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18 pages, 5460 KiB  
Article
GC/MS Screening of Substances Released from Post-Consumer Recycled HDPE Pellets into 95% Ethanol: Reproducibility and Variation between Production Batches
by Melanie Brandt, Jens-Peter Vietzke, Dennis Bankmann and Heiner Gers-Barlag
Recycling 2024, 9(5), 101; https://doi.org/10.3390/recycling9050101 - 16 Oct 2024
Viewed by 517
Abstract
The use of post-consumer recycled (PCR) plastic materials in sensitive packaging applications, such as for cosmetic products and detergents, requires a clear understanding of the identities and quantities of chemical substances, which they may release into packed products. With many potential sources of [...] Read more.
The use of post-consumer recycled (PCR) plastic materials in sensitive packaging applications, such as for cosmetic products and detergents, requires a clear understanding of the identities and quantities of chemical substances, which they may release into packed products. With many potential sources of and thus different types of potentially releasable substances, a reliable non-targeted screening method is required to assess these materials. Such a method should be readily applicable in industrial practice and provide a realistic estimation of substance release. This investigation focused on the use of gas chromatography/coupled mass spectrometry (GC/MS) to analyze substances, which recycled HDPE (rHDPE) plastic pellets release into 95% ethanol under accelerated testing conditions. The results of the repeated testing of reference samples clearly demonstrated the good reproducibility of the described methodology, with standard deviations of repeated determinations of the total released substance amounts of 6.8–8.1%. The application to several production batches of three commercial rHDPE grades additionally demonstrated that the batch-to-batch variation of substances which rHDPE materials release can be confined to less than 10% of variation of the total detectable substance amount. The described methodology is therefore seen as a pragmatic, repeatable assessment of recycled HDPE plastic batches with a view to substance release. Full article
(This article belongs to the Special Issue Challenges and Opportunities in Plastic Waste Management)
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<p>Comparison of the average concentrations (<b>left</b>) and the number (<b>right</b>) of substances released in the measurements of the reference sample for the materials rHDPE-A1, rHDPE-A2 and rHDPE-B1 by substance group. The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>Reproducibility of GC/MS results between repeated measurements of the REF-A1 reference material (the first number represents the week of testing; the second number is the number of the replicate). The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>GC/MS results for nine production batches (A–I) of rHDPE-A1, measured in triplicate and grouped by substance class. The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>GC/MS results for nine production batches (A–I) of rHDPE-A2, measured in triplicate and grouped by substance class. The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>GC/MS results for four production batches (A–C) of rHDPE-B1, measured in triplicate and grouped by substance class. The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>Comparison of representative chromatograms of select samples of rHDPE-A1, rHDPE-A2 and rHDPE-B1 (a.u.: arbitrary units; all chromatograms produced to the same scale but offset for clarity of presentation).</p>
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<p>Reproducibility of GC/MS results between repeated measurements of the REF-A2 reference material (the first number represents the week of testing; the second number is the number of the replicate). The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>Reproducibility of GC/MS results between repeated measurements of the REF-B1 reference material (the first number represents the week of testing; the second number is the number of the replicate). The grouping represents alkanes (ALK), fatty acids, fatty acid esters and alcohols (FAE), and other intentionally or non-intentionally added substances (IAS/NIAS).</p>
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<p>GC/MS results for select individual substances across all batches (A up to I) of rHDPE-A1.</p>
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<p>GC/MS results for select individual substances across all batches (A up to I) of rHDPE-A2.</p>
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<p>GC/MS results for select individual substances across all batches (A up to C) of rHDPE-B1.</p>
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<p>Analysis of the distribution of the standard deviation of the quantification results for each identified substance across all analyses of production batches of sample rHDPE-A1 (replicates were averaged before the analysis).</p>
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<p>Analysis of the distribution of the standard deviation of the quantification results for each identified substance across all analyses of production batches of sample rHDPE-A2 (replicates were averaged before the analysis).</p>
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<p>Results of the pre-study related to the potential absorption of internal standard into the pellet sample. A solution of two internal standards at equal concentration in 95% ethanol was used as a reference (S). Two rHDPE pellet samples (X, Y) were stored for seven days at 60 °C in 95% ethanol with the internal standard added from stock solution before or after the incubation time. Three replicates (1–3) were performed for each case. The mass spectrometer counts for the chromatographic peak related to the internal standards are reported in the graph.</p>
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12 pages, 1486 KiB  
Article
Garnet-Type Zinc Hexacyanoferrates as Lithium, Sodium, and Potassium Solid Electrolytes
by Leonhard Karger, Saravanakumar Murugan, Liping Wang, Zhirong Zhao-Karger, Aleksandr Kondrakov, Florian Strauss and Torsten Brezesinski
Batteries 2024, 10(10), 365; https://doi.org/10.3390/batteries10100365 (registering DOI) - 16 Oct 2024
Viewed by 348
Abstract
Sodium-ion batteries offer an attractive alternative to lithium-based chemistries due to the lower cost and abundance of sodium compared to lithium. Using solid electrolytes instead of liquid ones in such batteries may help improve safety and energy density, but they need to combine [...] Read more.
Sodium-ion batteries offer an attractive alternative to lithium-based chemistries due to the lower cost and abundance of sodium compared to lithium. Using solid electrolytes instead of liquid ones in such batteries may help improve safety and energy density, but they need to combine easy processing with high stability toward the electrodes. Herein, we describe a new class of solid electrolytes that are accessible by room-temperature, aqueous synthesis. The materials exhibit a garnet-type zinc hexacyanoferrate framework with large diffusion channels for alkaline ions. Specifically, they show superionic behavior and allow for facile processing into pellets. We compare the structure, stability, and transport properties of lithium-, sodium-, and potassium-containing zinc hexacyanoferrates and find that Na2Zn3[Fe(CN)6]2 achieves the highest ionic conductivity of up to 0.21 mS/cm at room temperature. In addition, the electrochemical performance and stability of the latter solid electrolyte are examined in solid-state sodium-ion batteries. Full article
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<p>(<b>a</b>) PXRD patterns of the different ZHFs dried at 70 °C. (<b>b</b>,<b>c</b>) Schematic representations of the garnet-type structure, with iron and zinc shown as brown and gray polyhedra, and carbon, nitrogen, and Li<sup>+</sup>/Na<sup>+</sup>/K<sup>+</sup> as black, blue, and yellow spheres, respectively. Note that the alkali-metal sites are only partially occupied. (<b>d</b>) SEM image collected from the Na-ZHF-70 sample.</p>
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<p>(<b>a</b>) Unit-cell volumes of the different ZHFs dried at temperatures ranging from 70 to 120 °C (Li-ZHF: green, Na-ZHF: blue, K-ZHF: purple). (<b>b</b>) TGA of the ZHF-70 samples and (<b>c</b>) corresponding ion currents related to water release from coupled MS measurements.</p>
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<p>(<b>a</b>) Room-temperature ionic conductivities of the different ZHFs dried at temperatures ranging from 70 to 120 °C (Li-ZHF: green, Na-ZHF: blue, K-ZHF: purple). (<b>b</b>) Arrhenius plot of the temperature-dependent conductivity from EIS measurements conducted on the Na-ZHF-90 sample.</p>
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<p>(<b>a</b>) Voltage profiles of full cell type 1 (Na<sub>3</sub>Sn|Na-ZHF-90|Na<sub>2</sub>Mn[Fe(CN)<sub>6</sub>]) at different rates of C/20, C/10, and C/5. The 1st, 3rd, and 5th cycles are shown. Cycling of symmetrical cells using (<b>b</b>) anode composite and (<b>c</b>) cathode composite.</p>
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<p>(<b>a</b>,<b>b</b>) Voltage profiles of full cell type 2 (LTO/Na<sub>3</sub>PS<sub>4</sub>/Super C65|Na-ZHF-90|Na<sub>2</sub>Mn[Fe(CN)<sub>6</sub>]) at different rates of C/20 (1st and 2nd cycles), C/10 (3rd cycle), and C/5 (5th cycle). Note that after the first two cycles, the voltage window was narrowed from 0.5–3.0 V to 0.5–2.75 V. (<b>c</b>) Long-term cycling at C/5 in the voltage window of 0.5–2.75 V.</p>
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16 pages, 8467 KiB  
Article
Quality Enhancement of Torrefied Biopellets Prepared by Unused Forest Biomass and Wood Chip Residues in Pulp Mills
by Tae-Gyeong Lee, Chul-Hwan Kim, Hyeong-Hun Park, Ju-Hyun Park, Min-Sik Park and Jae-Sang Lee
Appl. Sci. 2024, 14(20), 9398; https://doi.org/10.3390/app14209398 - 15 Oct 2024
Viewed by 385
Abstract
The effects of torrefaction of the biopellets made from hardwood chip residue (HW), camellia oilseed cake (CO), and pruning remnants of the toothache tree (TA) and mulberry tree (MT) were evaluated. Torrefaction of the biopellets reduced the volatile matter content of biopellets by [...] Read more.
The effects of torrefaction of the biopellets made from hardwood chip residue (HW), camellia oilseed cake (CO), and pruning remnants of the toothache tree (TA) and mulberry tree (MT) were evaluated. Torrefaction of the biopellets reduced the volatile matter content of biopellets by 18–58% and increased their heating value by 18–58% without negatively impacting durability or fines content. Torrefaction also reduced the initial ignition time of biopellets by 50–59% and prolonged their combustion duration by 15–24%. Regardless of the type of feedstock, all biopellets exhibited mass yields in the range of 60–80% and energy yields ranging from 80–95%. The novelty of this study lies in the application of torrefaction to already-formed biopellets, which enhances pellet quality without the need for binders, and the use of unused forest biomass and wood chip residue from pulp mills. The use of unused forest biomass and wood chip residue from pulp mills for biopellet production not only provides a sustainable and efficient method for waste utilization but also contributes to environmental conservation by reducing the reliance on fossil fuels. Overall, the torrefaction of biopellets represents a promising technology for producing high-quality solid biofuel from a variety of woody biomass feedstocks without compromising pelletizing efficiency. Full article
(This article belongs to the Section Applied Industrial Technologies)
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<p>Ground woody biomass used to manufacture biopellets.</p>
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<p>Pelletizer with a flat die.</p>
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<p>Images of pellets before and after torrefaction using various raw materials.</p>
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<p>Experimental image of analyzing time for the initial ignition and combustion duration of biopellets: (<b>a</b>) pellet ignition by a potable gas torch; (<b>b</b>) ignited pellet with a flame.</p>
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<p>Proximate analysis of the prepared pellets before and after torrefaction.</p>
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<p>Ultimate analysis of the prepared pellets before and after torrefaction.</p>
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<p>Durability of the prepared pellets before and after torrefaction: (<b>a</b>) durability; (<b>b</b>) fines content.</p>
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<p>Bulk density of the prepared pallets before and after torrefaction.</p>
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<p>Calorific value of the prepared biopellets before and after torrefaction.</p>
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<p>Mass and energy yield of the prepared biopellets by torrefaction.</p>
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<p>Ignition and combustion time of the biopellets before and after torrefaction: (<b>a</b>) ignition time; (<b>b</b>) combustion duration.</p>
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<p>Thermogravimetric analysis of the biopellets before and after torrefaction: (<b>a</b>) HW; (<b>b</b>) CO; (<b>c</b>) TA; (<b>d</b>) MT.</p>
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<p>SEM images of biopellets before and after torrefaction.</p>
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<p>Importance and applications of torrefied biopellets.</p>
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16 pages, 2049 KiB  
Article
Potentiometric Electronic Tongue for the Evaluation of Multiple-Unit Pellet Sprinkle Formulations of Rosuvastatin Calcium
by Patrycja Ciosek-Skibińska, Krzysztof Cal, Daniel Zakowiecki and Joanna Lenik
Materials 2024, 17(20), 5016; https://doi.org/10.3390/ma17205016 - 14 Oct 2024
Viewed by 417
Abstract
Sprinkle formulations represent an interesting genre of medicinal products. A frequent problem, however, is the need to mask the unpleasant taste of these drug substances. In the present work, we propose the use of a novel sensor array based on solid-state ion-selective electrodes [...] Read more.
Sprinkle formulations represent an interesting genre of medicinal products. A frequent problem, however, is the need to mask the unpleasant taste of these drug substances. In the present work, we propose the use of a novel sensor array based on solid-state ion-selective electrodes to evaluate the taste-masking efficiency of rosuvastatin (ROS) sprinkle formulations. Eight Multiple Unit Pellet Systems (MUPSs) were analyzed at two different doses (API_50) and (API_10), as well as pure Active Pharmaceutical Ingredient (API) as a bitter standard. Calcium phosphate-based starter pellets were coated with the mixture containing rosuvastatin. Some of them were additionally coated with hydroxypropyl methylcellulose, which was intended to separate the bitter substance and prevent it from coming into contact with the taste buds. The sensor array consisted of 16 prepared sensors with a polymer membrane that had a different selectivity towards rosuvastatin calcium. The main analytical parameters (sensitivity, selectivity, response time, pH dependence of potential, drift of potential, lifetime) of the constructed ion-selective electrodes sensitive for rosuvastatin were determined. The signals from the sensors array recorded during the experiments were processed using Principal Component Analysis (PCA). The results obtained, i.e., the chemical images of the pharmaceutical samples, indicated that the electronic tongue composed of the developed solid-state electrodes provided respective attributes as sensor signals, enabling both of various kinds of ROS pellets to be distinguished and their similarity to ROS bitterness standards to be tested. Full article
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<p>Rosuvastatin((3R,5S,6E)-7-[4-(4-fluorophenyl)-2-(N-ethylmethanesulfonamido)-6-(propan-2-yl)pyrimidin-5-yl]-3,5-dihydroxyhept-6-ene acid).</p>
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<p>Schematic presentation of ISE and potentiometric sensor array.</p>
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<p>Dynamic response for electrodes no. 5, 6, 10 (<b>a</b>) and for electrodes no. 11 and 12 (<b>b</b>).</p>
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<p>Potential drift of the selected electrodes in 2 × 10<sup>−4</sup> mol L<sup>−1</sup> rosuvastatin solution during one hour.</p>
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<p>Effect of the pH on the potential response of the selected electrodes in 2 × 10<sup>−4</sup> mol L<sup>−1</sup> of rosuvastatin solution.</p>
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<p>Stability of sensitivity of the electrode no. 11 in time.</p>
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<p>PCA score plot of electronic tongue results for the studied formulations (A–H). and pure API (API_10 and API_50).</p>
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<p>PC1 values of the electronic tongue results showing gradually changing characteristics of the studied formulations (A–H), compared to pure API standards (API_10 and API_50).</p>
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<p>HCA showing the discrimination of ROS samples. Dashed lines represent a division into 2 groups at variance weighted distance &gt; 30, and 3 groups at variance weighted distance ~20.</p>
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11 pages, 2558 KiB  
Article
Numerical Simulation of Vanadium–Titanium Blast Furnace under Different Smelting Intensities
by Yun Huang, Minghong Li, Shufang Lu and Haibin Zuo
Processes 2024, 12(10), 2220; https://doi.org/10.3390/pr12102220 - 11 Oct 2024
Viewed by 389
Abstract
The blast furnace smelting of vanadium–titanium ore plays a crucial role in the efficient utilization of vanadium-titanium resources. In this research, a detailed numerical simulation study of the temperature, velocity, and concentration fields during the smelting process in a vanadium–titanium blast furnace was [...] Read more.
The blast furnace smelting of vanadium–titanium ore plays a crucial role in the efficient utilization of vanadium-titanium resources. In this research, a detailed numerical simulation study of the temperature, velocity, and concentration fields during the smelting process in a vanadium–titanium blast furnace was conducted. The actual production data from a 1750 m3 vanadium–titanium blast furnace was utilized, combined with softening and dripping parameters and material balance calculations, to develop a two-dimensional blast furnace model. This model was employed to analyze the effects of varying smelting intensities on the internal operating conditions of the furnace. The study found that as smelting intensity increased, significant changes occurred in the temperature fields and CO concentration fields within the furnace, thereby affecting the reduction efficiency of the burdens. Additionally, this research also shows that increasing the proportion of Baima pellets in the furnace will lead to the expansion of the soft melting zone and the upward movement of the soft melting zone. This investigation not only revealed the variations in the internal physical fields of the blast furnace under different operating conditions but also provided theoretical foundations and references for optimizing the design and operation of vanadium–titanium blast furnaces. By comparing the velocity field under different smelting intensities, it was found that the difference was small, which was mainly related to the expansion behavior of the pellets. These findings provide an important scientific basis for further improving the efficiency of blast furnace smelting and reducing costs. Full article
(This article belongs to the Section Manufacturing Processes and Systems)
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<p>Geometric models of 1750 m<sup>3</sup> blast furnace in Xichang Steel Vanadium of Pangang Group (<b>a</b>) geometric model, unit: mm; (<b>b</b>) mesh model.</p>
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<p>Softening–smelting parameters of different smelting intensities.</p>
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<p>Blast furnace temperature field under different smelting intensities.</p>
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<p>Blast furnace CO concentration field under different smelting intensities.</p>
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<p>Blast furnace velocity fields under different smelting intensities.</p>
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14 pages, 5272 KiB  
Article
Chemical Safety Assessment of Pitch-Based Activated Carbon Pellets via Highly Toxic Gas Adsorption Properties
by Min Seong Han, Jong Gu Kim and Byong Chol Bai
Appl. Sci. 2024, 14(20), 9258; https://doi.org/10.3390/app14209258 - 11 Oct 2024
Viewed by 439
Abstract
This study focuses on the preparation of activated carbon using a petroleum-residue-based pitch, as well as the HCl gas adsorption properties of the resulting activated carbon pellets relative to their specific surface area and pore structure. Activated carbon was prepared under various oxidation [...] Read more.
This study focuses on the preparation of activated carbon using a petroleum-residue-based pitch, as well as the HCl gas adsorption properties of the resulting activated carbon pellets relative to their specific surface area and pore structure. Activated carbon was prepared under various oxidation and chemical activation conditions using pitch with a softening point of 220 °C. The activated carbon was mixed with distilled water, an acrylic binder, and carboxymethyl cellulose in a specific ratio to form pellets. These pellets were then dried in an oven at 80 °C. Scanning electron microscopy, energy-dispersive X-ray spectroscopy, and Brunauer–Emmett–Teller analyses were performed to evaluate the surface structure and specific surface area of the finalized pellets. HCl gas was adsorbed at a concentration of 50 ppm while examining the adsorption characteristics relative to the pore structure and specific surface area. Full article
(This article belongs to the Special Issue Synthesis and Applications of Mesoporous Materials)
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<p>(<b>a</b>) TGA with stabilization temperature; (<b>b</b>) FT-IR of pitch stabilization at various temperatures.</p>
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<p>SEM scanning images of the samples (<b>a</b>,<b>b</b>) SP220 RAW, (<b>c</b>,<b>d</b>) SP220 1:1, (<b>e</b>,<b>f</b>) SP220 1:4, (<b>g</b>,<b>h</b>) SP220 1:8.</p>
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<p>A BET image of SP220 activation.</p>
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<p>SEM scanning images of the AC pellet: (<b>a</b>) SP220 1:1, (<b>b</b>) SP220 1:4, (<b>c</b>) SP220 1:8.</p>
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<p>A BET image of the AC pellet.</p>
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<p>An XPS image of the microwave-processed AC pellet.</p>
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<p>A BET of the microwave-processed AC pellet.</p>
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<p>The effect of microwave treatment on the HCl gas breakthrough curve of pellets.</p>
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14 pages, 3964 KiB  
Article
Influence of Polymer Film Thickness on Drug Release from Fluidized Bed Coated Pellets and Intended Process and Product Control
by Marcel Langner, Florian Priese and Bertram Wolf
Pharmaceutics 2024, 16(10), 1307; https://doi.org/10.3390/pharmaceutics16101307 - 8 Oct 2024
Viewed by 452
Abstract
Background/Objectives: Coated drug pellets enjoy widespread use in hard gelatine capsules. In heterogeneous pellets, the drug substance is layered onto core pellets. Coatings are often applied to generate a retarded release or an enteric coating. Methods: In the present study, the thickness of [...] Read more.
Background/Objectives: Coated drug pellets enjoy widespread use in hard gelatine capsules. In heterogeneous pellets, the drug substance is layered onto core pellets. Coatings are often applied to generate a retarded release or an enteric coating. Methods: In the present study, the thickness of a polymer coating layer on drug pellets was correlated to the drug release kinetics. Results: The question should be answered whether it is possible to stop the coating process when a layer thickness referring to an intended drug release is achieved. Inert pellets were first coated with sodium benzoate and second with different amounts of water insoluble polyacrylate in a fluidized bed apparatus equipped with a Wurster inlet. The whole process was controlled in-line and at-line with process analytical technology by the measurement of the particle size and the layer thickness. The in-vitro sodium benzoate release was investigated, and the data were linearized by different standard models and compared with the polyacrylate layer thickness. With increasing polyacrylate layer thickness the release rate diminishes. The superposition of several processes influencing the release results in release profiles corresponding approximately to first order kinetics. The coating layer thickness corresponds to a determined drug release profile. Conclusions: The manufacturing of coated drug pellets with intended drug release is possible by coating process control and layer thickness measurement. Preliminary investigations are necessary for different formulations. Full article
(This article belongs to the Special Issue Impact of Raw Material Properties on Solid Dosage Form Processes)
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<p>SEM photograph of a polyacrylate coated SB pellet.</p>
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<p>Double linear plot of the sodium benzoate release, SB pellets without polyacrylate layer, experimental release from polyacrylate-coated lots P1, P2 and P3 with increasing layer thickness and calculated release P1cal, P2cal and P3cal.</p>
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<p>First order Sigma minus function of the experimental and calculated (cal) sodium benzoate release, lots P1, P2 and P3.</p>
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<p>First order Weibull function of the experimental sodium benzoate release, lots P1, P2 and P3.</p>
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<p>Weibull function release parameter t<sub>63.2%</sub> versus coating layer thickness, lots P1 (coefficient of determination 0.87, polyacrylate content 6.5%), P2 (0.99, 10.5%) and P3 (0.99, 16.1%).</p>
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<p>Square root function of the experimental sodium benzoate release, lots P1, P2 and P3.</p>
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<p>Cubic root function of the experimental sodium benzoate release, lots P1, P2 and P3.</p>
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14 pages, 1267 KiB  
Article
Application End Evaluation of Electrostatic Precipitation for Control PM and NOx Emissions from Small-Scale Combustions
by Oleksandr Molchanov, Kamil Krpec, Jiří Horák, Lenka Kuboňová, František Hopan and Jiří Ryšavý
Fire 2024, 7(10), 356; https://doi.org/10.3390/fire7100356 - 7 Oct 2024
Viewed by 633
Abstract
Electrostatic precipitators (ESPs) have shown promise in reducing particulate matter (PM) emissions, but their potential for simultaneous NOx reduction in small-scale combustion systems remains underexplored. This study focuses on using non-thermal plasma generated in a corona discharge to reduce PM and NOx emissions [...] Read more.
Electrostatic precipitators (ESPs) have shown promise in reducing particulate matter (PM) emissions, but their potential for simultaneous NOx reduction in small-scale combustion systems remains underexplored. This study focuses on using non-thermal plasma generated in a corona discharge to reduce PM and NOx emissions from small-scale combustion. ESP was specifically designed for a commercially available 15 kW boiler with wood pellet combustion and used with both positive and negative discharge polarity to control emissions without any chemical additives. ESP performance was evaluated across a range of specific input energies (SIE) in terms of particle mass and number concentrations and NOx concentrations obtained by continuous gas analysis. ESP ensured the reduction in PM concentrations from 48 mg/m3 to the magnitude of PM content in the ambient air. The highest precipitation efficiency was observed for particles in the 20–200 nm range. Concurrently, NOx emissions were reduced by up to 78%, from 178 mg/m3 to 39 mg/m3. These results were achieved at specific input energies of 36 for positive and 48 J/L for negative corona, which is significantly lower than those reported for many existing separate PM and NOx control systems. This study demonstrates the potential of ESPs as a compact, energy-efficient solution for simultaneous PM and NOx removal in small-scale combustion systems, offering promising implications for improving air pollution control technologies for small-scale combustion systems. Full article
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<p>Measuring system.</p>
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<p>The current–voltage characteristic.</p>
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<p>Changes in NOx (<b>A</b>) and PN (<b>B</b>) concentration with ESP operation.</p>
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<p>Changes particle size distribution with ESP energisation with negative (<b>A</b>) and positive (<b>B</b>) corona.</p>
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13 pages, 520 KiB  
Article
Styrene Migration from Polystyrene for Food Contact: A Case Study on the Processing Chain of Yoghurt Pots
by Valeria Guazzotti, Veronika Hendrich, Anita Gruner, Dominik Fiedler, Angela Störmer and Frank Welle
Appl. Sci. 2024, 14(19), 9056; https://doi.org/10.3390/app14199056 - 7 Oct 2024
Viewed by 508
Abstract
A precautionary specific migration limit of 40 µg/kg for styrene from food contact materials is currently under evaluation in Europe. In the ongoing discussion about applicable methods to demonstrate compliance, testing with food instead of simulants or total transfer calculations has been proposed. [...] Read more.
A precautionary specific migration limit of 40 µg/kg for styrene from food contact materials is currently under evaluation in Europe. In the ongoing discussion about applicable methods to demonstrate compliance, testing with food instead of simulants or total transfer calculations has been proposed. In this study, the residual styrene levels in high-impact polystyrene (HIPS) blended with general-purpose polystyrene (GPPS) were determined at several levels of the processing chain of yoghurt pots (from pellets to sheets, then to pots). The styrene migration from extruded sheets and thermoformed pots was analyzed in food simulants at 10 days/20 °C and 40 °C, as well as in yoghurt after storage at 8 °C after 50 days. The obtained results show that the residual styrene content in the PS materials correlates with migration. However, the migration of styrene was far below the total transfer assumption. Styrene migration from the sheets into food simulants and into yoghurt exceeded that migrating from the pots. Styrene migration into food simulants in 20% ethanol at 10 days/20 °C and 40 °C and, more clearly, in 50% ethanol at 10 days/40 °C, was higher than that into yoghurt tested on the best-before date. Styrene migration from PS pots into yoghurt after storage at 8 °C for 50 days reached up to 15 µg/kg (applying the EU cube model), which would be conservatively covered by testing the PS pots with 20% ethanol at 10 days/20 °C. Full article
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<p>Specific migration of styrene into food simulants from the extruded sheets (solid bars) and the thermoformed pots (dashed bars).</p>
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<p>Relative migration of styrene in yoghurt at 8 °C (area weight normalized to 1 g/dm<sup>2</sup>).</p>
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8 pages, 833 KiB  
Article
Evaluation and Comparison of the Effect of Three Dental Luting Cements on Mineralized Bone Derived from Dental Pulp Stem Cells: An In Vitro Study
by Sneha Bajoria, Shwetha Rajesh Shetty, Vinod Bandela, Shital Sonune, Roshan Noor Mohamed, Kulashekar Reddy Nandalur, Anil Kumar Nagarajappa, Amjad Obaid Aljohani, Aljowharah Ali Alsattam, Eatedal Mukhlef Alruwaili, Alreem Abdulaziz Alnuman, Miad Abdulnasser Alahmed, Saraswathi Kanaparthi and Doaa Abdelaziz A. Helal
Medicina 2024, 60(10), 1622; https://doi.org/10.3390/medicina60101622 - 4 Oct 2024
Viewed by 514
Abstract
Background and Objectives: This study aimed to investigate the effect of zinc phosphate (ZnP) cement, glass ionomer cement (GIC), and nano-integrated bio-ceramic (NIB) cement on mineralization when placed in contact with bone tissue-forming cells. Materials and Methods: ZnP cement, GIC, and NIB cement [...] Read more.
Background and Objectives: This study aimed to investigate the effect of zinc phosphate (ZnP) cement, glass ionomer cement (GIC), and nano-integrated bio-ceramic (NIB) cement on mineralization when placed in contact with bone tissue-forming cells. Materials and Methods: ZnP cement, GIC, and NIB cement were divided into direct and indirect groups. A total of 72 cement pellets (24 pellets of each test sample) of 3 × 1 mm (width × height) were prepared using polytetrafluoroethylene molds. A total of 3 sample groups were demarcated using 96- cell well culture plates. In the control group, 24 wells were filled with mineralized osteoblasts and 1 µL of gingival crevicular fluid (GCF). In test group 1, to show a direct effect, 36 samples were plated with mineralized osteoblasts and 1 µL GCF for 24 h; the cells were directly exposed to cement pellets. A total of 36 samples were immersed in GCF for 24 h; later the supernatant was transferred to the mineralized osteoblasts to demonstrate an indirect effect in test group 2. To assess the mineralization, osteoblasts were stained with alizarin red and later observed under an inverted phase-contrast microscope. Data were analyzed using the statistical package for social sciences. An independent t-test compared the direct and indirect effects of the ZnP cement, GIC, NIB cement, and control groups on the mineralization of osteoblasts derived from hDPCs. Results: A statistically significant difference was observed between the ZnP cement, GIC, and NIB cement groups (p < 0.05). ZnP cement exhibited a moderate, NIB cement the least harmful effect, and GIC showed the most harmful effect on the mineralization of osteoblast cells. Conclusions: The biocompatibility of dental luting cements is an important aspect that clinicians should consider during their selection. Nano-integrated bio-ceramic cement showed the least negative effect on the mineralization of osteoblast cells which is beneficial for the cementation of cement-retained implant prostheses. However, further studies are needed to evaluate osteoblast and osteoclast activity in vivo. Full article
(This article belongs to the Topic Advances in Dental Materials)
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<p>Cytotoxicity of cement formulations tested on primary human osteoblasts and MG-63 osteoblast-like cells using MTT and WST-1 assays.</p>
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<p>Comparison of different cements on hDPCs by direct and indirect method.</p>
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15 pages, 5791 KiB  
Article
Operational and Design Factors in Air Staging and Their Effects on Fouling from Biomass Combustion
by Akram Elsebaie, Mingming Zhu and Yasir M. Al-Abdeli
Sustainability 2024, 16(19), 8584; https://doi.org/10.3390/su16198584 - 3 Oct 2024
Viewed by 539
Abstract
The global transition towards a carbon-neutral economy highlights the potential of biomass as a renewable fuel source. However, the sustainability of biomass energy systems is challenged by its complex fouling behaviours during combustion. This study investigates the impact of air staging on mitigating [...] Read more.
The global transition towards a carbon-neutral economy highlights the potential of biomass as a renewable fuel source. However, the sustainability of biomass energy systems is challenged by its complex fouling behaviours during combustion. This study investigates the impact of air staging on mitigating fouling in biomass combustion. By optimising the secondary-to-total air flowrate ratio (Qs/Qt) and the positioning of secondary air, this research investigates the impact of operational and design parameters on fouling deposits in biomass combustion. A fixed-bed combustor was used for the experiments, with hardwood pellets as fuel. This study employed TGA and SEM to analyse the fouling deposit samples’ chemical composition and morphology. First, visible inspection established that the inclination of fouling matter to accumulate on cooled deposition pipes is indeed sensitive to Qs/Qt. The results show that lower Qs/Qt ratios (<0.50) lead to heavier, stickier fouling. Peak temperatures in the fuel bed increase with higher Qs/Qt, enhancing the combustion efficiency and affecting the fouling characteristics. SEM analysis further shows that higher Qs/Qt ratios produce finer, more dispersed fouling particles, whereas lower ratios result in larger, more cohesive particles. These findings provide actionable insights for enhancing the sustainability of biomass energy systems and minimising their environmental impact. Full article
(This article belongs to the Section Pollution Prevention, Mitigation and Sustainability)
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<p>(<b>a</b>) Combustor sectional view and (<b>b</b>) lab set-up: (1) primary air inlet ports (2×), (2) packed fuel bed, (3) fuel charging ports, (4) fouling module and air-cooled fouling deposition probes, (5) exhaust stack, (6) secondary air supply line and distribution, (7) thermocouples.</p>
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<p>(<b>a</b>) Fouling module lab set-up and (<b>b</b>) schematic diagram.</p>
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<p>Deposit pipes’ physical appearance: (<b>a</b>) Qs/Qt = 0.33 at LI = 200 mm, (<b>b</b>) Qs/Qt = 0.33 at LI = 300 mm, (<b>c</b>) Qs/Qt = 0.50 at LI = 200 mm, (<b>d</b>) Qs/Qt = 0.50 at LI = 300 mm, (<b>e</b>) Qs/Qt = 0.66 at LI = 200 mm, (<b>f</b>) Qs/Qt = 0.66 at LI = 300 mm, (<b>g</b>) Qs/Qt = 0.71 at LI = 200 mm, (<b>h</b>) Qs/Qt = 0.71 at LI = 300 mm, (<b>i</b>) Qs/Qt = 0.75 at LI = 200 mm, and (<b>j</b>) Qs/Qt = 0.75 at LI = 300 mm.</p>
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<p>Normalised weight loss percentages of fouling deposits derived from TGA (left <span class="html-italic">Y</span>-axis) at Qs/Qt = 0.33 to 0.75; program temperature (right <span class="html-italic">Y</span>-axis). Conditions: (<b>a</b>) LI = 200 mm and (<b>b</b>) LI = 300 mm.</p>
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<p>Temperatures, ash content, and total deposits for (<b>a</b>) LI = 200 mm and (<b>b</b>) LI = 300 mm at Qs/Qt = 0.33 to 0.75. Left axis: fuel bed temperatures (°C) and total fouling deposits (mg). Right axis: fouling probe temperatures.</p>
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<p>SEM images of fouling deposits samples for combustion condition LI = 200 mm at Qs/Qt ratios of (<b>a</b>) 0.33, (<b>b</b>) 0.50, (<b>c</b>) 0.66, (<b>d</b>) 0.71, and (<b>e</b>) 0.75.</p>
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<p>SEM images of fouling deposits samples for combustion condition LI = 200 mm at Qs/Qt ratios of (<b>a</b>) 0.33, (<b>b</b>) 0.50, (<b>c</b>) 0.66, (<b>d</b>) 0.71, and (<b>e</b>) 0.75.</p>
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<p>(<b>a</b>) CO (100×) (ppm) and NOx (ppm) emissions and (<b>b</b>) CO<sub>2</sub>%, O<sub>2</sub>% (left axis), and burning rate (kg·m<sup>−2</sup>·s<sup>−1</sup>) (right axis) at LI = 200 mm (solid) and LI = 300 mm (stripes) for Qs/Qt = 0.33 to 0.75.</p>
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22 pages, 968 KiB  
Article
Diet of Three Cryptobenthic Clingfish Species and the Factors Influencing It
by Domen Trkov, Danijel Ivajnšič, Marcelo Kovačić and Lovrenc Lipej
Animals 2024, 14(19), 2835; https://doi.org/10.3390/ani14192835 - 1 Oct 2024
Viewed by 433
Abstract
Cryptobenthic fish are small benthic fish species that normally live in various hiding places. Due to their large numbers, they are very important for energy transfer to higher trophic levels. However, due to their small size and hidden lifestyle, knowledge about them and [...] Read more.
Cryptobenthic fish are small benthic fish species that normally live in various hiding places. Due to their large numbers, they are very important for energy transfer to higher trophic levels. However, due to their small size and hidden lifestyle, knowledge about them and their ecology, including their diet, is still limited. Using a non-destructive method based on faecal pellets, we investigated the diet of three clingfish species, Lepadogaster lepadogaster, L. candolii, and Apletodon incognitus, in the shallow northern Adriatic Sea. To better understand the results, we studied the fauna of potential prey in the habitats of the fish studied and also took fish specimens to observe their behaviour in the laboratory. The three species feed predominantly on crustaceans, particularly amphipods, copepods, and decapods. The proportion of the different taxa in the diet depends on the species of clingfish, the size of the specimens, and the size of the prey. In addition, the behaviour of the fish, the home range of the specimens, and the availability of food played an important role. The presence of certain crustacean groups in the environment also determines the occurrence of clingfish of different species and sizes. Full article
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<p>Sampling sites (black dots) along the Slovenian coast where clingfish were searched for.</p>
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<p>Index of the relative importance (%) of different prey groups for three clingfish species.</p>
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15 pages, 4997 KiB  
Article
Development of Vertical Farming Systems from Waste Polymers Using Additive Manufacturing Techniques
by Sunilkarthik Ezhilarasu, Carlos Bañón and Arlindo Silva
Recycling 2024, 9(5), 90; https://doi.org/10.3390/recycling9050090 - 1 Oct 2024
Viewed by 921
Abstract
Driven by population growth, rising living costs, and the urgent need to address climate change, sustainable food production and circular economy principles are becoming increasingly important. Conventional agriculture faces significant challenges, including land scarcity, water shortages, and disrupted supply chains. As a solution, [...] Read more.
Driven by population growth, rising living costs, and the urgent need to address climate change, sustainable food production and circular economy principles are becoming increasingly important. Conventional agriculture faces significant challenges, including land scarcity, water shortages, and disrupted supply chains. As a solution, cities are adopting vertical farming to enhance urban food security and promote circularity. This research introduces FLOAT (Farming Lab on a Trough), an innovative vertical farming system made from bio-polymers and recycled polyethylene terephthalate glyco (rPETG) pellets from plastic bottles. FLOAT’s design emphasizes sustainability and closed-loop material usage. The study showcases the versatility of additive manufacturing (AM) in creating complex geometries with fully functional 1:1 prototypes. These prototypes highlight FLOAT’s potential as a scalable and adaptable solution for sustainable food production in urban settings, contributing to improved food security and environmental sustainability. By integrating FLOAT with conventional practices, we aim to exceed Singapore’s 2030 food security targets and achieve lasting urban food resilience. FLOAT aims to scale sustainable food production, fostering community ties with food, and nurturing future responsibility. Full article
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<p>3D model of Farming Lab on a Trough—FLOAT.</p>
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<p>Exploded isometric view of FLOAT Trough.</p>
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<p>3D model of FLOAT’s Linear Configuration.</p>
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<p>Overview of proposed design using generative parametric scripting.</p>
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<p>(<b>a</b>) Troughs along desired path curve (<b>b</b>) Section cuts [Linear Trough] (<b>c</b>) Infill pattern/density.</p>
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<p>(<b>a</b>) Circular lattice configuration. (<b>b</b>) 3D rendering of Circular Prototype.</p>
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<p>Lattice geometry design iterations.</p>
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<p>Prototyping of Linear FLOAT module in circular configuration (<b>a</b>) Top view, (<b>b</b>) Isometric View.</p>
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<p>(<b>1</b>) Exploration into recycling plastic wastes with (<b>a</b>) Shredder, (<b>b</b>) Dryer, (<b>c</b>) Filament Extruder, (<b>d</b>) 3D Printer, (<b>2</b>) Filament Extrusion process.</p>
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<p>(<b>a</b>) Scaled prototype of FLOAT in PLA. (<b>b</b>) Scaled prototype of FLOAT in PETG.</p>
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<p>(<b>a</b>) Lattice support braces. (<b>b</b>) Foot support. (<b>c</b>) Signage support.</p>
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<p>Section slice with infill pattern and printing material data.</p>
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<p>Table illustrating the estimated waste recycled for a sample model.</p>
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<p>City Developments Limited showcases 3D-printed FLOAT in PLA.</p>
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<p>FLOAT in rPETG with automated irrigation, display at National Design Centre.</p>
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20 pages, 4872 KiB  
Article
Antimicrobial Properties of Fennel By-Product Extracts and Their Potential Applications in Meat Products
by Marica Egidio, Loriana Casalino, Filomena De Biasio, Marika Di Paolo, Ricardo Gómez-García, Manuela Pintado, Alma Sardo and Raffaele Marrone
Antibiotics 2024, 13(10), 932; https://doi.org/10.3390/antibiotics13100932 - 1 Oct 2024
Viewed by 768
Abstract
Background: Beef burgers are perishable meat products, and to extend their shelf life, EU Regulation 1129/11 permits the use of certain additives. Objectives: However, given the concerns of health-conscious consumers and the potential toxicity of synthetic substances, this study aimed to explore the [...] Read more.
Background: Beef burgers are perishable meat products, and to extend their shelf life, EU Regulation 1129/11 permits the use of certain additives. Objectives: However, given the concerns of health-conscious consumers and the potential toxicity of synthetic substances, this study aimed to explore the use of fennel waste extracts as natural preservatives. Methods: This study characterized the bioactive compounds (phenolic content), the antioxidant activity (ABTS+ and DPPH assay), and the antimicrobial properties (against Salmonella enterica serotype Enteritidis, Escherichia coli, Staphylococcus aureus, Bacillus cereusi, and Pseudomonas aeruginosa) of different fennel waste extracts (LF, liquid fraction; SF, solid fraction and PF, pellet fraction). Additionally, the potential use of the best fennel extract was evaluated for its impact on beef burger shelf life (up to 18 days at 4 ± 1 °C) in terms of microbiological profile, pH, and activity water (aw). Results: The PF extract, which was rich in flavones, hydroxybenzoic, and hydroxycinnamic acids, demonstrated the highest antioxidant and antimicrobial activities. Microbiological analyses on beef burgers with PF identified this extract as a potential antimicrobial substance. The aw and pH values did not appear to be affected. Conclusions: In conclusion, fennel extracts could be proposed as natural compounds exploitable in beef burgers to preserve their quality and extend their shelf-life. Full article
(This article belongs to the Special Issue Natural Compounds as Antimicrobial Agents, 2nd Edition)
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<p>Inhibitory effects of fennel hydroalcoholic extracts (LF, liquid fraction used directly; LF*, liquid fraction at 40 °C; SF, solid fraction extract; PF, pellet fraction extract) against <span class="html-italic">Staphylococcus aureus</span> growth (<b>a</b>) and <span class="html-italic">Escherichia coli</span> (<b>b</b>).</p>
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14 pages, 6380 KiB  
Article
Extrusion-Cooking Aspects and Physical Characteristics of Snacks Pellets with Addition of Selected Plant Pomace
by Jakub Soja, Maciej Combrzyński, Tomasz Oniszczuk, Marek Gancarz and Anna Oniszczuk
Appl. Sci. 2024, 14(19), 8754; https://doi.org/10.3390/app14198754 - 27 Sep 2024
Viewed by 529
Abstract
The article presents the possibilities of using by-products from the agri-food industry in the form of fruit and vegetable pomace as a supplementary ingredient to extruded food products in the form of snack pellets. In the recipe based on potato starch, pomace from [...] Read more.
The article presents the possibilities of using by-products from the agri-food industry in the form of fruit and vegetable pomace as a supplementary ingredient to extruded food products in the form of snack pellets. In the recipe based on potato starch, pomace from apples, chokeberries, pumpkin, nigella seed and flaxseed were added in amounts of 10%, 20% and 30%. The prepared raw material blends were processed using a single-screw extruder-cooker with a plastification system L/D = 20 and variable screw speed. The aim of the research was to determine the effect of pomace addition on the extrusion-cooking process, i.e., efficiency and energy consumption, as well as on selected physical properties of the obtained food pellets, such as expansion index, bulk density and durability. The addition of selected pomace influenced the extrusion-cooking process and the physical properties of the extrudates. A percentage contribution ranging from 10 to 20% can optimize the extrusion-cooking process and improve the quality characteristics of the final product, while simultaneously utilizing by-products from the agri-food industry and reducing their negative environmental impact. Full article
(This article belongs to the Section Food Science and Technology)
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<p>Snack pellets without addition (<b>a</b>) and from left with 10, 20 and 30% pomace: (<b>b</b>) chokeberry pomace; (<b>c</b>) apple pomace; (<b>d</b>) pumpkin pomace; (<b>e</b>) nigella seed pomace; (<b>f</b>) flaxseed pomace.</p>
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<p>Snack pellets (intermediate product) with 30% pomace: (<b>a</b>) pumpkin pomace; (<b>b</b>) chokeberry pomace.</p>
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<p>Response plots of extrusion-cooking efficiency of snack pellets depending on selected plant pomace addition level and applied processing variables: (<b>a</b>) apple pomace; (<b>b</b>) chokeberry pomace; (<b>c</b>) pumpkin pomace; (<b>d</b>) flaxseed pomace; (<b>e</b>) nigella seed pomace.</p>
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<p>Response plots of specific mechanical energy demand during the extrusion-cooking process of snack pellets as a function of the level of addition of selected plant pomace and the processing variables used: (<b>a</b>) apple pomace; (<b>b</b>) chokeberry pomace; (<b>c</b>) pumpkin pomace; (<b>d</b>) flaxseed pomace; (<b>e</b>) nigella seed pomace.</p>
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<p>Response plots of expansion index of snack pellets depending on selected plant pomace addition level and applied processing variables: (<b>a</b>) apple pomace; (<b>b</b>) chokeberry pomace; (<b>c</b>) pumpkin pomace; (<b>d</b>) flaxseed pomace; (<b>e</b>) nigella seed pomace.</p>
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<p>Response plots of bulk density of snack pellets depending on selected plant pomace addition level and applied processing variables: (<b>a</b>) apple pomace; (<b>b</b>) chokeberry pomace; (<b>c</b>) pumpkin pomace; (<b>d</b>) flaxseed pomace; (<b>e</b>) nigella seed pomace.</p>
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<p>Snack pellets (intermediate product) with the highest and lowest bulk density: (<b>a</b>) nigella seed pomace; (<b>b</b>) chokeberry pomace.</p>
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<p>Response plots of durability of snack pellets depending on selected plant pomace addition level and applied processing variables: (<b>a</b>) apple pomace; (<b>b</b>) chokeberry pomace; (<b>c</b>) pumpkin pomace; (<b>d</b>) flaxseed pomace; (<b>e</b>) nigella seed pomace.</p>
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<p>Projection of (<b>a</b>) variables parameters on the PC1 and PC2 loadings plot and (<b>b</b>) addition type on the PC1 and PC2 scores.</p>
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<p>Projection of: (<b>a</b>) variables parameters on the PC1 and PC2 loadings; (<b>b</b>) addition quantity on the PC1 and PC2 scores.</p>
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<p>Projection of (<b>a</b>) variables parameters on the PC1 and PC2 loadings and (<b>b</b>) screw speed on the PC1 and PC2 scores.</p>
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