisceglie, Alessandro Antonio Papa, Armando Vitale, Umberto Pasqual Laverdura, Andrea Di Carlo and Enrico Bocci
Energies 2025, 18(3), 753; https://doi.org/10.3390/en18030753 - 6 Feb 2025
Viewed by 244
Abstract
This study focuses on the modeling, simulation, and optimization of an integrated biomass gasification and methanation process to produce bio-synthetic natural gas (Bio-SNG) as part of the AIRE project. The process was simulated using Aspen Plus® software, incorporating experimental results from pilot-scale [...] Read more.
This study focuses on the modeling, simulation, and optimization of an integrated biomass gasification and methanation process to produce bio-synthetic natural gas (Bio-SNG) as part of the AIRE project. The process was simulated using Aspen Plus® software, incorporating experimental results from pilot-scale gasification setups. Key steps involved syngas production in a dual fluidized bed gasifier and its subsequent conversion to Bio-SNG in a methanation section. Heat integration strategies were implemented to enhance system results demonstrate that optimized heat recovery, achieved by utilizing exothermic methanation reactions to preheat gasification inputs, eliminates the need for auxiliary fuel in the gasification process. The optimized system achieved a thermal recovery rate of 80%, a cold gas efficiency of 79%, a Bio-SNG production rate of 0.4 Nm3/kgBiom, and a methane content of 85 vol.%. These optimizations reduced CO2 emissions by 10% while increasing overall energy efficiency. This work highlights the potential of integrating biomass gasification and methanation processes with heat recovery for sustainable methane production. The findings provide a basis for scaling up the process and further exploring syngas utilization pathways to produce renewable energy carriers. Full article
16 pages, 2689 KiB  
Article
Flow and Corrosion Analysis of CO2 Injection Wells: A Case Study of the Changqing Oilfield CCUS Project
by Wei Lv, Tongyao Liang, Cheng Lu, Mingxing Li, Pei Zhou, Xing Yu, Bin Wang and Haizhu Wang
Processes 2025, 13(2), 439; https://doi.org/10.3390/pr13020439 - 6 Feb 2025
Viewed by 305
Abstract
In carbon dioxide capture, utilization and storage (CCUS) technology, CO2 flooding and storage is currently the most effective geological storage method and the flow law of the gas injection wellbore is the key to achieving safe and efficient CO2 injection. The [...] Read more.
In carbon dioxide capture, utilization and storage (CCUS) technology, CO2 flooding and storage is currently the most effective geological storage method and the flow law of the gas injection wellbore is the key to achieving safe and efficient CO2 injection. The existing wellbore flow model lacks research on the corrosion law. To this end, this paper established a gas injection wellbore flow-heat transfer-corrosion coupling model based on the actual situation of Huang 3 District of the CCUS Demonstration Base of Changqing Oilfield. The field measured data verification showed that the relative average error of the model in predicting pressure and temperature was less than 7.5% and the R2 of the predicted value and the measured value was greater than 0.99. The model was used for sensitivity analysis to evaluate the effects of different gas injection temperatures (15–55 °C), pressures (15–55 MPa), displacements (10–500 t/d) and CO2 contents (50–100%) on wellbore temperature, pressure and corrosion rate, and the wellbore flow law under different gas injection conditions was clarified. The results show that the wellbore temperature, pressure and corrosion rate are significantly affected by gas injection parameters. The wellbore temperature increases with the increase of gas injection temperature and decreases with the increase of gas injection displacement. The wellbore pressure is positively correlated with the gas injection pressure and CO2 content and the gas injection temperature and displacement have little effect on the pressure. The corrosion rate increases with the increase of gas injection temperature and displacement and decreases with the increase of gas injection pressure. In the wellbore, it shows a trend of first increasing and then decreasing with depth. The wellbore corrosion rate is affected by many factors. Reasonable adjustment of gas injection parameters (lowering temperature, increasing pressure, controlling displacement and CO2 content) can effectively slow down the wellbore corrosion loss. The research results can provide a theoretical basis for the optimization of gas injection system. Full article
15 pages, 4558 KiB  
Article
Effect of Carbonization Pressure on CO2 Sequestration and Rheological Properties of Coal Gangue-Based Backfilling Slurry
by Lei Zhu, Zhicheng Liu, Qiang Guo, Binbin Huo, Nan Zhou, Yuejin Zhou, Meng Li and Wenzhe Gu
Appl. Sci. 2025, 15(3), 1656; https://doi.org/10.3390/app15031656 - 6 Feb 2025
Viewed by 268
Abstract
The wet carbonation of coal gangue-based backfilling slurry (CGBS) is considered to be an effective method for the resource utilization of coal gangue solid waste and CO2 sequestration, but CO2 sequestration has a negative impact on the rheological properties of CGBS. [...] Read more.
The wet carbonation of coal gangue-based backfilling slurry (CGBS) is considered to be an effective method for the resource utilization of coal gangue solid waste and CO2 sequestration, but CO2 sequestration has a negative impact on the rheological properties of CGBS. This investigation explores the effect of carbonization pressure on the rheological properties and CO2 sequestration properties of CGBS by using a carbonization reactor, a rheometer, X-ray diffraction, a nitrogen adsorption–desorption instrument, a scanning electron microscope and other testing methods. The results show that increasing the carbonization pressure can increase the CO2 sequestration capacity of CGBS, and the carbonization products produced make the pores of CGBS smaller and the structure more compact; however, increasing the carbonization pressure will reduce the rheological properties of the slurry, and the optimal carbonization pressure is 0.7 MPa. At this time, the yield stress, plastic viscosity and hysteresis loop area of CGBS are 171.66 Pa, 0.0998 Pa·s and 1376 Pa/s, respectively. However, when the carbonization pressure is further increased, the CO2 sequestration capacity tends to remain unchanged. This is mainly because the carbonization pressure causes the carbonization reaction to intensify, forming a calcified layer on the particle surface, which hinders the penetration of CO2 into the particles. This study is of great significance for improving the utilization rate of gangue solid waste and CO2 sequestration. Full article
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<p>Particle size distribution of CG and FA.</p>
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<p>XRD spectra of CG and FA.</p>
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<p>CO<sub>2</sub> sequestration reaction device.</p>
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<p>Rheological testing equipment and procedure.</p>
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<p>CO<sub>2</sub> sequestration capacity of CGBS at different pressures.</p>
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<p>Rheological parameters of CGBS at different carbonization pressures. (<b>a</b>) Shear stress–shear rate. (<b>b</b>) Apparent viscosity–shear rate relationship.</p>
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<p>Yield stress and plastic viscosity of CGBS at different pressures.</p>
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<p>Schematic diagram of CGBS hysteresis loop.</p>
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<p>Relationship between hysteresis loop area and carbonization pressure.</p>
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<p>XRD patterns of CGBS at different carbonization pressures.</p>
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<p>BET diagram of CGBS at different carbonization pressures.</p>
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<p>SEM images of CGBS at different carbonization pressures. (<b>a</b>) CGBS1, (<b>b</b>) CGBS2, (<b>c</b>) CGBS3, (<b>d</b>) CGBS4, (<b>e</b>) CGBS5 and (<b>f</b>) CGBS6.</p>
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<p>LCA boundary of CGBS [<a href="#B37-applsci-15-01656" class="html-bibr">37</a>].</p>
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26 pages, 13415 KiB  
Article
A Methodology for the Multitemporal Analysis of Land Cover Changes and Urban Expansion Using Synthetic Aperture Radar (SAR) Imagery: A Case Study of the Aburrá Valley in Colombia
by Ahmed Alejandro Cardona-Mesa, Rubén Darío Vásquez-Salazar, Juan Camilo Parra, César Olmos-Severiche, Carlos M. Travieso-González and Luis Gómez
Remote Sens. 2025, 17(3), 554; https://doi.org/10.3390/rs17030554 - 6 Feb 2025
Viewed by 422
Abstract
The Aburrá Valley, located in the northwestern region of Colombia, has undergone significant land cover changes and urban expansion in recent decades, driven by rapid population growth and infrastructure development. This region, known for its steep topography and dense urbanization, faces considerable environmental [...] Read more.
The Aburrá Valley, located in the northwestern region of Colombia, has undergone significant land cover changes and urban expansion in recent decades, driven by rapid population growth and infrastructure development. This region, known for its steep topography and dense urbanization, faces considerable environmental challenges. Monitoring these transformations is essential for informed territorial planning and sustainable development. This study leverages Synthetic Aperture Radar (SAR) imagery from the Sentinel-1 mission, covering 2017–2024, to propose a methodology for the multitemporal analysis of land cover dynamics and urban expansion in the valley. The novel proposed methodology comprises several steps: first, monthly SAR images were acquired for every year under study from 2017 to 2024, ensuring the capture of surface changes. These images were properly calibrated, rescaled, and co-registered. Then, various multitemporal fusions using statistics operations were proposed to detect and find different phenomena related to land cover and urban expansion. The methodology also involved statistical fusion techniques—median, mean, and standard deviation—to capture urbanization dynamics. The kurtosis calculations highlighted areas where infrequent but significant changes occurred, such as large-scale construction projects or sudden shifts in land use, providing a statistical measure of surface variability throughout the study period. An advanced clustering technique segmented images into distinctive classes, utilizing fuzzy logic and a kernel-based method, enhancing the analysis of changes. Additionally, Pearson correlation coefficients were calculated to explore the relationships between identified land cover change classes and their spatial distribution across nine distinct geographic zones in the Aburrá Valley. The results highlight a marked increase in urbanization, particularly along the valley’s periphery, where previously vegetated areas have been replaced by built environments. Additionally, the visual inspection analysis revealed areas of high variability near river courses and industrial zones, indicating ongoing infrastructure and construction projects. These findings emphasize the rapid and often unplanned nature of urban growth in the region, posing challenges to both natural resource management and environmental conservation efforts. The study underscores the need for the continuous monitoring of land cover changes using advanced remote sensing techniques like SAR, which can overcome the limitations posed by cloud cover and rugged terrain. The conclusions drawn suggest that SAR-based multitemporal analysis is a robust tool for detecting and understanding urbanization’s spatial and temporal dynamics in regions like the Aburrá Valley, providing vital data for policymakers and planners to promote sustainable urban development and mitigate environmental degradation. Full article
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<p>The Aburrá Valley (white line) between the valleys of the Magdalena and Cauca rivers. Data were acquired from ALOS PALSAR Terrain Corrected and data from IGAC.</p>
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<p>Region of interest (yellow bounding box) selected from the interior of the Aburrá Valley (red line) and the municipalities that are part of it (green lines). Data were acquired from IGAC.</p>
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<p>Proposed methodology for the multitemporal analysis <math display="inline"><semantics> <mrow> <mi>S</mi> <mi>M</mi> <msub> <mi>A</mi> <mn>1</mn> </msub> </mrow> </semantics></math>.</p>
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<p>Proposed methodology for kurtosis multitemporal analysis, <math display="inline"><semantics> <mrow> <mi>S</mi> <mi>M</mi> <msub> <mi>A</mi> <mn>2</mn> </msub> </mrow> </semantics></math>.</p>
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<p>Proposed methodology for analysis of zonal land cover changes.</p>
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<p>Samples of resulting images of the multitemporal analysis methodology proposed in <math display="inline"><semantics> <mrow> <mi>S</mi> <mi>M</mi> <msub> <mi>A</mi> <mn>1</mn> </msub> </mrow> </semantics></math> (<b>a</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mrow> <mi>M</mi> <mi>d</mi> <mi>n</mi> </mrow> </msub> </mrow> </semantics></math>, (<b>b</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mi>σ</mi> </msub> </mrow> </semantics></math>, (<b>c</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mi>M</mi> </msub> </mrow> </semantics></math>, (<b>d</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mrow> <mi>C</mi> <mi>V</mi> </mrow> </msub> </mrow> </semantics></math>, (<b>e</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mi>C</mi> </msub> </mrow> </semantics></math> for the year 2018, and (<b>f</b>) <math display="inline"><semantics> <mrow> <mi>M</mi> <msub> <mi>F</mi> <mi>K</mi> </msub> </mrow> </semantics></math> of <math display="inline"><semantics> <mrow> <mi>S</mi> <mi>M</mi> <msub> <mi>A</mi> <mn>2</mn> </msub> </mrow> </semantics></math> for 2017–2014. Scale, coordinate frame (grid), and north correspond to the region described in the Study area section.</p>
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<p>Areas of analysis of the results by the SMA1 methodological route and kurtosis. (<b>A</b>). Central Park in Bello (<b>B</b>). Parques del Río Medellín (<b>C</b>). Arkadia Shopping center; (<b>D</b>). Peldar Plant (<b>E</b>). La García water supply reservoir (<b>F</b>). Conasfaltos dam (<b>G</b>). La Ayurá stream basin in Envigado (<b>H</b>). Central Park in Bello (<b>I</b>). Avenida Regional Norte (<b>J</b>). Vía Distribuidora Sur.</p>
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<p>Side-by-side comparison of the Aburrá Valley. (<b>a</b>) Division into 9 geographical zones. (<b>b</b>) The corresponding correlation coefficients for 5 different land cover change types of the 9 zones.</p>
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<p>Color maps for every change class in the Aburrá Valley’s nine geographical zones.</p>
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16 pages, 2888 KiB  
Article
Rheological Properties of Crude Oil and Produced Emulsion from CO2 Flooding
by Mingzheng Qiao, Fan Zhang and Weiqi Li
Energies 2025, 18(3), 739; https://doi.org/10.3390/en18030739 - 6 Feb 2025
Viewed by 309
Abstract
Carbon Capture, Utilization and Storage (CCUS) technology is recognized as a pivotal strategy to mitigate global climate change. The CO2 storage and enhanced oil recovery (CCUS-EOR) technology not only enhances oil recovery rates but also contributes to significant reductions in CO2 [...] Read more.
Carbon Capture, Utilization and Storage (CCUS) technology is recognized as a pivotal strategy to mitigate global climate change. The CO2 storage and enhanced oil recovery (CCUS-EOR) technology not only enhances oil recovery rates but also contributes to significant reductions in CO2 emissions, with significant social and economic benefits. This paper examines the application of CO2-EOR technology in both enhancing oil recovery and facilitating geological CO2 storage, and analyzes its implementation status and differences in the United States and China. Through experimental investigations conducted in a specific oilfield, we analyze the effects of dissolved CO2 on the viscosity–temperature characteristics, yield value under pressure, stability, and rheological properties of crude oil and produced fluids. Additionally, we assess the demulsification effectiveness of various demulsifiers. Our findings indicate that both dissolved CO2 in crude oil and emulsions exhibit non-Newtonian fluid behavior characterized by shear thinning, and the viscosity decreases with the increase in temperature and pressure. Furthermore, the presence of dissolved CO2 exacerbates the oil–water separation phenomenon in produced fluids, thereby diminishing emulsion stability. The increase in emulsion concentration and the increase in emulsification temperature are both conducive to improving the emulsification rate. These research results provide critical insights for pipeline design and pump selection in oilfield production processes. Full article
(This article belongs to the Special Issue Low Carbon Energy Generation and Utilization Technologies)
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<p>CO<sub>2</sub> storage methods existing in the EOR process: (<b>a</b>) structural storage; (<b>b</b>) mineralization storage; (<b>c</b>) residual storage; (<b>d</b>) dissolution storage.</p>
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<p>Viscosity–temperature characteristic curves of the dissolved CO<sub>2</sub> crude oil of sample 1 under different pressures and shear rates.</p>
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<p>The curve of the influence of pressure on the viscosity of the dissolved-gas crude oil of sample 1 at a temperature of 30 °C.</p>
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<p>Variation in the pressure-dependent yield value of the dissolved-gas crude oil of sample 1 with temperature under different pressures.</p>
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<p>Viscosity–temperature curve diagram of the sample 2 emulsion.</p>
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<p>Variation in the viscosity of oil–water emulsion with shear time.</p>
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<p>Variation in the viscosity of CO<sub>2</sub>-dissolved emulsion with shear time (sample 5).</p>
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<p>Variation in the viscosity of CO<sub>2</sub>-dissolved emulsion with shear time (sample 6).</p>
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<p>Photographs of demulsification after 60 min (the crude oil emulsion of sample 4, a demulsifier dosage of 150 mg/L, with the temperature at 50 °C; (<b>a</b>) represents TPR-03, (<b>b</b>) represents RKP-2, (<b>c</b>) represents HTMAC, and (<b>d</b>) represents the blank sample).</p>
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<p>Demulsification rate curves of three demulsifiers (crude oil emulsion of sample 4, the dosages are all 150 mg/L, and the temperature is 50 °C).</p>
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<p>Demulsification rate curves under (<b>a</b>) different demulsifier concentrations and (<b>b</b>) different demulsification temperatures.</p>
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25 pages, 4775 KiB  
Review
Sodium-Ion Batteries: Applications and Properties
by Petr Bača, Jiří Libich, Sára Gazdošová and Jaroslav Polkorab
Batteries 2025, 11(2), 61; https://doi.org/10.3390/batteries11020061 - 6 Feb 2025
Viewed by 321
Abstract
With the growing interest in reducing CO2 emissions to combat climate change, humanity is turning to green or renewable sources of electricity. There are numerous issues associated with the development of these sources. One of the key aspects of renewable energy sources [...] Read more.
With the growing interest in reducing CO2 emissions to combat climate change, humanity is turning to green or renewable sources of electricity. There are numerous issues associated with the development of these sources. One of the key aspects of renewable energy sources is their problematic controllability, namely the control of energy production over time. Renewable sources are also associated with issues of recycling, utilization in different geographical zones, environmental impact within the required area, and so on. One of the most discussed issues today, however, is the question of efficient use of the energy produced from these sources. There are several different approaches to storing renewable energy, e.g., supercapacitors, flywheels, batteries, PCMs, pumped-storage hydroelectricity, and flow batteries. In the commercial sector, however, mainly due to acquisition costs, these options are narrowed down to only one concept: storing energy using an electrochemical storage device—batteries. Nowadays, lithium-ion batteries (LIBs) are the most widespread battery type. Despite many advantages of LIB technology, the availability of materials needed for the production of these batteries and the associated costs must also be considered. Thus, this battery type is not very ideal for large-scale stationary energy storage applications. Sodium-ion batteries (SIBs) are considered one of the most promising alternatives to LIBs in the field of stationary battery storage, as sodium (Na) is the most abundant alkali metal in the Earth’s crust, and the cell manufacturing process of SIBs is similar to that of LIBs. Unfortunately, considering the physical and electrochemical properties of Na, different electrode materials, electrolytes, and so on, are required. SIBs have come a long way since they were discovered. This review discusses the latest developments regarding the materials used in SIB technology. Full article
(This article belongs to the Special Issue Towards a Smarter Battery Management System: 2nd Edition)
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<p>Brief history of battery development [<a href="#B2-batteries-11-00061" class="html-bibr">2</a>,<a href="#B28-batteries-11-00061" class="html-bibr">28</a>,<a href="#B30-batteries-11-00061" class="html-bibr">30</a>,<a href="#B31-batteries-11-00061" class="html-bibr">31</a>,<a href="#B32-batteries-11-00061" class="html-bibr">32</a>,<a href="#B33-batteries-11-00061" class="html-bibr">33</a>,<a href="#B34-batteries-11-00061" class="html-bibr">34</a>,<a href="#B35-batteries-11-00061" class="html-bibr">35</a>]. Parts of this figure were adapted with permission from [<a href="#B15-batteries-11-00061" class="html-bibr">15</a>,<a href="#B36-batteries-11-00061" class="html-bibr">36</a>,<a href="#B37-batteries-11-00061" class="html-bibr">37</a>]. Copyright 2020, 2014, 2015 American Chemical Society.</p>
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<p>Number of article publications since 2015 according to Web of Science.</p>
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<p>Number of released articles by leading country in each year according to Web of Science.</p>
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<p>Principle of the sodium-ion battery. Adapted with permission from [<a href="#B15-batteries-11-00061" class="html-bibr">15</a>]. Copyright 2014 American Chemical Society.</p>
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<p>Schematic cell configuration of Na/O<sub>2</sub> and Na/S batteries [<a href="#B38-batteries-11-00061" class="html-bibr">38</a>].</p>
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<p>Na<sup>+</sup> storage mechanisms [<a href="#B48-batteries-11-00061" class="html-bibr">48</a>].</p>
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<p>Na<sup>+</sup> storage mechanism in soft carbon and hard carbon, respectively [<a href="#B59-batteries-11-00061" class="html-bibr">59</a>].</p>
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<p>(<b>a</b>) Na<sub>2</sub>Ti<sub>3</sub>O<sub>7</sub> zigzag structure [<a href="#B70-batteries-11-00061" class="html-bibr">70</a>]. (<b>b</b>) SEM image of nanobelts/CNF [<a href="#B67-batteries-11-00061" class="html-bibr">67</a>]. (<b>c</b>) FESEM (fast emission scanning electron microscopy) image of Na<sub>2</sub>Ti<sub>3</sub>O<sub>7</sub>@C [<a href="#B69-batteries-11-00061" class="html-bibr">69</a>].</p>
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<p>Illustration of crystal representative P2-type and O3-type layered oxides [<a href="#B80-batteries-11-00061" class="html-bibr">80</a>].</p>
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<p>FESEM images of the combined stoichiometries of the Faradion positive-electrode material. (<b>a</b>) A zoomed-out image. (<b>b</b>,<b>c</b>) Magnified images showing the stacked O3/P2 phase morphologies of the primary particles [<a href="#B57-batteries-11-00061" class="html-bibr">57</a>].</p>
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<p>SEM image of Natron iron-based positive-electrode material Na<sub>x</sub>Mn<sub>y</sub>Fe(CN)<sub>6</sub>⋅nH<sub>2</sub>O [<a href="#B95-batteries-11-00061" class="html-bibr">95</a>].</p>
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