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23 pages, 5431 KiB  
Article
Emulsion-Based Encapsulation of Fibrinogen with Calcium Carbonate for Hemorrhage Control
by Henry T. Peng, Tristan Bonnici, Yanyu Chen, Christian Kastrup and Andrew Beckett
J. Funct. Biomater. 2025, 16(3), 86; https://doi.org/10.3390/jfb16030086 - 3 Mar 2025
Viewed by 182
Abstract
Hemorrhage, particularly non-compressible torso bleeding, remains the leading cause of preventable death in trauma. Self-propelling hemostats composed of thrombin-calcium carbonate (CaCO3) particles and protonated tranexamic acid (TXA+) have been shown to reduce blood loss and mortality in severe bleeding [...] Read more.
Hemorrhage, particularly non-compressible torso bleeding, remains the leading cause of preventable death in trauma. Self-propelling hemostats composed of thrombin-calcium carbonate (CaCO3) particles and protonated tranexamic acid (TXA+) have been shown to reduce blood loss and mortality in severe bleeding animal models. To further enhance both hemostatic and self-propelling properties, this study was to investigate fibrinogen-CaCO3 particles prepared via a water-oil-water (W/O/W) emulsion method. The particles were characterized using light and fluorescence microscopy, gel electrophoresis, rotational thromboelastometry (ROTEM), and video motion tracking. The method produced spherical micrometer-sized particles with various yields and fibrinogen content, depending on the preparation conditions. The highest yield was achieved with sodium carbonate (SC), followed by ammonium carbonate (AC) and sodium bicarbonate (SBC). AC and paraffin generated smaller particles compared to SC and heptane, which were used as the carbonate source and oil phase, respectively. Fibrinogen incorporation led to an increase in particle size, indicating a correlation between fibrinogen content and particle size. Fluorescence microscopy confirmed successful fibrinogen encapsulation, with various amounts and hemostatic effects as assessed by gel electrophoresis and ROTEM. Combining fibrinogen-CaCO3 particles with TXA+ and thrombin-CaCO3 particles showed synergistic hemostatic effects. All fibrinogen-encapsulated particles exhibited self-propulsion when mixed with TXA+ and exposed to water, regardless of fibrinogen content. This study advances current hemostatic particle technology by demonstrating enhanced self-propulsion and fibrinogen incorporation via the W/O/W emulsion method. Further optimization of the encapsulation method could enhance the effectiveness of fibrinogen-CaCO3 particles for hemorrhage control. Full article
(This article belongs to the Collection Feature Papers in Biomaterials for Healthcare Applications)
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Figure 1

Figure 1
<p>Images of light microscopy of (<b>a</b>) Enc AC<sub>lowest</sub> Fib Hep, (<b>b</b>) Enc AC<sub>low</sub> Fib Hep, and (<b>c</b>) Enc AC Fib Hep, (<b>d</b>) Enc AC Fib<sub>high</sub> Hep and (<b>e</b>) Enc AC Fib Par. The scale bar represents 20 µm. See <a href="#jfb-16-00086-t001" class="html-table">Table 1</a> for details of the sample preparation.</p>
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<p>Images of fluorescence microscopy of FITC-labeled fibrinogen-CaCO<sub>3</sub> particles after subtraction of control particles: (<b>a</b>) Enc AC Fib<sub>high</sub> Hep, (<b>b</b>) Enc AC Fib<sub>high</sub> Par, and (<b>c</b>) Enc SBC Fib<sub>high</sub> Hep. Each particle was prepared under the same conditions as detailed in <a href="#jfb-16-00086-t001" class="html-table">Table 1</a> after FITC-labeling of fibrinogen. The scale bar represents 10 µm.</p>
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<p>Coomassie-stained SDS-PAGE analysis of fibrinogen and fibrinogen-encapsulated CaCO<sub>3</sub> particle samples dissolved in TXA<sup>+</sup> solution. Each sample except standard proteins (Mw STD) was reduced with 5% dithiothreitol and analyzed by the gel electrophoresis. Indicated molecular weights were estimated by Mw STD with known molecular weights from 11 to 250 kDa. From left to right, each lane represents: Mw STD, fibrinogen (5 mg/mL), Enc AC Fib<sub>high</sub> Par, Enc AC Fib Par, Enc AC Fib<sub>high</sub> Par 30 min, Enc AC Fib<sub>high</sub> Hep, Enc AC Fib Hep, Enc AC<sub>low</sub> Fib Hep, Enc AC<sub>lowest</sub> Fib Hep, Enc CaCl<sub>2</sub> Fib Hep AC. See <a href="#jfb-16-00086-t001" class="html-table">Table 1</a> for the details of each sample.</p>
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<p>Effects of fibrinogen-encapsulated CaCO<sub>3</sub> particle (Enc AC Fib<sub>high</sub> Par) alone and in combination with TXA<sup>+</sup> and thrombin-encapsulated CaCO<sub>3</sub> particle (Enc Thr) on ROTEM coagulation time (CT) and maximum clot firmness (MCF). ROTEM NATEM tests were performed with plasma containing an abnormally low level of fibrinogen in the presence of 6 mg Enc AC Fib<sub>high</sub> Par alone and together with 2 mg TXA<sup>+</sup> and 2 mg Enc Thr (see <a href="#sec2dot3dot3-jfb-16-00086" class="html-sec">Section 2.3.3</a> for details). Data represent mean ± SD (n = 3).</p>
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<p>Effects of fibrinogen content on the size of fibrinogen-encapsulated CaCO<sub>3</sub> particles. A linear relationship with a Pearson correlation coefficient of 0.689 (<span class="html-italic">p</span> = 0.002) was observed.</p>
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<p>Effects of fibrinogen content on ROTEM coagulation time (CT) and maximum clot firmness (MCF). ROTEM NATEM tests were performed with human plasma containing an abnormally low level of fibrinogen. It should be noted that all control particles prepared in the absence of fibrinogen resulted in non-detectable coagulation and were omitted. The Pearson correlation coefficient between the fibrinogen content and NATEM CT: r = 0.128 (<span class="html-italic">p</span> = 0.66), and NATEM MCF: r = −0.354 (<span class="html-italic">p</span> = 0.22).</p>
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<p>Effects of particle size on ROTEM coagulation time (CT) and maximum clot firmness (MCF). ROTEM NATEM tests were performed with human plasma containing an abnormally low level of fibrinogen. It should be noted that all control particles prepared in the absence of fibrinogen resulted in non-detectable coagulation and thus were omitted. The Pearson correlation coefficient between the particle size and CT: r = 0.466 (<span class="html-italic">p</span> = 0.097), and MCF: r = −0.523 (<span class="html-italic">p</span> = 0.055).</p>
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<p>Effects of fibrinogen content on the self-propelling lag time and speed of fibrinogen-CaCO<sub>3</sub> particles. No linear association of the fibrinogen content with the lag time and speed was observed: r = −0.119 (<span class="html-italic">p</span> = 0.65) and r = −0.276 (<span class="html-italic">p</span> = 0.28), respectively.</p>
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<p>Effects of particle size on the self-propelling lag time and speed of fibrinogen-CaCO<sub>3</sub> particles. No linear relationship between the particle size and self-propelling lag time r = 0.117 (<span class="html-italic">p</span> = 0.65), and a linear relationship between the particle size and self-propelling speed with a Pearson correlation coefficient of −0.506 (<span class="html-italic">p</span> = 0.038) was observed.</p>
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21 pages, 6477 KiB  
Article
Pickering Emulsion-Based Gels with Halloysite as a Stabilizer: Formulation, Mechanical Properties and In Vitro Drug Release Studies
by Anna Froelich
Molecules 2025, 30(5), 1087; https://doi.org/10.3390/molecules30051087 - 27 Feb 2025
Viewed by 169
Abstract
Lidocaine is an analgesic agent frequently incorporated in topical formulations intended for application in minor surgical procedures or relieving neuropathic pain associated with numerous conditions, including post-herpetic neuralgia or diabetic peripheral neuropathy. In this study, Pickering o/w emulsions with halloysite nanotubes as a [...] Read more.
Lidocaine is an analgesic agent frequently incorporated in topical formulations intended for application in minor surgical procedures or relieving neuropathic pain associated with numerous conditions, including post-herpetic neuralgia or diabetic peripheral neuropathy. In this study, Pickering o/w emulsions with halloysite nanotubes as a stabilizing agent and lidocaine incorporated in the internal phase were formulated with the use of the Quality by Design (QbD) approach. The selected emulsions were transformed into semisolid gels with poloxamer 407 as a thickening agent, and investigated for rheological and textural properties, indicating the mechanical features of the obtained gels. Moreover, the obtained formulations were tested for lidocaine release with the use of vertical Franz diffusion cells in order to assess the relationship between the applied composition and potential clinical applicability of the analyzed gels. The obtained results indicate that the emulsion droplet diameter is affected mostly by the oil and halloysite contents. The yield stress points, hardness and cohesiveness values of the obtained gels increased with the oil content. The drug release rate seems to be affected mostly by the concentration of the active ingredient in the oil phase. Full article
(This article belongs to the Special Issue Drug Candidates for Inflammatory Diseases)
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Figure 1
<p>Structure and morphology of halloysite nanotubes. Adapted with permission from [<a href="#B25-molecules-30-01087" class="html-bibr">25</a>].</p>
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<p>Actual (black dots) vs. predicted (red line) values plot. The red area corresponds to the 95% confidence region.</p>
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<p>The 3D response of Sauter mean diameter (D [3;2]) to oil and halloysite (H) content changes.</p>
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<p>Prediction profilers of Sauter mean diameter (D [3;2]) as a function of oil and halloysite (H) content changes and homogenization time. The red numbers and red dotted lines indicate the predicted value (vertical axis) and optimized parameters (horizontal axes), while the gray areas, blue lines and blue numbers show confidence intervals.</p>
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<p>Optical microscopy images of the emulsions used in further studies ((<b>A</b>): emulsion 5, (<b>B</b>): emulsion 12, (<b>C</b>): emulsion 16) and the corresponding placebo gels ((<b>D</b>): G5, (<b>E</b>): G12, (<b>F</b>): G16).</p>
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<p>The results of rotational rheological experiments performed in controlled stress mode for placebo (<b>A</b>), lidocaine-loaded gels (<b>B</b>) and reference halloysite-loaded gel (<b>C</b>).</p>
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<p>The results of oscillatory stress sweep experiments performed for placebo (<b>A</b>), lidocaine-loaded gels (<b>B</b>) and reference halloysite-loaded gel (<b>C</b>).</p>
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<p>The results of oscillatory frequency sweep experiments performed for placebo gels ((<b>A</b>): G5, (<b>B</b>): G12, (<b>C</b>): G16).</p>
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<p>The results of oscillatory frequency sweep experiments performed for lidocaine-loaded gels ((<b>A</b>): G5_L, (<b>B</b>): G12_L, (<b>C</b>): G16_L) and reference halloysite-loaded gel (<b>D</b>).</p>
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<p>The results of texture profile analysis performed for placebo gels (<b>A</b>), lidocaine-loaded gels (<b>B</b>) and reference halloysite-loaded gel (<b>C</b>).</p>
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<p>The correlation matrix depicting the relationships between yield stress points obtained in CS and SS modes, hardness, cohesiveness and adhesiveness (1 corresponds to ideal positive correlation, while −1 corresponds to ideal negative correlation).</p>
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<p>The results of drug release experiments performed for lidocaine-loaded gels G5_L, G12_L and G16_L (n = 5).</p>
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<p>The analysis of correlations between the mechanical parameters ((<b>A</b>): yield stress point obtained in CS experiments; (<b>B</b>): yield stress point obtained in oscillatory studies; (<b>C</b>): hardness; (<b>D</b>): adhesiveness) and LID concentration in the oil phase (<b>E</b>) and the calculated flux values. In plot (<b>D</b>), absolute values of adhesiveness are presented.</p>
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18 pages, 3703 KiB  
Article
Characterization and Rheological Properties of a New Exopolysaccharide Overproduced by Rhizobium sp. L01
by Haolin Huang, Yaolan Wen, Zhuangzhuang Li, Biao Wang and Shuang Li
Polymers 2025, 17(5), 592; https://doi.org/10.3390/polym17050592 - 23 Feb 2025
Viewed by 374
Abstract
The exopolysaccharides produced by rhizobia play an important role in their biotechnological and bioremediation properties. The characteristics and properties of an exopolysaccharide produced by Rhizobium sp. L01 were investigated. Strain Rhizobium sp. L01 was identified as Rhizobium tropici and produced a high yield [...] Read more.
The exopolysaccharides produced by rhizobia play an important role in their biotechnological and bioremediation properties. The characteristics and properties of an exopolysaccharide produced by Rhizobium sp. L01 were investigated. Strain Rhizobium sp. L01 was identified as Rhizobium tropici and produced a high yield of exopolysaccharides (REPS-L01), reaching 22.8 g/L after 63 h of fermentation in a 5 L bioreactor with glucose as the carbon source. REPS-L01 was composed of glucose and galactose in a ratio of 2.95:1, carrying pyruvate, acetate, and succinate groups. REPS-L01 had good shear-thinning properties in aqueous solutions at various concentrations and revealed typical non-crosslinked polymer properties. REPS-L01 revealed thermal stability up to 275 °C. REPS-L01 had the potential to be thicker, being suitable for use under conditions ranging from 4 to 60 °C, pH between 2 and 12, and salt concentrations up to 20,000 mg/L. REPS-L01 showed strong emulsifying activity, particularly with n-hexane; even at concentrations as low as 0.25 wt%, the emulsification index could reach more than 50%. Even more impressively, stable n-hexane emulsion gel was formed with 2 wt% REPS-L01 solution. Rheological studies showed that the solid-like emulsion gel had a high storage modulus, and the SEM studies of the emulsion gel indicated that n-hexane could fill the pores of REPS-L01. Full article
(This article belongs to the Section Biobased and Biodegradable Polymers)
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Figure 1
<p>(<b>A</b>) The colony morphology of strain L01. (<b>B</b>) Phylogenetic analysis of the L01 isolate based on the sequencing of 16S rDNA.</p>
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<p>Time course of REPS-L01 production by the strain <span class="html-italic">Rhizobium</span> sp. L01 in optimized fermentation process.</p>
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<p>(<b>A</b>) FTIR spectra of REPS-L01. (<b>B</b>) TGA and DTG curves of REPS-L01 from 20 to 600 °C.</p>
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<p>(<b>A</b>) Steady shear curve of REPS-L01. (<b>B</b>) Dynamic viscoelastic curve of REPS-L01. (<b>C</b>) Temperature sweep curve of REPS-L01.</p>
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<p>(<b>A</b>) Effect of temperature on apparent viscosity of 0.5 wt% REPS-L01 solution. (<b>B</b>) Effect of pH on apparent viscosity of 0.5 wt% REPS-L01 solution. (<b>C</b>) Effect of metal ions on apparent viscosity of 0.5 wt% REPS-L01 solution.</p>
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<p>(<b>A</b>) Emulsifying activity of REPS-L01 solution (1 wt%) on different substrates. (<b>B</b>) The emulsions formed by different concentrations of REPS-L01 solution on <span class="html-italic">n</span>-hexane. (<b>C</b>) Gelling performance of emulsion layer: inverted vial test after mixing hydrocarbons or water with REPS-L01 solution (2 wt%).</p>
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<p>The dynamic viscoelastic properties of REPS-L01 aqueous solution (1 wt%, black) and <span class="html-italic">n</span>-hexane emulsion gels with different concentrations of REPS-L01 solution (1 wt%, 1.5 wt%, and 2 wt%; yellow, blue, and red).</p>
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<p>(<b>A</b>) SEM of 1 wt% REPS-L01 aqueous solution under 200× magnification. (<b>B</b>) SEM of 1 wt% REPS-L01 aqueous solution under 500× magnification. (<b>C</b>) SEM of <span class="html-italic">n</span>-hexane emulsion gel formed with 2 wt% REPS-L01 under 200× magnification. (<b>D</b>) SEM of <span class="html-italic">n</span>-hexane emulsion gel formed with 2 wt% REPS-L01 under 500× magnification.</p>
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15 pages, 3431 KiB  
Article
Effect of Chinese-Yam-Based Emulsion Gel on Beef Emulsification Characteristics
by Hao Zhang, Xujin Yang, Aiwu Gao and Limin Li
Foods 2025, 14(4), 692; https://doi.org/10.3390/foods14040692 - 17 Feb 2025
Viewed by 409
Abstract
Addressing the prevalent issue of excessive fat consumption in contemporary diets, a novel method has been devised for the preparation of an emulsion gel enriched with healthful fatty acids which possesses superior emulsification characteristics. This innovative approach aims to serve as a viable [...] Read more.
Addressing the prevalent issue of excessive fat consumption in contemporary diets, a novel method has been devised for the preparation of an emulsion gel enriched with healthful fatty acids which possesses superior emulsification characteristics. This innovative approach aims to serve as a viable substitute for the fat content in beef mince. This paper aims to evaluate the effect of emulsion gels, formulated primarily with Chinese yam as the key ingredient, on the emulsification properties and microstructural characteristics of beef mince. The findings indicate that, when the proportion of fat substituted by the emulsion gel reaches 50%, the surface hydrophobicity of the beef mince attains a value of 37.34%, which approximates that of beef tallow. Furthermore, the water retention capacity of this formulation is significantly superior to that of the other test groups (p < 0.05). Additionally, when the fat replacement with emulsion gel is increased to 75%, the protein solubility is observed to be 22.85 mg/mL. As the quantity of emulsion gel increases, the gel structure of the beef mince undergoes a gradual densification. This alteration is accompanied by a statistically significant upward trend in the overall α-helix content (p < 0.05), whereas the β-turn angle exhibits an opposite trend and the β-sheet content demonstrates a biphasic pattern, initially increasing and subsequently decreasing. Notably, the random coil of the emulsion gel reaches its minimum when the fat content is at 50%, corresponding to a state of maximal stability in the beef mince. This study provides a basis for developing research into meat products with a healthier fat profile. Full article
(This article belongs to the Section Food Physics and (Bio)Chemistry)
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<p>Surface hydrophobicity of beef minced with addition of different amounts of emulsion gel. Note: Amount of bound bromophenol blue is difference between total bromophenol blue and free bromophenol blue. Different letters indicate that there are significant differences between experimental groups (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Effect of adding different amounts of emulsion gel on juice loss of beef mince. Note: Different letters indicate that there are significant differences between experimental groups (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Water retention and cooking loss of beef minced with different amounts of emulsion gel. Note: Different letters indicate that there are significant differences between experimental groups (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Solubility of minced beef protein with addition of different amounts of emulsion gel.</p>
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<p>Secondary structure analysis of minced beef protein with different amounts of emulsion gel.</p>
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<p>Intermolecular force of minced beef protein with addition of different amounts of emulsion gel. Note: Different letters indicate that there are significant differences between experimental groups (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>The microstructure of beef mince with addition of different amounts of emulsion gel.</p>
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24 pages, 6687 KiB  
Article
Pea Protein—ĸ-Carrageenan Nanoparticles for Edible Pickering Emulsions
by Galia Hendel, Noy Hen, Shulamit Levenberg and Havazelet Bianco-Peled
Polysaccharides 2025, 6(1), 14; https://doi.org/10.3390/polysaccharides6010014 - 17 Feb 2025
Viewed by 201
Abstract
Pickering emulsions (PEs) can be utilized as inks for 3D food printing owing to their extensive stability and appropriate viscoelastic properties. This research explores food-grade PEs stabilized with nanoparticles (NPs) based on modified pea protein (PP) isolate and k-carrageenan (KC). NPs are fabricated [...] Read more.
Pickering emulsions (PEs) can be utilized as inks for 3D food printing owing to their extensive stability and appropriate viscoelastic properties. This research explores food-grade PEs stabilized with nanoparticles (NPs) based on modified pea protein (PP) isolate and k-carrageenan (KC). NPs are fabricated from solutions with different concentrations of protein and polysaccharide and characterized in terms of size, zeta potential, and wetting properties. The composition of the emulsion is 60% sunflower oil and 40% aqueous phase. Nine emulsion formulations with varying PP and KC concentrations are investigated. The formation of hollow NPs with a hydrodynamic diameter of 120–250 nm is observed. Microscope imaging shows oil droplets surrounded by a continuous aqueous phase, forming homogenous PEs in all formulations that are stable for over 30 days. Further, the oil droplet size decreases with increasing NP concentration while the viscosity increases. Rheologic experiments portray elastic emulsion gels with thixotropic qualities ascribed to the presence of the polysaccharide. The emulsions are subjected to centrifugation in order to compare the original emulsions to concentrated PEs that possess improved capabilities. These emulsions may serve as sustainable and printable saturated fat alternatives due to their composition, texture, stability, and rheological properties. Lastly, PEs are printed smoothly and precisely while maintaining a self-supported structure. Full article
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Figure 1
<p>(<b>A</b>) Mean hydrodynamic diameter and (<b>B</b>) zeta potential. Different letters within the same graph indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Cryo-TEM images: (<b>A</b>,<b>C</b>) P1K0.25, and (<b>B</b>) P2K0.25. Scale bar 100 [nm].</p>
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<p>(<b>A</b>) Three-phase contact angle measurements of NPs with different compositions. (<b>B</b>) Surface tension. Different letters within the same graph indicate a significant difference (<span class="html-italic">p</span> &lt; 0.05) in surface tension.</p>
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<p>FTIR spectra of NPs formed from solutions with 3% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) PP with 0.25–0.5% KC (<span class="html-italic">w</span>/<span class="html-italic">v</span>), compared to the spectra of PP and KC.</p>
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<p>Oil concentration series: (<b>A</b>) Emulsions after preparation, (<b>B</b>) after one week, (<b>C</b>) after two weeks, and (<b>D</b>) after one month. NPs concentration P2K0.25, oil volume fraction φ = 20–70% (<span class="html-italic">v</span>/<span class="html-italic">v</span>). Stored at 4 °C. Emulsions circled in red exhibit phase separation.</p>
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<p>Series of the concentration of solids: (<b>A</b>) Emulsions after preparation, (<b>B</b>) after one week, (<b>C</b>) after two weeks, and (<b>D</b>) after one month. Oil volume fraction φ = 60% (<span class="html-italic">v</span>/<span class="html-italic">v</span>), PP = 1%, 2%, and 3% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), KC = 0.0, 0.25, and 0.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>). Stored at 4 °C.</p>
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<p>CLSM images of emulsions of different concentrations (<b>A</b>) as-prepared and (<b>B</b>) after undergoing centrifugation. The scale bar represents 20 μm.</p>
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<p>Size analysis of oil droplets at a KC concentration of (<b>A</b>) 0.0% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), (<b>B</b>) 0.25% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), and (<b>C</b>) 0.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), as prepared (light blue) and after centrifugation (dark blue). Different letters within the same graph indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Amplitude sweeps of PEs as-prepared and after applying centrifugation: G′ (full symbols) and G″ (open symbols) as a function of strain. (<b>A</b>) PEs stabilized P3K0 NPs: as-prepared (light blue) and after centrifugation (dark blue). (<b>B</b>) As-prepared PEs stabilized with P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs, (<b>C</b>) As-prepared PEs stabilized with P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs (<b>D</b>) PEs stabilized with P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs after centrifugation. (<b>E</b>) PEs stabilized with P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs after centrifugation.</p>
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<p>Frequency sweep of PEs as-prepared and after applying centrifugation. G′ (full symbols) and G″ (open symbols) as a function of angular frequency. (<b>A</b>) PEs stabilized by P3K0 NPs, as-prepared (light blue) and after centrifugation (dark blue). (<b>B</b>) As-prepared PEs stabilized by P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs. (<b>C</b>) As-prepared PEs stabilized by P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs. (<b>D</b>) PEs stabilized by P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs after centrifugation. (<b>E</b>) PEs stabilized by P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs after centrifugation.</p>
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<p>Viscosity of as-prepared emulsions compared to the same formulations after centrifugation (AC). (<b>A</b>) PEs P3K0 (blue), P2K0 (green), or P1K0 (grey) NPs. (<b>B</b>) PEs stabilized by P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (grey) NPs. (<b>C</b>) PEs stabilized by P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (grey) NPs.</p>
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<p>Shear recovery of PEs as-prepared and after applying centrifugation: G′ (full symbols) and G″ (open symbols) as a function of time. (<b>A</b>) PEs stabilized with P3K0 NPs: as-prepared (light blue) and after centrifugation (dark blue). (<b>B</b>) As-prepared PEs stabilized P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs. (<b>C</b>) As-prepared PEs stabilized by P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs. (<b>D</b>) PEs stabilized by P3K0.25 (blue), P2K0.25 (green), or P1K0.25 (gray) NPs after centrifugation. (<b>E</b>) PEs stabilized by P3K0.5 (blue), P2K0.5 (green), or P1K0.5 (gray) NPs after centrifugation.</p>
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<p>(<b>A</b>) Representation of continuous filament extrusion using PE bioink. (<b>B</b>) 3D printing of rectilinear grids: 10·10 mm (left) and 20·20 mm (right). (<b>C</b>) computer-aided design (CAD) of the printed structures; scale bar 5 mm. (<b>D</b>) The obtained printed structures of as-prepared PE and (<b>E</b>) 3D printed PE after centrifugation. PEs are stabilized with P3K0.5 NPs, scale bar: 10 mm. (<b>F</b>) Calculation of the Pr index and fidelity parameters of as-prepared PEs compared to emulsions after centrifugation (<span class="html-italic">n</span> = 5), * <span class="html-italic">p</span> &lt; 0.05, ** <span class="html-italic">p</span> &lt; 0.01.</p>
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20 pages, 1470 KiB  
Review
Cold Plasma-Induced Modulation of Protein and Lipid Macromolecules: A Review
by Srutee Rout, Pradeep Kumar Panda, Pranjyan Dash, Prem Prakash Srivastav and Chien-Te Hsieh
Int. J. Mol. Sci. 2025, 26(4), 1564; https://doi.org/10.3390/ijms26041564 - 13 Feb 2025
Viewed by 717
Abstract
Nowadays, the food industry is prioritizing many innovative processing technologies that can produce minimally processed foods with superior and higher quality, lower costs, and faster operations. Among these advancements, cold plasma (CP) processing stands out for its remarkable capabilities in food preservation and [...] Read more.
Nowadays, the food industry is prioritizing many innovative processing technologies that can produce minimally processed foods with superior and higher quality, lower costs, and faster operations. Among these advancements, cold plasma (CP) processing stands out for its remarkable capabilities in food preservation and extending the shelf life. Beyond its established role in microbial inactivation, CP has emerged as a transformative tool for modifying food biomolecules through reactive plasma species, addressing the versatile requirements of food industries for various applications. This review focuses on the interactions between reactive plasma species and essential food macromolecules, including proteins, lipids, and polysaccharides. The novelty lies in its detailed examination of how CP technology triggers structural, functional, and biochemical changes in proteins and lipids and explains the mechanisms involved. It connects fundamental molecular transformations to practical applications, such as enhanced protein functionality, lipid stabilization, and improved oxidative resistance. CP induces alterations in protein structure, especially in amino acid configurations, that can be applicable to the formulation of advanced gel, 3D printing, thermostable emulsions, enhanced solubility, and sensory materials. This review explores the ability of CP to modify protein allergenicity, its different effects on the mechanical and interfacial properties of proteins, and its role in the production of trans-fat-free oils. Despite its potential, a detailed understanding of the mechanism of CP’s interactions with food macromolecules is also discussed. Furthermore, this review addresses key challenges and outlines future research opportunities, positioning CP as a sustainable and adaptable approach for innovating next-generation food systems. Further research is crucial to fully understand the potential of CP for food processing, followed by product development. Full article
(This article belongs to the Section Macromolecules)
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<p>Schematic diagram showing generation of plasma by (<b>a</b>) radiofrequency, (<b>b</b>) dielectric barrier discharge, (<b>c</b>) surface DBD, (<b>d</b>) corona discharge, (<b>e</b>) microwave, (<b>f</b>) plasma jet, and (<b>g</b>) gliding arc discharge—adapted, redrawn, and modified from ref. [<a href="#B32-ijms-26-01564" class="html-bibr">32</a>] with copyright permission from Elsevier publication.</p>
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<p>Schematic diagram modification of zeolite by the DBD in the CO<sub>2</sub> atmosphere—adapted from ref. [<a href="#B55-ijms-26-01564" class="html-bibr">55</a>] with copyright permission from Wiley publication.</p>
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<p>CP technique’s effect on proteins—adapted from ref. [<a href="#B80-ijms-26-01564" class="html-bibr">80</a>] with copyright permission from Elsevier publication.</p>
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14 pages, 5219 KiB  
Article
Novel Epigenetics Control (EpC) Nanocarrier for Cancer Therapy Through Dual-Targeting Approach to DNA Methyltransferase and Ten-Eleven Translocation Enzymes
by Risa Mitsuhashi, Kiyoshi Sato and Hiroyoshi Kawakami
Epigenomes 2025, 9(1), 6; https://doi.org/10.3390/epigenomes9010006 - 11 Feb 2025
Viewed by 395
Abstract
Background/Objectives: Aberrant hypermethylation in the promoter regions of tumor suppressor genes facilitates the pathogenesis and progression of cancer. Therefore, inhibitors targeting DNA methyltransferase (DNMT) have been tested in clinical studies. However, the current monotherapy of DNMT inhibitors shows limited efficacy. Furthermore, the mechanism [...] Read more.
Background/Objectives: Aberrant hypermethylation in the promoter regions of tumor suppressor genes facilitates the pathogenesis and progression of cancer. Therefore, inhibitors targeting DNA methyltransferase (DNMT) have been tested in clinical studies. However, the current monotherapy of DNMT inhibitors shows limited efficacy. Furthermore, the mechanism of action of DNMT inhibitors is DNA replication-dependent. To address these limitations, we developed a novel core–shell-type “epigenetics control (EpC) nanocarrier” that encapsulated decitabine (5-aza-dC) in the PLGA core nanoparticle and hybridized TET1 gene-encoding pDNA on the lipid shell surface. This study aimed to evaluate whether the dual delivery of DNMT inhibitors and pDNA of TET1 could synergistically enhance tumor suppressor gene expression and induce cell cycle arrest and/or apoptosis in cancer cells. Herein, we demonstrate the potential of the EpC carrier in HCT116 human colon cancer cells to upregulate tumor suppressor gene expression and rapidly achieve cell cycle arrest. Methods: PLGA core nanoparticles were prepared by the W/O/W double emulsion method. The formation of core–shell nanoparticles and complexation with pDNA were investigated and optimized by dynamic light scattering, zeta potential measurement, and agarose gel electrophoresis. The cellular uptake and transfection efficiency were measured by confocal laser scanning microscopy and a luciferase assay, respectively. The expression of p53 protein was detected by Western blotting. The anti-tumor effects of the EpC nanocarrier were evaluated by cell cycle analysis and an apoptosis assay. Results: The EpC nanocarrier delivered the DNMT inhibitor and TET gene-encoding pDNA into HCT116 cells. It promoted the expression of the tumor suppressor protein p53 and induced rapid cell cycle arrest in the G2/M phase in HCT116 cells. Conclusions: Our findings suggest that the dual-targeting of DNMT and TET enzymes effectively repairs aberrant DNA methylation and induces growth arrest in cancer cells, and the dual-targeting strategy may contribute to the advancement of epigenetic cancer therapy. Full article
(This article belongs to the Collection Feature Papers in Epigenomes)
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<p>Structure (<b>A</b>) and preparation scheme (<b>B</b>) of the novel EpC nanocarrier for dual-targeting DNMT and TET1 enzymes in colorectal cancer cells.</p>
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<p>Characterization of EpC nanocarrier. (<b>A</b>) Mean particle size and zeta potential of nanoparticles measured by DLS. (<b>B</b>) pDNA loading ability of lipid-coated PLGA nanoparticles analyzed by agarose gel electrophoresis. (<b>C</b>) Cytotoxicity of EpC nanocarrier for WI-38 cells. (<b>D</b>) Transfection efficiency of EpC nanocarrier in HCT116 cells verified by luciferase assay.</p>
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<p>Cellular uptake of Rho-B-encapsulated EpC nanocarrier into HCT116 cells observed by confocal laser scanning microscopy. The cells were stained with DAPI after incubation with EpC nanocarrier.</p>
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<p>Expression of p53 protein in HCT116 cells with various treatments analyzed by Western blotting.</p>
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<p>(<b>A</b>) A flow cytometry cell cycle analysis in HCT116 cells. (<b>i</b>) NT, (<b>ii</b>) 5-aza-dC, (<b>iii</b>) pDNA of TET1, and (<b>iv</b>) EpC nanocarrier. (<b>B</b>) The ratio of G2/M cell cycle arrest cells.</p>
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<p>Flow cytometry analysis of the apoptosis in HCT116 cells. (<b>i</b>) NT, (<b>ii</b>) 5-aza-dC, (<b>iii</b>) TET1 carrier, and (<b>iv</b>) EpC nanocarrier.</p>
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16 pages, 9150 KiB  
Article
The Development and Preparation of Novel Gel Emulsion Systems Based on a Cholesterol Star-Shaped Derivative
by Shuaihua Liu, Tian Yao, Donghui Xia, Quan Liu, Guanghui Tian and Yang Liu
Molecules 2025, 30(4), 787; https://doi.org/10.3390/molecules30040787 - 8 Feb 2025
Viewed by 340
Abstract
Low-molecular-mass gelators (LMMGs) as stabilizers for gel emulsions offer numerous advantages, such as low usage, functionalizability, and insensitivity to phase ratio. Using LMMGs as stabilizers is one of the effective strategies for preparing gel emulsions. Currently, developing LMMGs and stable gel emulsion systems [...] Read more.
Low-molecular-mass gelators (LMMGs) as stabilizers for gel emulsions offer numerous advantages, such as low usage, functionalizability, and insensitivity to phase ratio. Using LMMGs as stabilizers is one of the effective strategies for preparing gel emulsions. Currently, developing LMMGs and stable gel emulsion systems in a rapid and convenient manner remains a challenge. To cope with the challenge, this study aims to develop a simple and efficient gel emulsion preparation method based on LMMGs. In this study, a cholesterol-based star-shaped derivative (CSD) was designed and synthesized as an LMMG. Based on gelation experiments, a high internal phase W/O gel emulsion system (H2O/CSD-poly(oligo)-dimethylsiloxane/dichloromethane) was successfully developed and stabilized synergistically by the stabilizer (CSD) and the crosslinker (poly(oligo)-dimethylsiloxane with two olefinic bonds at its ends, D-PDMS). The results demonstrate that the synergistic interaction between CSD and D-PDMS is critical for the formation of the gel emulsion. Building on the original gel emulsion system, two novel in situ polymerizable gel emulsion systems (H2O/CSD-D-PDMS/dichloromethane-tert-butyl methacrylate and H2O/CSD-D-PDMS/dichloromethane-N-tert-butyl methacrylamide) were successfully developed by introducing suitable amphiphilic (hydrophilic/lipophilic) polymerizable monomers. This study found that changes in the amphiphilicity of the introduced monomers significantly affected the stability and microscopic morphology of the gel emulsion system. The findings indicate that constructing a hydrophilic/lipophilic balanced system via the synergistic action of stabilizers and crosslinkers in a solvent system, followed by the introduction of polymerizable monomers, is a simple and efficient method for rapidly developing novel polymerizable gel emulsions. These new polymerizable gel emulsions lay the foundation for the subsequent preparation of porous organic polymers (POPs). Full article
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<p>Structure of CSD and D-PDMS.</p>
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<p>Gelation behavior of CSD in different components: (<b>a</b>) CSD 0% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), 100 µL DCM, 900 µL water; (<b>b</b>) CSD 0% (<span class="html-italic">w</span>/<span class="html-italic">v</span>), 0.075 g D-PDMS; (<b>c</b>) CSD 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>); (<b>d</b>) CSD 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) and 0.075 g D-PDMS (total volume 1 mL; CSD concentration is the mass volume fraction relative to the organic phase).</p>
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<p>Inverted fluorescence microscopy image of the gel emulsion, with the following components: 2.5% CSD (<span class="html-italic">w</span>/<span class="html-italic">v</span>, mass volume fraction relative to the organic phase), 0.0175 g D-PDMS, 100 µL DCM, 900 µL water.</p>
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<p>Four polymerizable monomers: (<b>a</b>) <span class="html-italic">tert</span>-butyl methacrylate (<span class="html-italic">t</span>-BMA), (<b>b</b>) <span class="html-italic">N</span>-<span class="html-italic">tert</span>-butyl methacrylamide (<span class="html-italic">N</span>-<span class="html-italic">t</span>-BMA), (<b>c</b>) <span class="html-italic">N</span>-<span class="html-italic">tert</span>-butyl acrylamide (<span class="html-italic">N</span>-<span class="html-italic">t</span>-BAA), (<b>d</b>) styrene.</p>
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<p>Photos of gel emulsions formed with different DCM–<span class="html-italic">t</span>-BMA (<span class="html-italic">v</span>/<span class="html-italic">v</span>) ratios: (<b>a</b>) 10:0, (<b>b</b>) 9:1, (<b>c</b>) 8:2, (<b>d</b>) 7:3, (<b>e</b>) 6:4, (<b>f</b>) 5:5, (<b>g</b>) 4:6, (<b>h</b>) 3:7, (<b>i</b>) 2:8, (<b>j</b>) 1:9, (<b>k</b>) 0:10 (stabilizer content is 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) of the organic phase, D-PDMS is 0.075 g, and the aqueous phase makes up 90% of the total volume).</p>
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<p>Inverted fluorescence microscope images of gel emulsions formed with different DCM–<span class="html-italic">t</span>-BMA (<span class="html-italic">v</span>/<span class="html-italic">v</span>) ratios: (<b>a</b>) 10:0, (<b>b</b>) 7:3, (<b>c</b>) 6:4, (<b>d</b>) 5:5.</p>
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<p>Photos of emulsions or gel emulsions formed at <span class="html-italic">N</span>-<span class="html-italic">t</span>-BMA concentrations ranging from 0% to 100% of the saturation concentration (relative to the organic phase): (<b>a</b>) 0%, (<b>b</b>) 10%, (<b>c</b>) 20%, (<b>d</b>) 30%, (<b>e</b>) 40%, (<b>f</b>) 50%, (<b>g</b>) 60%, (<b>h</b>) 70%, (<b>i</b>) 80%, (<b>j</b>) 90%, (<b>k</b>) 100% (stabilizer content is 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) of the organic phase, D-PDMS is 0.075 g, and the aqueous phase makes up 90% of the total volume).</p>
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<p>Inverted fluorescence microscope image of the gel emulsion formed at 50% of the saturation concentration (relative to the organic phase) of <span class="html-italic">N</span>-<span class="html-italic">t</span>-BMA.</p>
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<p>Photos of emulsions or gel emulsions formed at <span class="html-italic">N</span>-<span class="html-italic">t</span>-BAA concentrations ranging from 0% to 100% of the saturation concentration (relative to the organic phase): (<b>a</b>) 0%, (<b>b</b>) 10%, (<b>c</b>) 20%, (<b>d</b>) 30%, (<b>e</b>) 40%, (<b>f</b>) 50%, (<b>g</b>) 60%, (<b>h</b>) 70%, (<b>i</b>) 80%, (<b>j</b>) 90%, (<b>k</b>) 100% (stabilizer content is 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) of the organic phase, D-PDMS is 0.075 g, and the aqueous phase makes up 90% of the total volume).</p>
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<p>Photos of emulsions formed with different DCM–styrene (<span class="html-italic">v</span>/<span class="html-italic">v</span>) ratios: (<b>a</b>) 10:0, (<b>b</b>) 9:1, (<b>c</b>) 8:2, (<b>d</b>) 7:3, (<b>e</b>) 6:4, (<b>f</b>) 5:5, (<b>g</b>) 4:6, (<b>h</b>) 3:7, (<b>i</b>) 2:8, (<b>j</b>) 1:9, (<b>k</b>) 0:10 (stabilizer content is 2.5% (<span class="html-italic">w</span>/<span class="html-italic">v</span>) of the organic phase, D-PDMS is 0.075 g, and the aqueous phase makes up 90% of the total volume).</p>
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<p>The <span class="html-italic">G</span>′ and <span class="html-italic">G</span>″ curves of DCM and gel emulsions containing different polymerizable monomers as a function of shear stress.</p>
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<p>Molecular structure of the fluorescent probe.</p>
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<p>Synthesis route of the CSD.</p>
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<p>Synthesis route of the D-PDMS.</p>
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25 pages, 5607 KiB  
Article
Hydroxypropyl Cellulose Polymers as Efficient Emulsion Stabilizers: The Effect of Molecular Weight and Overlap Concentration
by Diana Cholakova, Krastina Tsvetkova, Viara Yordanova, Kristina Rusanova, Nikolai Denkov and Slavka Tcholakova
Gels 2025, 11(2), 113; https://doi.org/10.3390/gels11020113 - 5 Feb 2025
Viewed by 577
Abstract
Hydroxypropyl cellulose (HPC) is a non-digestible water-soluble polysaccharide used in various food, cosmetic, and pharmaceutical applications. In the current study, the aqueous solutions of six HPC grades, with molecular mass ranging from 40 to 870 kDa, were characterized with respect to their precipitation [...] Read more.
Hydroxypropyl cellulose (HPC) is a non-digestible water-soluble polysaccharide used in various food, cosmetic, and pharmaceutical applications. In the current study, the aqueous solutions of six HPC grades, with molecular mass ranging from 40 to 870 kDa, were characterized with respect to their precipitation temperatures, interfacial tensions (IFTs), rheological properties and emulsifying and stabilization ability in palm (PO) and sunflower (SFO) oil emulsions. The main conclusions from the obtained results are as follows: (1) Emulsion drop size follows a master curve as a function of HPC concentration for all studied polymers, indicating that polymer molecular mass and solution viscosity have a secondary effect, while the primary effect is the fraction of surface-active molecules, estimated to be around 1–2% for all polymers. (2) Stable emulsions were obtained only with HPC polymers with Mw ≥ 400 kDa at concentrations approximately 3.5 times higher than the critical overlap concentration, c*. At PO concentrations beyond 40 wt. % or when the temperature was 25 °C, these emulsions appeared as highly viscous liquids or non-flowing gels. (3) HPC polymers with Mw < 90 kDa were unable to form stable emulsions, as the surface-active molecules cannot provide steric stabilization even at c ≳ 4–5 c*, resulting in drop creaming and coalescence during storage. Full article
(This article belongs to the Special Issue Food Gels: Gelling Process and Innovative Applications)
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<p>(<b>a</b>) Temperature dependence of 2 wt. % HPC-H aqueous solution viscosity. Below ca. 45 °C the solution is transparent and jelly-like, whereas the polymer precipitates and the viscosity decreases at higher temperatures. Inset: pictures of bottles filled with solution and general chemical structure of HPC. (<b>b</b>) DSC thermogram of bulk palm oil. The experiment was performed at 2 °C/min rate. The phase transition enthalpies measured upon both cooling and heating are in excellent agreement with each other, ΔH ≈ 65 J/g. The temperatures noted on the figure show the peaks maxima.</p>
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<p>(<b>a</b>) Apparent shear viscosity as a function of the shear rate for HPC-H aqueous solutions with different polymer concentrations. (<b>b</b>) Zero shear viscosity as a function of HPC concentration for the different HPC grades studied. The symbol <span class="html-italic">c</span>* denotes the critical overlap concentration for the SSL polymer. The same approach was used for the determination of all <span class="html-italic">c</span>* concentrations.</p>
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<p>Average drop size in 25 wt. % palm oil emulsions as a function of the HPC polymer concentration in the aqueous phase at 40 °C temperature.</p>
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<p>(<b>a</b>) The 25 wt. % PO emulsion viscosities measured at a 10 s<sup>−1</sup> shear rate as a function of HPC concentration. The viscosity increases with the increase in polymer concentration, mainly due to the increase in the viscosity of the respective aqueous solution. Data obtained at 40 °C. (<b>b</b>) Illustrative pictures showing the non-flowing gel-like emulsions prepared with 3 wt. % HPC-H or 4 wt. % HPC-MX, for 25 wt. % PO-in-water emulsions stored at 25 °C. (<b>c</b>) Storage (<span class="html-italic">G</span>′, full symbols) and loss (<span class="html-italic">G</span>″, empty symbols) moduli measured for 3 wt. % HPC-M emulsion with 25 wt. % PO at 25 °C (blue symbols) and 40 °C (red symbols). The moduli increase their values upon cooling due to the partial PO freezing. The lines show the respective HPC-M solution moduli (<span class="html-italic">G</span>′, solid line and <span class="html-italic">G</span>″, dash–dot line). (<b>d</b>) Storage moduli dependence on PO concentration. All samples are prepared with 3 wt. % HPC-H polymer and the rheological properties are measured at 40 °C. The solid black line represents the storage modulus of the 3 wt. % HPC-H solution.</p>
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<p>Illustrative examples of emulsion appearance after 28 days of storage at 40 °C. (<b>a</b>–<b>f</b>) Examples for the six main types of behavior as defined in <a href="#gels-11-00113-t002" class="html-table">Table 2</a>. The emulsions are prepared with 25 wt. % PO and stabilized by (<b>a</b>) 2.5 wt. % HPC-MX—stable emulsion; (<b>b</b>) 3 wt. % SDS—stable with respect to coalescence, but intensive creaming is observed; (<b>c</b>) 2 wt. % HPC-M—partial coalescence in the upper layer; (<b>d</b>) 20 wt. % HPC-SSL—bulk oil layer is formed on the top; (<b>e</b>) 1 wt. % HPC-H—creaming and partial coalescence; and (<b>f</b>) 2 wt. % HPC-L—creaming and coalescence. (<b>g</b>–<b>i</b>) Optical microscopy images obtained at 25 °C in polarized light, showing the content of different layers in the sample shown in (<b>f</b>): (<b>g</b>) oily layer—crystallized PO is observed; (<b>h</b>) emulsion layer; and (<b>i</b>) aqueous phase layer in which only the smallest oily drops have remained, making it slightly turbid. Scale bars = 20 μm.</p>
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<p>Results from centrifugation experiments performed with 25 wt. % PO emulsions, stabilized by HPC-L polymer. (<b>a</b>) The 2 wt. % HPC-L, 40 °C centrifugation temperature, with emulsion appearance shown before centrifugation and after 1, 2, 3 and 4 h centrifugation; (<b>b</b>) the 15 wt. % HPC-L at 40 °C; and (<b>c</b>) the 15 wt. % HPC-L at 25 °C.</p>
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<p>Results obtained in centrifugation experiments at 40 °C. (<b>a</b>,<b>b</b>) Percentage of separated oil, as a function of centrifugation time. The results for palm oil emulsions are given with full symbols and the results for sunflower oil with empty symbols. (<b>c</b>,<b>d</b>) Emulsions with 25 wt. % PO stabilized by 3 wt. % SDS (<b>c</b>) or 2 wt. % HPC-MX + 0.5 wt. % T80 (<b>d</b>). After 4 h of centrifugation, these samples experienced only creaming, while no drop coalescence or formation of bulk oily layer was observed.</p>
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<p>Interfacial tensions measured after 100 s (empty symbols) and 900 s (full symbols) for palm oil (blue triangles) or sunflower oil (red circles) pendant drops, immersed in 1 wt. % HPC solution (SSL, L, M, MX, H, AW) or 3 wt. % SDS. The emulsifiers are arranged in the order of descending IFT.</p>
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<p>Foam films observed in reflected light in the Scheludko cell. The HPC concentrations are 1 wt. % for AW, M and MX (<b>a</b>,<b>d</b>,<b>e</b>), 2 wt. % for SSL and L (<b>b</b>,<b>c</b>) and 1 wt. % for MX + 0.25 wt. % Tween 80<sup>®</sup> mixture in (<b>f</b>). The films shown in (<b>a</b>–<b>c</b>) are unstable and broke, whereas those shown in (<b>d</b>–<b>f</b>) remained stable for more than 15 min. Time elapsed between the film formation and taking the pictures: (<b>a</b>) 10 min, (<b>b</b>) 2 min, (<b>c</b>) 10 min, (<b>d</b>) 10 min, (<b>e</b>) 10 min, (<b>f</b>) 10 min. Scale bars = 50 μm.</p>
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<p>Optical microscopy images, illustrating the process of drop–drop coalescence, observed upon heating of PO drops, dispersed in 1 wt. % HPC-SSL solution. Scale bars = 20 μm.</p>
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<p>Visual appearance upon storage of emulsions prepared with 25 wt. % PO stabilized by HPC polymers. (<b>a</b>) Emulsions stabilized by HPC-H solutions with different concentrations as noted on the images. The samples were stored for 2 days at 40 °C. Partial coalescence and creaming is observed in the sample with 0.5 wt. % polymer, and a thin layer of partially coalesced drops is formed on top of the 1 wt. % emulsion, whereas the 2 and 2.5 wt. % emulsions are stable and no changes are seen compared to the initial emulsions. (<b>b</b>,<b>c</b>) The 1 wt. % HPC-M emulsions stored at 25 °C (<b>b</b>) and at 40 °C (<b>c</b>) for a period of 1 to 28 days. (<b>d</b>) The 3 wt. % HPC-AW emulsion stored for 71 days at 25 °C (left picture). Although this emulsion does not seem completely destroyed, after melting the PO for 2 h at 40 °C, the main fraction of the oil phase separates as a bulk layer on top of the container (right-hand-side image).</p>
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22 pages, 30132 KiB  
Review
Advances in 3D and 4D Printing of Gel-Based Foods: Mechanisms, Applications, and Future Directions
by Zhou Qin, Zhihua Li, Xiaowei Huang, Liuzi Du, Wenlong Li, Peipei Gao, Zhiyang Chen, Junjun Zhang, Ziang Guo, Zexiang Li, Baoze Liu and Tingting Shen
Gels 2025, 11(2), 94; https://doi.org/10.3390/gels11020094 - 27 Jan 2025
Viewed by 984
Abstract
This review examines recent advancements in gel-based 3D and 4D food-printing technologies, with a focus on their applications in personalized nutrition and functional foods. It emphasizes the critical role of tunable rheological and mechanical properties in gels such as starch, protein, and Pickering [...] Read more.
This review examines recent advancements in gel-based 3D and 4D food-printing technologies, with a focus on their applications in personalized nutrition and functional foods. It emphasizes the critical role of tunable rheological and mechanical properties in gels such as starch, protein, and Pickering emulsions, which are essential for successful printing. The review further explores 4D food printing, highlighting stimuli-responsive mechanisms, including color changes and deformation induced by external factors like temperature and pH. These innovations enhance both the sensory and functional properties of printed foods, advancing opportunities for personalization. Key findings from recent studies are presented, demonstrating the potential of various gels to address dietary challenges, such as dysphagia, and to enable precise nutritional customization. The review integrates cutting-edge research, identifies emerging trends and challenges, and underscores the pivotal role of gel-based materials in producing high-quality 3D-printed foods. Additionally, it highlights the potential of Pickering emulsions and lipid gels for expanding functionality and structural diversity. Overall, this work provides a comprehensive foundation for advancing future research and practical applications in gel-based 3D and 4D food printing. Full article
(This article belongs to the Special Issue Recent Advance in Food Gels (2nd Edition))
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<p>Common ways to 3D print gel food and related latest research results. (<b>A</b>) Schematic of common 3D printing process types (FDM, SLS, and SLA). (<b>B</b>) Real-time in situ ultrasound monitoring with hydrogel 3D printing. (<b>C</b>) Direct 4D printing of ceramics driven by hydrogel dehydration. (<b>D</b>) Contactless printing of food micro-particles controlled by ultrasound. (<b>E</b>) Development of soy protein isolate–chelator soluble pectin composite gels as extrusion-based 3D food printing inks: effects of mingling strategy.</p>
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<p>VOS viewer-based network map of hotspots and trends co-occurring in food 3D printing and gelation research.</p>
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<p>Food gel 3D printing for personalization and precision nutrition.</p>
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24 pages, 12258 KiB  
Article
A Comparative Study on the Structural, Physicochemical, Release, and Antioxidant Properties of Sodium Casein and Gelatin Films Containing Sea Buckthorn Oil
by Dariusz Kowalczyk, Monika Karaś, Waldemar Kazimierczak, Tomasz Skrzypek, Adrian Wiater, Artur Bartkowiak and Monika Basiura-Cembala
Polymers 2025, 17(3), 320; https://doi.org/10.3390/polym17030320 - 24 Jan 2025
Viewed by 494
Abstract
The aim of this study was to compare the effect of increasing concentrations (0, 1, 2, 4%) of sea buckthorn oil (SBO) on the structural, physicochemical, release, and antioxidant properties of glycerol-plasticized sodium casein (NaCAS) and gelatin (GEL) films. Ultrasonic treatment ensured effective [...] Read more.
The aim of this study was to compare the effect of increasing concentrations (0, 1, 2, 4%) of sea buckthorn oil (SBO) on the structural, physicochemical, release, and antioxidant properties of glycerol-plasticized sodium casein (NaCAS) and gelatin (GEL) films. Ultrasonic treatment ensured effective homogenization of SBO in both types of emulsions, resulting in yellow-tinted semi-opaque films with relatively low micro-roughness. Generally, GEL films demonstrated lower UV barrier properties and solubility but exhibited higher compactness, crystallinity, transparency, surface hydrophobicity, oxygen barrier performance, strength, and antiradical activity compared to their NaCAS-based counterparts. In a concentration-dependent manner, SBO decreased the solubility and water absorption of the gelatin-based film and enhanced its oxygen permeability. Conversely, SBO improved the water vapor barrier properties of both films in a concentration-independent manner. At the highest SBO concentration, the tensile strength of NaCAS- and GEL-based films decreased by 27% and 20%, respectively, while their antiradical activity increased by 9.3× and 4.3× (based on the time required for the half-neutralization of 2,2-diphenyl-1-picrylhydrazyl radicals). Migration studies showed that at the lowest concentration, SBO was released (into 95% ethanol) approximately 2× faster from the GEL-based film than from the NaCAS film, whereas at higher concentrations, the trend reversed. Full article
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<p>200× DIC microscopy images (<b>A</b>) and 3D representations with calculated root-mean-square roughness (Rq) (<b>B</b>) of the air-side surface of films made from sodium caseinate (NaCAS) and gelatin (GEL) with increasing concentrations of sea buckthorn oil (SBO).</p>
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<p>5000× SEM images of the air-side surface of films made from sodium caseinate (NaCAS) and gelatin (GEL) with increasing concentrations of sea buckthorn oil (SBO).</p>
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<p>Cryo-fractured cross-sections of films made from sodium caseinate (NaCAS) and gelatin (GEL), without and with addition of sea buckthorn oil (SBO), visualized by differential interference contrast microscopy at a magnification of 200× (<b>A</b>) and scanning electron microscopy at magnifications of 1000× (<b>B</b>) and 5000× (<b>C</b>).</p>
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<p>ATR/FTIR spectra of sea buckthorn oil (SBO) and films made from sodium caseinate (NaCAS) (<b>A</b>) and gelatin (GEL) (<b>B</b>) with increasing concentrations of SBO.</p>
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<p>WAXD patterns of films made from sodium caseinate (NaCAS) and gelatin (GEL), without and with addition of sea buckthorn oil (SBO).</p>
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<p>Effect of increasing sea buckthorn oil (SBO) concentrations on UV/VIS light transmission of sodium caseinate (NaCAS) and gelatin (GEL) films.</p>
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<p>Effect of increasing sea buckthorn oil (SBO) concentrations on swelling (<b>A</b>) and water solubility kinetics (<b>B</b>) of sodium caseinate (NaCAS) and gelatin (GEL) films. cnbd—cannot be determined.</p>
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<p>Effect of relative humidity (RH) (<b>A</b>) and increasing concentrations of sea buckthorn oil (SBO) (<b>B</b>) on the oxygen permeability of sodium caseinate (NaCAS) and gelatin (GEL) films. a–e Values with the different superscript letters are significantly different (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>The kinetics of sea buckthorn oil (SBO) release (<b>A</b>) and antiradical activity (against DPPH*) (<b>B</b>) of sodium caseinate (NaCAS) and gelatin (GEL) films.</p>
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19 pages, 4221 KiB  
Article
Bio-Based Interpolyelectrolyte Complexes for the Stabilization of Pickering-like Emulsions
by Francisco Joel Guerrero-Vasquez, Francisco Ortega, Ramón G. Rubio and Eduardo Guzmán
Colloids Interfaces 2025, 9(1), 9; https://doi.org/10.3390/colloids9010009 - 22 Jan 2025
Viewed by 633
Abstract
This work studies the stabilization of Pickering-like emulsions using dispersions of interpolyelectrolyte complexes (IPECs) formed by chitosan (CS) and sodium alginate (ALG), two polymers from natural resources, as the aqueous phase and soybean oil as the oil phase. The ability of these bio-based [...] Read more.
This work studies the stabilization of Pickering-like emulsions using dispersions of interpolyelectrolyte complexes (IPECs) formed by chitosan (CS) and sodium alginate (ALG), two polymers from natural resources, as the aqueous phase and soybean oil as the oil phase. The ability of these bio-based IPECs to form stable emulsions was evaluated by varying the compositional ratio of CS to ALG (Z-ratio) and the oil volume fraction (ϕo). Turbidity, zeta potential, and dynamic light scattering measurements revealed the dependence of IPEC properties on the Z-ratio, with phase separation observed near stoichiometric ratios. Phase diagram analysis showed that stable oil-in-water (O/W) and water-in-oil (W/O) emulsions could be obtained under certain combinations of the Z-ratio and ϕo. Emulsion stability increased with higher Z-ratios due to increased interfacial activity of the complexes and reduced coalescence. Emulsions with high ϕo exhibited transitions from discrete droplets to bicontinuous interfacially jammed emulsion gels (bijels), suggesting tunable morphologies. These results highlight the potential of CHI-ALG IPECs as eco-friendly and efficient stabilizers of Pickering-like emulsions for applications in food, cosmetics and pharmaceuticals. Full article
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<p>(<b>a</b>) Dependence of the turbidity of the mixtures on the compositional ratio <span class="html-italic">Z</span>. The figure presents data for freshly prepared samples (■) and samples after 24 h of ageing (<span style="color:red">●</span>). The lines are visual guides, and the yellow-highlighted region corresponds to the phase separation region. (<b>b</b>) Image of a set of samples with different <span class="html-italic">Z</span> (indicated in the vial) values after equilibration. The two vertical yellow lines indicate the beginning and end of the phase separation region. The nature of each sample is indicated in the image: 1<span class="html-italic">ϕ</span> corresponds to single-phase systems, and 2<span class="html-italic">ϕ</span> corresponds to biphasic systems.</p>
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<p>Dependence of the ζ-potential of IPECs on the <span class="html-italic">Z</span>-ratio. Note that only single-phase samples can be evaluated by electrophoretic mobility measurements for the determination of the <span class="html-italic">ζ</span>-potential. The line is a guide for the eyes and the yellow shaded area corresponds to the phase separation region.</p>
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<p>DLS results: intensity autocorrelation function for aqueous dispersions of IPECs with different values of <span class="html-italic">Z</span> (<b>a</b>) and apparent hydrodynamic diameter distribution obtained from the analysis of the intensity autocorrelation functions (<b>b</b>). In both panels the color code is the same: (<b>―</b>) <span class="html-italic">Z</span> = 0.05, (<b><span style="color:red">―</span></b>) <span class="html-italic">Z</span> = 1.23, (<b><span style="color:#66FF66">―</span></b>) <span class="html-italic">Z</span> = 2.45, and (<b><span style="color:#0033CC">―</span></b>) <span class="html-italic">Z</span> = 2.87.</p>
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<p>Dependence of the average apparent hydrodynamic diameter of IPECs on the <span class="html-italic">Z</span>-ratio. The yellow shaded area corresponds to the phase separation region. The error bars indicate the standard deviation between the average values of the 5 independent measurements obtained for each sample.</p>
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<p>Set of images for emulsions stabilized by IPECs with different values of the <span class="html-italic">Z</span>-ratio (indicated in the images) and different volume fractions of the liquid phases (<b>a</b>) <span class="html-italic">ϕ</span><sub>o</sub> = 0.10, (<b>b</b>) <span class="html-italic">ϕ</span><sub>o</sub> = 0.75, and (<b>c</b>) <span class="html-italic">ϕ</span><sub>o</sub> = 0.90. Images correspond to emulsions aged for 2 months.</p>
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<p>Set of images for emulsions stabilized by IPECs with fixed value of the <span class="html-italic">Z</span>-ratio and different volume fractions of the liquid phases (indicated in the images). (<b>a</b>) <span class="html-italic">Z</span> = 1.23, (<b>b</b>) <span class="html-italic">Z</span> = 2.45, and (<b>c</b>) <span class="html-italic">Z</span> = 3.28. (<b>d</b>) <span class="html-italic">Z</span> = 5.12. Images correspond to emulsions aged for 2 months.</p>
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<p>Images obtained from the test for the determination of the type of emulsion obtained. (<b>a</b>) Dispersion of a drop of W/O emulsion in water. (<b>b</b>) Dispersion of a drop of W/O emulsion in soybean oil. (<b>c</b>) Dispersion of a drop of O/W emulsion in water. (<b>d</b>) Dispersion of a drop of O/W emulsion in soybean oil. Images correspond to emulsions aged for 2 months.</p>
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<p>Compositional map <span class="html-italic">ϕ</span><sub>o</sub>-<span class="html-italic">Z</span> for two-phase systems formed by aqueous dissolution of IPECs and soybean oil. The diagram shows the different types of systems obtained with different symbols: (<span class="html-fig-inline" id="colloids-09-00009-i001"><img alt="Colloids 09 00009 i001" src="/colloids/colloids-09-00009/article_deploy/html/images/colloids-09-00009-i001.png"/></span>) Phase-separated systems, (<span class="html-fig-inline" id="colloids-09-00009-i002"><img alt="Colloids 09 00009 i002" src="/colloids/colloids-09-00009/article_deploy/html/images/colloids-09-00009-i002.png"/></span>) W/O emulsions and (<span class="html-fig-inline" id="colloids-09-00009-i003"><img alt="Colloids 09 00009 i003" src="/colloids/colloids-09-00009/article_deploy/html/images/colloids-09-00009-i003.png"/></span>) O/W emulsions. Results correspond to emulsions aged for 2 months.</p>
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<p>Dependence of the stabilization index, <span class="html-italic">SI</span>, on the value of the <span class="html-italic">Z</span>-ratio for emulsions with different volume fractions of liquid phases. Note that the emulsions obtained for <span class="html-italic">ϕ</span><sub>o</sub> = 0.10 are of W/O type while the emulsions obtained for <span class="html-italic">ϕ</span><sub>o</sub> = 0.75 and 0.90 are of O/W type, while for <span class="html-italic">ϕ</span><sub>o</sub> = 0.25 no emulsion was obtained as shown by the values of <span class="html-italic">SI</span> close to 0. Results correspond to emulsions aged for 2 months.</p>
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<p>Optical microscopy images for emulsions prepared by varying the volume fraction of the oil phase and the <span class="html-italic">Z</span>-ratio of the IPECs used for their stabilization. Images correspond to emulsions aged for 2 months.</p>
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15 pages, 4471 KiB  
Article
Research and Application of Deep Profile Control Technology in Narrow Fluvial Sand Bodies
by Xu Zheng, Yu Wang, Yuan Lei, Dong Zhang, Wenbo Bao and Shijun Huang
Processes 2025, 13(1), 289; https://doi.org/10.3390/pr13010289 - 20 Jan 2025
Viewed by 843
Abstract
Narrow Fluvial Sand Bodies are primarily developed along the river center, with horizontal wells for injection and production in some Bohai waterflooded oilfields. This results in a rapid increase in water cut due to a single injection–production direction. Over time, dominant water breakthrough [...] Read more.
Narrow Fluvial Sand Bodies are primarily developed along the river center, with horizontal wells for injection and production in some Bohai waterflooded oilfields. This results in a rapid increase in water cut due to a single injection–production direction. Over time, dominant water breakthrough channels form between wells, and the remaining oil moves to deeper regions, which makes conventional profile control measures less effective. We developed a quantitative method based on integrated dynamic and static big data to identify these breakthrough channels and measure the flow intensity between injection and production wells. To address deep remaining oil mobilization, we performed micro-analysis and physical simulations with heterogeneous core models, which led to the development of a deep profile control system using emulsion polymer gel and self-assembling particle flooding. Experiments show that the combined technology can reduce oil saturation in low-permeability layers to 45.3% and improve recovery by 30.2% compared to water flooding. Field trials proved to be completely effective, with a cumulative oil increase of over 23,200 cubic meters and a 12% reduction in water cut per well. This deep profile control technology offers significant water cut reduction and enhanced oil recovery. It can provide technical support for efficient water control and profile management in similar reservoirs. Full article
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<p>Planar flow pattern of the Ming Lower Section A sand body in Bohai C Oilfield.</p>
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<p>Characteristics of water injection distribution.</p>
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<p>Physical model of injection–production well profile in high-permeability reservoir.</p>
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<p>Distribution map of strong channeling between wells in the Ming Lower Section A sand body of Bohai C Oilfield.</p>
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<p>“Linear” well network and schematic diagram of narrow channel sand bodies.</p>
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<p>Core schematic diagram: (<b>a</b>) model schematic; (<b>b</b>) physical model image.</p>
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<p>Gelation performance of emulsion polymer gel.</p>
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<p>Microscopic morphology of emulsion polymer and gel. (<b>a</b>) Emulsion polymer (at 50 μm scale); (<b>b</b>) emulsion polymer gel (at 40 μm scale).</p>
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<p>Relationship between particle size and aging time for samples of different concentrations.</p>
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<p>Microscopic morphology of self-aggregating particles.</p>
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<p>Oil saturation distribution at different stages in Scheme 2: (<b>a</b>) water flooding, (<b>b</b>) self-aggregating particles, (<b>c</b>) oil displacement agent, (<b>d</b>) subsequent water flooding.</p>
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<p>Oil saturation distribution at different stages in Scheme 2: (<b>a</b>) water flooding, (<b>b</b>) emulsion polymer gel, (<b>c</b>) self-aggregating particles, (<b>d</b>) subsequent water flooding.</p>
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<p>Oil saturation distribution at different stages in Scheme 3: (<b>a</b>) water flooding, (<b>b</b>) emulsion polymer gel, (<b>c</b>) self-aggregating particles, (<b>d</b>) oil displacement agent, (<b>e</b>) subsequent water flooding.</p>
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<p>J20H well production curve.</p>
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22 pages, 3967 KiB  
Article
Techno-Functionalities of White Bean Protein Concentrate: A Comparative Study with Soy and Pea Proteins
by Paula Zambe Azevedo, Juliana Eloy Granato Costa, Jessica da Silva Matos, Breno Rodrigues de Souza, Sueli Rodrigues, Fabiano André Narciso Fernandes, Vanelle Maria Silva, Márcia Cristina Teixeira Ribeiro Vidigal, Paulo Cesar Stringheta, Evandro Martins and Pedro Henrique Campelo
Macromol 2025, 5(1), 3; https://doi.org/10.3390/macromol5010003 - 15 Jan 2025
Viewed by 623
Abstract
The study of the techno-functional properties of novel plant-based proteins has gained importance due to their as alternatives to conventional proteins in food systems. This work evaluated the techno-functional and structural properties of white bean protein concentrate (WBPC) in comparison with commercial soy [...] Read more.
The study of the techno-functional properties of novel plant-based proteins has gained importance due to their as alternatives to conventional proteins in food systems. This work evaluated the techno-functional and structural properties of white bean protein concentrate (WBPC) in comparison with commercial soy and pea proteins. The WBPC exhibited a higher foaming capacity (FC) at neutral pH and excellent foam stability (FS) at both tested pH levels, outperforming the commercial proteins. Although the WBPC’s gelation occurred only at concentrations above 16% and its water-holding capacity (WHC) was lower than that of the soy and pea proteins, the WBPC showed a high binding capacity for nonpolar molecules, excelling in its oil-holding capacity (OHC) and forming stable emulsions, which are relevant for stabilization in food products. Additionally, WBPC can form more rigid gel networks, suitable for systems requiring greater mechanical strength. These techno-functional properties indicate that WBPC is a promising alternative source for the plant-based food industry, helping to meet the demand for innovative, sustainable products and contributing to the diversification of protein sources. Full article
(This article belongs to the Collection Advances in Biodegradable Polymers)
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Graphical abstract
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<p>Flowchart of the white bean protein concentrate extraction process. The steps include grinding the beans in a blender (initially on the left), adjusting the pH to 10, centrifugation for fraction separation, subsequent pH adjustment (to 3), a second centrifugation to obtain the precipitated protein, and finally drying the protein concentrate, resulting in a powder.</p>
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<p>Surface hydrophobicity of white bean protein concentrate compared with commercial soy protein isolate and pea protein concentrate. The letters a, b, and c indicate significant differences between the data in the same column (<span class="html-italic">p</span>-value &lt; 0.05). Bound BPB refers to the amount of Bromophenol Blue bound to proteins, with the unit of measurement expressed in micrograms (µg), indicating the quantity of this substance or the complexes formed.</p>
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<p>Solubility of white bean protein concentrate as a function of pH variation. Solubility is expressed as the amount of protein (g) dissolved in 100 g of water, showing variation with pH. The points represent the experimental measurements.</p>
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<p>Solubility of white bean protein concentrate as a function of NaCl concentration. Solubility is expressed as the amount of protein (g) dissolved in 100 g of water. The points represent the experimental measurements.</p>
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<p>Correlation between glucose concentration (M) and protein solubility (g of protein per 100 g of water): the curve represents the variation in protein solubility as a function of glucose concentration.</p>
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<p>Comparison of foam functional properties at different pH levels and protein sources. (<b>A</b>) Foam capacity (FC%) of proteins from white bean, soybean, and pea at pH 4 and pH 7. Bars represent mean values ± standard error and different letters indicate statistically significant differences (<span class="html-italic">p</span> &lt; 0.05) within the same pH range. (<b>B</b>) Foam stability (FS%) over time (0–60 min) for the same protein sources at pH 4 and pH 7. Stability is represented by the remaining foam fraction over time, with distinct symbols used for each condition.</p>
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<p>Minimum gelation capacity of white bean protein concentrate. The images represent the behavior of proteins at increasing concentrations (2% to 22%) and the corresponding gel formation. The samples are classified into three categories, absence of gel (2%, 6%, 10%), weak gel formation (16%), and firm gel formation (20%, 22%), indicating the dependence of the protein concentration on gel structuring.</p>
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<p>Rheological behavior of white bean, soy, and pea protein gels as a function of frequency. The figures present the elastic (<span class="html-italic">G</span>′) and viscous (<span class="html-italic">G</span>″) moduli as a function of frequency (0.01–10 Hz) for white bean protein (<b>upper</b> part) and soy and pea proteins (<b>lower</b> part). The results show the rheological dependence of the protein systems, highlighting the formation of distinct structural networks.</p>
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<p>Deformation resistance of white bean, soy, and pea protein gels. The figures present the elastic (<span class="html-italic">G</span>′) and viscous (<span class="html-italic">G</span>″) moduli as a function of shear strain (%): (<b>A</b>) white bean protein gels; (<b>B</b>) soy and pea protein gels. The analysis demonstrates the structural stability of the gels under increasing deformation, indicating the structural rupture point at different protein concentrations.</p>
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<p>Water-holding capacity (WHC) and oil-holding capacity (OHC) of white bean protein concentrate, pea protein concentrate, and soy protein isolate. The water-holding capacity (WHC) is presented on the left axis (gray bars) and the oil-holding capacity (OHC) on the right axis (red bars). The bars represent the mean ± standard deviation. Different letters indicate statistically significant differences (<span class="html-italic">p</span> &lt; 0.05) between groups for each evaluated parameter. WHC is expressed in g of water per g of protein, while OHC is expressed in g of oil per g of protein.</p>
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<p>Turbiscan Stability Index (TSI) as a function of time (seconds) for emulsions formulated with white bean (WB), soy (SB), and pea (PEA) proteins at different pH values and oil/water ratios. The samples were evaluated at pH 4 and pH 7, with oil/water ratios of 2:1 and 1:1. The symbols represent the different treatments. The evolution of the TSI values reflects the stability of the emulsions, with lower values indicating greater stability.</p>
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13 pages, 2555 KiB  
Article
Peanut and Soy Protein-Based Emulsion Gels Loaded with Curcumin as a New Fat Substitute in Sausages: A Comparative Study
by Hong-Yan Yan and Shao-Bing Zhang
Gels 2025, 11(1), 62; https://doi.org/10.3390/gels11010062 - 13 Jan 2025
Viewed by 600
Abstract
The aim of this study was to evaluate the effects of the complete or partial substitution (0, 20, 40, and 100%) of the pork backfat in prepared sausage with protein emulsion gels loaded with curcumin. The effects of three protein emulsion gels (i.e., [...] Read more.
The aim of this study was to evaluate the effects of the complete or partial substitution (0, 20, 40, and 100%) of the pork backfat in prepared sausage with protein emulsion gels loaded with curcumin. The effects of three protein emulsion gels (i.e., peanut proteins, ultrasound-modified peanut proteins, and soy proteins) on sausage characteristics (cooking loss, textural properties, microstructure, sensory characteristics, and antioxidant activity) were investigated and compared using a one-way analysis of variance and Duncan’s multiple tests. The results revealed that the addition of each emulsion gel reduced cooking loss and improved the textural properties of the sausages in a dose-dependent manner. When 20% of pork backfat was substituted with untreated or ultrasound-modified peanut protein emulsion gel (PPEG), cooking loss decreased to a greater extent than when soy protein emulsion gel (SPEG) was used. However, the latter yielded higher cohesiveness and resilience at the same substitution levels. Compared with untreated PPEG, the sausages containing modified PPEG (at 200 W for 20 min) had significantly greater resilience and a denser microstructure. In addition, when 100% of pork backfat was substituted with modified PPEG, the sausages had desirable sensory characteristics. All sausages enriched with protein emulsion gels loaded with curcumin presented higher DPPH and ABTS radical scavenging capacities than the control sausages. The sausages prepared with the modified PPEG had the highest antioxidant activity (DPPH: 37.43 ± 0.35%; ABTS: 39.48 ± 0.50%; TBARS: 0.65 ± 0.05 mg MDA/Kg), which may be attributed to the increased stability of curcumin in the modified PPEG with a denser network structure. Therefore, ultrasound-modified PPEG loaded with curcumin can be used as a new fat substitute in functional sausages or other healthy meat products. Full article
(This article belongs to the Special Issue Recent Developments in Food Gels (2nd Edition))
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<p>Cooking loss from sausages after replacing pork backfat with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. Values are mean ± standard error (<span class="html-italic">n</span> = 3). Different letters indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Juice loss from sausages after replacing pork backfat with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. Values are mean ± standard error (<span class="html-italic">n</span> = 3). Different letters indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Appearance, cross-sections, and SEM images of sausages after replacing pork backfat with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. SEM images represent cross-sections of freeze-dried sausages. The bars in the SEM images indicate a length of 500 μm. Holes and gel clumps in the surface (cross-section) are indicated by red arrows and circles, respectively.</p>
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<p>Appearance, cross-sections, and SEM images of sausages after replacing pork backfat with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. SEM images represent cross-sections of freeze-dried sausages. The bars in the SEM images indicate a length of 500 μm. Holes and gel clumps in the surface (cross-section) are indicated by red arrows and circles, respectively.</p>
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<p>Radical scavenging capacity of freshly cooked sausages with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. Values are mean ± standard error (<span class="html-italic">n</span> = 3). Different letters indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>TBARS values for fresh cooked sausages with different protein emulsion gels. Control: without emulsion gel; PPEG: peanut protein emulsion gel; UPPEG: ultrasound-modified peanut protein emulsion gel; SPEG: soy protein emulsion gel. Values are mean ± standard error (<span class="html-italic">n</span> = 3). Different letters indicate significant differences (<span class="html-italic">p</span> &lt; 0.05).</p>
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