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22 pages, 11317 KiB  
Article
Exploring 3D Printing in Drug Development: Assessing the Potential of Advanced Melt Drop Deposition Technology for Solubility Enhancement by Creation of Amorphous Solid Dispersions
by Nabil Lamrabet, Florian Hess, Philip Leidig, Andreas Marx and Thomas Kipping
Pharmaceutics 2024, 16(12), 1501; https://doi.org/10.3390/pharmaceutics16121501 - 22 Nov 2024
Viewed by 1356
Abstract
Background: Melt-based 3D printing technologies are currently extensively evaluated for research purposes as well as for industrial applications. Classical approaches often require intermediates, which can pose a risk to stability and add additional complexity to the process. The Advanced Melt Drop Deposition (AMDD) [...] Read more.
Background: Melt-based 3D printing technologies are currently extensively evaluated for research purposes as well as for industrial applications. Classical approaches often require intermediates, which can pose a risk to stability and add additional complexity to the process. The Advanced Melt Drop Deposition (AMDD) technology, is a 3D printing process that combines the principles of melt extrusion with pressure-driven ejection, similar to injection molding. This method offers several advantages over traditional melt-based 3D printing techniques, making it particularly suitable for pharmaceutical applications. Objectives: This study evaluates the AMDD printing system for producing solid oral dosage forms, with a primary focus on the thermo-stable polymer polyvinyl alcohol (PVA). The suitability of AMDD technology for creating amorphous solid dispersions (ASDs) is also examined. Finally, the study aims to define the material requirements and limitations of the raw materials used in the process. Methods: The active pharmaceutical ingredients (APIs) indometacin and ketoconazole were used, with PVA 4-88 serving as the carrier polymer. Powders, wet granulates, and pellets were investigated as raw materials and characterized. Dissolution testing and content analyses were performed on the printed dosage forms. Solid-state characterization was conducted using differential scanning calorimetry (DSC) and X-ray diffraction (XRD). Degradation due to thermal and mechanical stress was analyzed using nuclear magnetic resonance spectroscopy (NMR). Results/Conclusions: The results demonstrate that the AMDD 3D printing process is well-suited for producing solid dosage forms. Tablets were successfully printed, meeting mass uniformity standards. Adjusting the infill volume from 30% to 100% effectively controlled the drug release rate of the tablets. Solid-state analysis revealed that the AMDD process can produce amorphous solid dispersions with enhanced solubility compared to their crystalline form. The experiments also demonstrated that powders with a particle size of approximately 200 µm can be directly processed using AMDD technology. Full article
(This article belongs to the Special Issue Impact of Raw Material Properties on Solid Dosage Form Processes)
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Graphical abstract

Graphical abstract
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<p>Illustration of the AMDD technology. 1. The API and polymer are introduced into the plasticizer barrel. 2. In the heated plasticizer barrel, the polymer–API mixture is melted. 3. A screw mechanism conveys the molten material toward the printing head, generating pressure through its motion. 4. The molten polymer–API mass is directed into the nozzle chamber. 5. The molten polymer–API mixture is then precisely ejected in the form of individual droplets, controlled by a piezo actuator that modulates a nozzle closure mechanism.</p>
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<p>(<b>A</b>): Complex viscosity against temperature. (<b>B</b>): Phase angle δ against temperature; for PVA and PVA/API mixtures, API proportion is 10%, means of n = 3 ± SD.</p>
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<p>(<b>Left</b>): Strand produced with HME pellets containing PVA 4-88 and 10% KTZ; (<b>Right</b>): Determination of FF using five cubes with different FF (20 mm × 20 mm × 4 mm).</p>
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<p>SEM images of 3DP tablets created with HME pellets (variation of infill volume).</p>
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<p>SEM image of a 3DP tablet with 30% infill volume produced with HME pellets.</p>
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<p>Mass distribution of 3DP placebo tablets produced with different intermediates n = 10 (specifications according to Ph. Eur.).</p>
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<p>Mass deviation of 3DP tablets produced with hme pellets and APIs (10%).</p>
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<p>PXRD patterns of the various intermediates and the printed tablets printed from them, (<b>left</b>): PVA with 10% IND, (<b>right</b>): PVA with 10% KTZ.</p>
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<p>DSC thermograms of the crystalline API, the various intermediates (API-PVA combinations with a drug load of 10%), and the tablets printed from these intermediates, also with a drug load of 10%. (<b>Left</b>): PVA with IND; (<b>Right</b>): PVA with KTZ.</p>
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<p>Molecular structure of PVA (<b>left</b>) and the model compound IND (<b>right</b>).</p>
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<p>NMR results of PVA, IND, HME pellets IND (10%), and 3DP tablets of HME pellets.</p>
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<p>NMR results of pure PVA, HME pellets, and 3DP tablets of HME pellets.</p>
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<p>Left: Dissolution profile of 3DP tablets with different infill volumes in 900 mL 0.1 M HCL, Mean value ± SD, n = 3.</p>
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<p>Dissolution profile of 3DP tablets with 10% KTZ in 100 mL FaSSiF (pH = 6.5), Mean Value ± SD, n = 3.</p>
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<p>Dissolution profile of 3DP tablets produced from HME pellets with different infill volumes in 900 mL SGF Mean Value ± SD, n = 3.</p>
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13 pages, 3053 KiB  
Article
Alkali-Activated Binders as Sustainable Alternatives to Portland Cement and Their Resistance to Saline Water
by Erion Luga, Enea Mustafaraj, Marco Corradi and Cengiz Duran Atiș
Materials 2024, 17(17), 4408; https://doi.org/10.3390/ma17174408 - 6 Sep 2024
Viewed by 1061
Abstract
Alkali-activated binders have emerged as promising alternatives to Ordinary Portland Cement (OPC) due to their sustainability features and potential advantages. This study evaluates the durability properties of heat-cured fly ash (FA) and ground granulated blast-furnace slag (GGBFS) geopolymer mortars activated with sodium hydroxide, [...] Read more.
Alkali-activated binders have emerged as promising alternatives to Ordinary Portland Cement (OPC) due to their sustainability features and potential advantages. This study evaluates the durability properties of heat-cured fly ash (FA) and ground granulated blast-furnace slag (GGBFS) geopolymer mortars activated with sodium hydroxide, which were subjected to wet–dry cycling in saline environments. Three series of FA, a FA/GGBFS blend, and GGBFS mortars previously optimized on a compressive strength basis were investigated and compared against two control OPC mixes. Performance indicators such as the water absorption, porosity, flexural strength, and compressive strength were analyzed. The results demonstrate that geopolymer mortars have significantly reduced water absorption and porosity with increasing wet–dry cycles. The compressive strength of the FA/GGBFS mortars also increased from 66.5 MPa (untreated) to 87.9 MPa over 45 cycles. The flexural strength remained stable or improved slightly across all geopolymer mortars. The control OPC specimens experienced significant deterioration, with compressive strength in CEM I 42.5R dropping from 51.8 to 17.1 MPa. These findings highlight the superior durability of geopolymer mortars under harsh saline conditions, demonstrating their potential as a resilient alternative for coastal and marine structures. Full article
(This article belongs to the Section Construction and Building Materials)
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<p>Historical development of AAMs [<a href="#B4-materials-17-04408" class="html-bibr">4</a>].</p>
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<p>(<b>a</b>) Samples under saline treatment. (<b>b</b>) Drying of mortar specimen for wet–dry treatment.</p>
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<p>Water absorption results under wet–dry cycling.</p>
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<p>Porosity values under wet–dry cycling.</p>
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<p>Flexural test of mortar prisms.</p>
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<p>Flexural strength values under wet–dry cycling.</p>
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<p>Compressive strength values under wet–dry cycling.</p>
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<p>Compressive strength changes (%) under wet–dry cycling.</p>
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23 pages, 27188 KiB  
Article
Durability Performance of CGF Stone Waste Road Base Materials under Dry–Wet and Freeze–Thaw Cycles
by Zimou Wang, Junjie Yang and Yalei Wu
Materials 2024, 17(17), 4272; https://doi.org/10.3390/ma17174272 - 29 Aug 2024
Viewed by 670
Abstract
The disposal of stone waste derived from the stone industry is a worldwide problem. The shortage of landfills, as well as transport costs and environmental pollution, pose a crucial problem. Additionally, as a substitute for cement that has high carbon emissions, energy consumption, [...] Read more.
The disposal of stone waste derived from the stone industry is a worldwide problem. The shortage of landfills, as well as transport costs and environmental pollution, pose a crucial problem. Additionally, as a substitute for cement that has high carbon emissions, energy consumption, and pollution, the disposal of stone wastes by utilizing solid waste-based binders as road base materials can achieve the goal of “waste for waste”. However, the mechanical properties and deterioration mechanism of solid waste-based binder solidified stone waste as a road base material under complex environments remains incompletely understood. This paper reveals the durability performance of CGF all-solid waste binder (consisting of calcium carbide residue, ground granulated blast furnace slag, and fly ash) solidified stone waste through the macro and micro properties under dry–wet and freeze–thaw cycling conditions. The results showed that the dry–wet and freeze–thaw cycles have similar patterns of impacts on the CGF and cement stone waste road base materials, i.e., the stress–strain curves and damage forms were similar in exhibiting the strain-softening type, and the unconfined compressive strengths all decreased with the number of cycles and then tended to stabilize. However, the influence of dry–wet and freeze–thaw cycles on the deterioration degree was significantly different; CGF showed excellent resistance to dry–wet cycles, whereas cement was superior in freeze–thaw resistance. The deterioration grade of CGF and cement ranged from 36.15 to 47.72% and 39.38 to 47.64%, respectively, after 12 dry–wet cycles, whereas it ranged from 57.91 to 64.48% and 36.61 to 40.00% after 12 freeze–thaw cycles, respectively. The combined use of MIP and SEM confirmed that the deterioration was due to the increase in the porosity and cracks induced by dry–wet and freeze–thaw cycles, which in turn enhanced the deterioration phenomenon. This can be ascribed to the fact that small pores occupy the largest proportion and contribute to the deterioration process, and the deterioration caused by dry–wet cycles is associated with the formation of large pores through the connection of small pores, while the freeze–thaw damage is due to the increase in medium pores that are more susceptible to water intrusion. The findings provide theoretical instruction and technical support for utilizing solid waste-based binders for solidified stone waste in road base engineering. Full article
(This article belongs to the Section Construction and Building Materials)
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Figure 1
<p>Stone production and road base material durability in China: (<b>a</b>) Stone production in China. (<b>b</b>) Durability of road base materials.</p>
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<p>Apparent state of stone waste and cementitious materials. (<b>A</b>) Apparent condition of stone waste. (<b>B</b>) Figure of cementitious material.</p>
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<p>SEM images of stone waste (the size unit marked on the particle in the figure: mm). (<b>a</b>) SEM images of stone waste (500 X). (<b>b</b>) SEM images of stone waste (1000 X). (<b>c</b>) SEM images of stone waste (5000 X).</p>
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<p>Particle size distribution curves of each component of binder and test soil.</p>
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<p>XRD patterns of materials. (<b>A</b>) XRD patterns and chemical composition of stone waste. (<b>B</b>) XRD patterns of the components of CGF.</p>
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<p>Test process.</p>
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<p>Apparent characteristics of the stone waste road base material under the action of dry–wet cycling: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>Apparent characteristics of stone waste road base material under freeze–thaw cycle: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>Quality loss rate of stone waste road base material in wet–dry cycle: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>Quality loss rate of stone waste road base material in freeze–thaw cycle: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>The strength of stone waste road base material varies with the number of dry–wet cycles.: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>The deterioration degree of stone waste road base material changes with the number of dry–wet cycles: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>The strength of stone waste road base material varies with the number of freeze–thaw cycles: (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>The deterioration degree of the stone waste road base material changes with the number of freeze–thaw cycles. (<b>a</b>) CGF stone waste road base material. (<b>b</b>) Cement stone waste road base material.</p>
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<p>Relationship curves between cumulative mercury intake and pressure.</p>
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<p>The pore diameter differential distribution curves of the stone waste road base materials.</p>
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<p>The pore diameter differential distribution curves of the stone waste road base materials.</p>
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<p>The relationship between <span class="html-italic">lnV</span> and <span class="html-italic">lnS</span>.</p>
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<p>The relationship between <span class="html-italic">lnV</span> and <span class="html-italic">lnS</span>.</p>
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<p>Schematic diagram of microstructure evolution of CGF stone waste road base material sample under dry–wet cycling.</p>
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<p>Schematic diagram of microstructure evolution of cement stone waste road base material sample under dry–wet cycling.</p>
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<p>Schematic diagram of microstructure evolution of CGF stone waste road base material sample under freeze–thaw cycling.</p>
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<p>Schematic diagram of microstructure evolution of cement stone waste road base material sample under freeze–thaw cycling.</p>
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<p>Schematic diagram of freeze–thaw cycle mechanism.</p>
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27 pages, 5979 KiB  
Article
Development and Characterization of Basalt Fiber-Reinforced Green Concrete Utilizing Coconut Shell Aggregates
by Muhammed Talha Ünal, Huzaifa Bin Hashim, Hacı Süleyman Gökçe, Pouria Ayough, Fuat Köksal, Ahmed El-Shafie, Osman Şimşek and Alireza Pordesari
Sustainability 2024, 16(17), 7306; https://doi.org/10.3390/su16177306 - 25 Aug 2024
Viewed by 1411
Abstract
Lightweight aggregate concrete (LWAC) is gaining interest due to its reduced weight, high strength, and durability while being cost-effective. This research proposes a method to design an LWAC by integrating coconut shell (CS) as coarse lightweight aggregate and a high volume of wet-grinded [...] Read more.
Lightweight aggregate concrete (LWAC) is gaining interest due to its reduced weight, high strength, and durability while being cost-effective. This research proposes a method to design an LWAC by integrating coconut shell (CS) as coarse lightweight aggregate and a high volume of wet-grinded ultrafine ground granulated blast furnace slag (UGGBS). To optimize the mix design of LWAC, a particle packing model was employed. A comparative analysis was conducted between normal-weight concrete (M40) and the optimized LWAC reinforced with basalt fibers (BF). The parameters analyzed include CO2 emissions, density, surface crack conditions, water absorption and porosity, sorptivity, and compressive and flexural strength. The optimal design was determined using the packing density method. Also, the impact of BF was investigated at varying levels (0%, 0.15%, and 1%). The results revealed that the incorporation of UGGBS had a substantial enhancement to the mechanical properties of LWAC when BF and CS were incorporated. As a significant finding of this research, a grade 30 LWAC with demolded density of 1864 kg/m3 containing only 284 kg/m3 cement was developed. The LWAC with high-volume UGGBS and BF had the minimum CO2 emissions at 390.9 kg/t, marking a reduction of about 31.6% compared to conventional M40-grade concrete. This research presents an introductory approach to sustainable, environmentally friendly, high-strength, and low-density concrete production by using packing density optimization, thereby contributing to both environmental conservation and structural outcomes. Full article
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Figure 1
<p>Flowchart for the optimization of the mechanical response of basalt fiber-reinforced green high-strength lightweight aggregate concrete (HSLWAC) with a coconut shell aggregate.</p>
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<p>Conceptual visualization of a highly packed matrix.</p>
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<p>Size of the employed coconut shells and basalt fibers.</p>
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<p>Packing density of coconut shells in (<b>a</b>) loose, (<b>b</b>) compacted conditions, and (<b>c</b>) optimum volume for coconut shell coarse aggregates.</p>
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<p>Packing density of fine aggregates with fractions of FA:P:F.</p>
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<p>Packing density of fine to coarse aggregate.</p>
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<p>Wet milling process: (<b>a</b>) equipment, (<b>b</b>) grinding process, and (<b>c</b>) the production of ultra-grinded grounded blast slag.</p>
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<p>Effect of grinding media: (<b>a</b>) underloading, (<b>b</b>) normal loading, and (<b>c</b>) overloading on milling efficiency [<a href="#B66-sustainability-16-07306" class="html-bibr">66</a>].</p>
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<p>Effect of UGGBS slurry replacement on the compressive strength of cementitious paste.</p>
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<p>Fresh and packing density values of the mixtures.</p>
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<p>Illustration for the effect of (<b>a</b>) rigid and (<b>b</b>) flexible fibers on packing density [<a href="#B76-sustainability-16-07306" class="html-bibr">76</a>].</p>
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<p>Surface cracks of concrete samples after water curing at 28 days.</p>
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<p>Sorptivity test results by square root of time.</p>
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<p>Compressive strength results of mixtures at different curing days.</p>
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<p>28-day flexural strength values of mixtures.</p>
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<p>Cracks of concrete samples after the flexural strength test.</p>
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<p>Enhanced visualization of maximum solid content LWAC.</p>
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30 pages, 9109 KiB  
Article
Development and Evaluation of a Dry Emulsion of Ostrich Oil as a Dietary Supplement
by Juthaporn Ponphaiboon, Sontaya Limmatvapirat and Chutima Limmatvapirat
Foods 2024, 13(16), 2570; https://doi.org/10.3390/foods13162570 - 17 Aug 2024
Viewed by 989
Abstract
This study aimed to develop a high-quality dry emulsion incorporating omega-3, 6, and 9 fatty acid-rich ostrich oil for use as a dietary supplement. Extracted from abdominal adipose tissues using a low-temperature wet rendering method, the ostrich oil exhibited antioxidant properties, favorable physicochemical [...] Read more.
This study aimed to develop a high-quality dry emulsion incorporating omega-3, 6, and 9 fatty acid-rich ostrich oil for use as a dietary supplement. Extracted from abdominal adipose tissues using a low-temperature wet rendering method, the ostrich oil exhibited antioxidant properties, favorable physicochemical properties, microbial counts, heavy metal levels, and fatty acid compositions, positioning it as a suitable candidate for an oil-in-water emulsion and subsequent formulation as a dry emulsion. Lecithin was employed as the emulsifier due to its safety and health benefits. The resulting emulsion, comprising 10% w/w lecithin and 10% w/w ostrich oil, was stable, with a droplet size of 3.93 ± 0.11 μm. This liquid emulsion underwent transformation into a dry emulsion to preserve the physicochemical stability of ostrich oil, utilizing Avicel® PH-101 or Aerosil® 200 through a granulation process. Although Aerosil® 200 exhibited superior adsorption, Avicel® PH-101 granules surpassed it in releasing the ostrich oil emulsion. Consequently, Avicel® PH-101 was selected as the preferred adsorbent for formulating the ostrich oil dry emulsion. The dry emulsion, encapsulated with a disintegration time of 3.11 ± 0.14 min for ease of swallowing, maintained microbial loads and heavy metal contents within acceptable limits. Presented as granules containing butylated hydroxytoluene, the dry emulsion showcased robust temperature stability, suggesting the potential incorporation of animal fat into dry emulsions as a promising dietary supplement. Full article
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Figure 1
<p>Appearances of the emulsions comprising 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 1% <span class="html-italic">w</span>/<span class="html-italic">w</span> to 15% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin on days 1, 3, and 7 (L01 to L15 represent lecithin concentrations ranging from 1% <span class="html-italic">w</span>/<span class="html-italic">w</span> to 15% <span class="html-italic">w</span>/<span class="html-italic">w</span>).</p>
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<p>Appearances of the emulsions comprising 5% <span class="html-italic">w</span>/<span class="html-italic">w</span> to 30% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin on days 1, 3, and 7 (O-05 to O-30 represent ostrich oil concentrations ranging from 5% <span class="html-italic">w</span>/<span class="html-italic">w</span> to 30% <span class="html-italic">w</span>/<span class="html-italic">w</span>).</p>
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<p>The viscosity of emulsions containing 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 1% <span class="html-italic">w</span>/<span class="html-italic">w</span>–15% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>The viscosity of emulsions containing 5% <span class="html-italic">w</span>/<span class="html-italic">w</span>–30% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>The droplet size of emulsions containing 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 1% <span class="html-italic">w</span>/<span class="html-italic">w</span>–15% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>The droplet size of emulsions containing 5% <span class="html-italic">w</span>/<span class="html-italic">w</span>–30% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>Photomicrographs of emulsions containing 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 1% <span class="html-italic">w</span>/<span class="html-italic">w</span>–15% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>Photomicrographs of emulsions containing 5% <span class="html-italic">w</span>/<span class="html-italic">w</span>–30% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>The zeta potential of emulsions containing 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 1% <span class="html-italic">w</span>/<span class="html-italic">w</span>–15% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>The zeta potential of emulsions containing 5% <span class="html-italic">w</span>/<span class="html-italic">w</span>–30% <span class="html-italic">w</span>/<span class="html-italic">w</span> ostrich oil and 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> lecithin.</p>
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<p>Appearances of the dry emulsions prepared using Avicel<sup>®</sup> PH-101 (<b>A</b>) and Aerosil<sup>®</sup> 200 (<b>B</b>) as adsorbents.</p>
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<p>Visual observations of Avicel<sup>®</sup> PH-101 and Aerosil<sup>®</sup> 200 granules containing ostrich oil emulsion reconstituted with distilled water at room temperature before (<b>A</b>) and after (<b>B</b>) centrifugation, along with their dry sediments (<b>C</b>). The initial weight of the dry emulsion and the remaining weight (dry sediment) were used to calculate the percentage of weight loss after oil release.</p>
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<p>Photomicrographs of Avicel<sup>®</sup> PH-101 (<b>upper</b>) and Aerosil<sup>®</sup> 200 (<b>lower</b>) granules containing ostrich oil emulsion reconstituted with distilled water at room temperature before (<b>A</b>) and after (<b>B</b>) centrifugation.</p>
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<p>Scanning electron microscopy (SEM) images of Avicel<sup>®</sup> PH-101 granules containing ostrich oil emulsion (<b>A</b>), Avicel<sup>®</sup> PH-101 (<b>B</b>), and lecithin (<b>C</b>).</p>
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<p>Scanning electron microscopy-energy-dispersive X-ray spectroscopy (SEM-EDS) images of Avicel<sup>®</sup> PH-101 (<b>A</b>), lecithin (<b>B</b>), and Avicel<sup>®</sup> PH-101 granules containing ostrich oil emulsion stored at 4 °C (<b>C</b>) and 45 °C (<b>D</b>), RH 75 ± 2%. The peak at 2.01 keV (indicated by the green circle) corresponds to the phosphate element, while the peak at 2.12 keV (marked by the blue arrow) is attributed to the gold element.</p>
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<p>Visual aspects of Avicel<sup>®</sup> PH-101 granules containing ostrich oil emulsion at the onset of storage (<b>A</b>) and following 180 days of storage at 4 °C (<b>B</b>), 25 °C (<b>C</b>), and 45 °C (<b>D</b>).</p>
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<p>Scanning electron microscopy (SEM) images of Avicel<sup>®</sup> PH-101 granules containing ostrich oil emulsion at the initial time (<b>A</b>) and after 180 days of storage at 4 °C (<b>B</b>), 25 °C (<b>C</b>), and 45 °C (<b>D</b>).</p>
Full article ">
16 pages, 4753 KiB  
Article
Application of Galenic Strategies for Developing Gastro-Resistant Omeprazole Formulation for Pediatrics
by Khadija Rouaz-El-Hajoui, Encarnación García-Montoya, Marc Suñé-Pou, Josep María Suñé-Negre and Pilar Pérez-Lozano
Children 2024, 11(8), 945; https://doi.org/10.3390/children11080945 - 5 Aug 2024
Viewed by 1241
Abstract
Objectives: This study addresses a critical need in pediatric pharmacotherapy by focusing on the development of an enteric formulation of omeprazole for pediatric use. Omeprazole, a widely used proton pump inhibitor, is essential for treating various gastrointestinal disorders in children. The main objective [...] Read more.
Objectives: This study addresses a critical need in pediatric pharmacotherapy by focusing on the development of an enteric formulation of omeprazole for pediatric use. Omeprazole, a widely used proton pump inhibitor, is essential for treating various gastrointestinal disorders in children. The main objective is to design a compounding formula that can be prepared in hospital pharmacy services without the need for industrial equipment, which is often unavailable in these settings. Methods: The research applied different galenic strategies to overcome the challenges of omeprazole’s instability in acidic environments and its complex pharmacokinetic and physicochemical properties. The experiments were conducted sequentially, employing salting out, ionic gelation, and matrix granulation strategies. Based on the results obtained, the control conditions and parameters for the various trials were established. Results: Among the techniques used, wet granulation proved to be the most promising, achieving a gastro-resistance level of 44%. In contrast, the ionic gelation and salting-out techniques did not yield satisfactory results. Conclusions: The findings of this study underscore the need to adopt alternative formulation strategies to ensure the stability of omeprazole. This goal requires a multidisciplinary approach and continuous effort to design omeprazole formulations that meet quality standards and appropriate gastro-resistance requirements. Full article
(This article belongs to the Special Issue Advances in Pediatric Formulations Update)
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<p>Schematic representation of the experiments conducted using the salting-out methodology. In Experiment 2, the aqueous solutions were alkalinized, in contrast to Experiment 1.</p>
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<p>pH 1.2 medium. Left image: omeprazole 2 mg/mL suspension in xanthan gum at 0 min. Right image: omeprazole 2 mg/mL suspension in xanthan gum at 5 min.</p>
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<p>Left image: pH 2.2 medium; omeprazole 2 mg/mL suspension in xanthan gum at 5 min. Right image: pH 4.5 medium; omeprazole 2 mg/mL suspension in xanthan gum at 5 min.</p>
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<p>The three pH media after 1 h and 15 min. Left: pH 1.2 medium. Middle: pH 2.2 medium. Right: pH 4.5 medium.</p>
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<p>The three pH media after 2 h. Left: pH 1.2 medium (yellow color). Middle: pH 2.2 medium (light brown color). Right: pH 4.5 medium (pink color).</p>
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<p>pH 1.2 medium with omeprazole base. Left image: 10 min after adding 20 mg of omeprazole base. Right image: 2 h after adding 20 mg of omeprazole base.</p>
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<p>Left image: pH 1.2 medium with placebo. No color change was observed after 2 h. Right image: pH 1.2 medium with enteric-coated omeprazole pellets. No color change was observed after 2 h.</p>
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<p>Left: microspheres from Experiment 2. Middle: microspheres from Experiment 3. Right: microspheres from Experiment 3 after the drying process.</p>
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<p>Left: microspheres from Experiment 2. Right: microspheres from Experiment 3 in acidic medium.</p>
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<p><b>Left</b>: appearance of the emulsion after 10 min of mechanical agitation with paddles. <b>Right</b>: appearance of the emulsion after 60 min of mechanical agitation with paddles.</p>
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<p>Appearance of the microspheres after the drying process.</p>
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<p>Chromatogram of omeprazole.</p>
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<p>Chromatogram of omeprazole microspheres produced via ionic gelation.</p>
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<p>Chromatogram of omeprazole microspheres produced via salting out.</p>
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<p>Chromatogram of omeprazole microspheres produced via wet granulation.</p>
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<p>Schematic representation of the results obtained, and the possible alternatives proposed for obtaining gastro-resistant microspheres of omeprazole.</p>
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18 pages, 3528 KiB  
Article
Physicochemical Characteristics of Porous Starch Obtained by Combined Physical and Enzymatic Methods—Part 2: Potential Application as a Carrier of Gallic Acid
by Agnieszka Ewa Wiącek and Monika Sujka
Molecules 2024, 29(15), 3570; https://doi.org/10.3390/molecules29153570 - 29 Jul 2024
Viewed by 833
Abstract
Wettability measurements were performed for aqueous dispersions of native and modified corn, potato, and pea starch granules deposited on glass plates by the thin layer method using test liquids of a different chemical nature (polar water and formamide or non-polar diiodomethane). High values [...] Read more.
Wettability measurements were performed for aqueous dispersions of native and modified corn, potato, and pea starch granules deposited on glass plates by the thin layer method using test liquids of a different chemical nature (polar water and formamide or non-polar diiodomethane). High values of the determination coefficient R2 confirm that the linear regression model describes the relationship between the wetting time and the square of the penetration distance very well, indicating the linear nature of the Washburn relationship. A change in free energy (enthalpy) during the movement of the liquid in the porous layer was determined for all starches before and after modification in contact with test liquids. Wetting times for polar liquids increased significantly (from 3 to 4 fold), especially for corn starch. The lower the value of the adhesive tension, the easier the wetting process takes place, and consequently, the adsorption process is facilitated. Adhesive tension for polar substances applies to the adsorption of hydrophilic substances, while in the case of apolar substances, adhesive tension applies to the adsorption of hydrophobic substances. For the adsorption of gallic acid on starch, the relationships obtained for polar substances are crucial. The adsorption of gallic acid by forming hydrogen bonds or, more generally, donor–acceptor (acid–base) bonds is definitely higher for corn starch than other starches. Therefore, this starch has the most significant potential for use as a carrier of gallic acid or, more broadly, compounds from the polyphenol group. Full article
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<p>Wetting times of native potato starch as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line, pentane—violet line).</p>
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<p>Wetting times of modified potato starch as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line, pentane—violet line).</p>
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<p>Wetting times of native pea starch as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line).</p>
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<p>Wetting times of modified pea starch as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line).</p>
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<p>Wetting times of native corn starches as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line).</p>
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<p>Wetting times of modified corn starch as a function of the penetration square distance of the tested liquid (water—blue line, formamide—claret line, diiodomethane—green line).</p>
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<p>Effect of pH (<b>a</b>), temperature (<b>b</b>), and phase contact time (<b>c</b>) on the adsorption of gallic acid on native starches (corn—blue line, potato—orange line, pea—gray line).</p>
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<p>Adsorption of gallic acid on native and modified starch (means with different letters are significantly different, <span class="html-italic">p</span> &lt; 0.05).</p>
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<p>ATR-FTIR spectra of starches: native (red), modified (green), and modified complexed with gallic acid (blue). Types of starches: (<b>a</b>) corn starch, (<b>b</b>) potato starch, (<b>c</b>) pea starch.</p>
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18 pages, 4244 KiB  
Article
Enhanced Stability and Compatibility of Montelukast and Levocetirizine in a Fixed-Dose Combination Monolayer Tablet
by Tae Han Yun, Moon Jung Kim, Jung Gyun Lee, Kyu Ho Bang and Kyeong Soo Kim
Pharmaceutics 2024, 16(7), 963; https://doi.org/10.3390/pharmaceutics16070963 - 21 Jul 2024
Viewed by 2079
Abstract
The purpose of this study was to enhance the stability of montelukast and levocetirizine for the development of a fixed-dose combination (FDC) monolayer tablet. To evaluate the compatibility of montelukast and levocetirizine, a mixture of the two drugs was prepared, and changes in [...] Read more.
The purpose of this study was to enhance the stability of montelukast and levocetirizine for the development of a fixed-dose combination (FDC) monolayer tablet. To evaluate the compatibility of montelukast and levocetirizine, a mixture of the two drugs was prepared, and changes in the appearance characteristics and impurity content were observed in a dry oven at 60 °C. Excipients that contributed minimally to impurity increases were selected to minimize drug interactions. Mannitol, microcrystalline cellulose, croscarmellose sodium, hypromellose, and sodium citrate were chosen as excipients, and montelukast–levocetirizine FDC monolayer tablets were prepared by wet granulating the two drugs separately. A separate granulation of montelukast and levocetirizine, along with the addition of sodium citrate as a pH stabilizer, minimized the changes in tablet appearance and impurity levels. The prepared tablets demonstrated release profiles equivalent to those of commercial products in comparative dissolution tests. Subsequent stability testing at 40 ± 2 °C and 75 ± 5% RH for 6 months confirmed that the drug content, dissolution rate, and impurity content met the specified acceptance criteria. In conclusion, the montelukast–levocetirizine FDC monolayer tablet developed in this study offers a potential alternative to commercial products. Full article
(This article belongs to the Special Issue Pharmaceutical Solid Forms: From Crystal Structure to Formulation)
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<p>Characteristics of the changes in the appearance of montelukast alone, levocetirizine alone, and both in a 1:1 mixture.</p>
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<p>(<b>A</b>) HPLC chart for the montelukast impurity analysis, and (<b>B</b>) HPLC chart for the levocetirizine impurity analysis.</p>
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<p>Results of (<b>A</b>) the total impurity content in montelukast, and (<b>B</b>) the total impurity content in levocetirizine for each drug and their mixture.</p>
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<p>Results of the (<b>A</b>) total impurity content in montelukast, and (<b>B</b>) the total impurity content in levocetirizine for each excipient.</p>
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<p>Comparison of (<b>A</b>) montelukast sulfoxide impurity, (<b>B</b>) the total impurity content of montelukast, (<b>C</b>) the specific impurity content of levocetirizine, and (<b>D</b>) the total impurity content of levocetirizine in the four formulations.</p>
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<p>Comparison of the changes in appearance characteristics between (<b>A</b>) the F3 tablet and (<b>B</b>) the F4 tablet.</p>
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<p>SEM-EDS mapping image of a F3 tablet cross-section.</p>
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<p>Comparison of the dissolution profiles of the montelukast–levocetirizine FDC monolayer tablet (F3 tablet) and montelukast commercial product (10 mg Singulair tablet) at (<b>A</b>) a pH of 1.2, (<b>B</b>) a pH of 4.0, (<b>C</b>) a pH of 6.8, and (<b>D</b>) in a 0.5% SLS. Each value represents the mean ± S.D. (n = 6).</p>
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<p>Comparison of the dissolution profiles of the montelukast–levocetirizine FDC monolayer tablet (F3 tablet) and levocetirizine commercial product (Xyzal 5 mg tablet) at (<b>A</b>) a pH of 1.2, (<b>B</b>) a pH of 4.0, (<b>C</b>) a pH of 6.8, and (<b>D</b>) in water. Each value represents the mean ± S.D. (n = 6).</p>
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<p>Stability test results over 6 months for the montelukast–levocetirizine FDC monolayer tablet (F3 tablet) regarding (<b>A</b>) drug content, (<b>B</b>) dissolution rate, (<b>C</b>) montelukast impurity content, and (<b>D</b>) levocetirizine impurity content.</p>
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14 pages, 4485 KiB  
Article
Film Coating of Phosphorylated Mandua Starch on Matrix Tablets for pH-Sensitive Release of Mesalamine
by Mayank Kumar Malik, Vipin Kumar, Vinoth Kumarasamy, Om Prakash Singh, Mukesh Kumar, Raghav Dixit, Vetriselvan Subramaniyan and Jaspal Singh
Molecules 2024, 29(13), 3208; https://doi.org/10.3390/molecules29133208 - 5 Jul 2024
Viewed by 1151
Abstract
Chemically modified mandua starch was successfully synthesized and applied to coat mesalamine-loaded matrix tablets. The coating material was an aqueous dispersion of mandua starch modified by sodium trimetaphosphate and sodium tripolyphosphate. To investigate the colon-targeting release competence, chemically modified mandua starch film-coated mesalamine [...] Read more.
Chemically modified mandua starch was successfully synthesized and applied to coat mesalamine-loaded matrix tablets. The coating material was an aqueous dispersion of mandua starch modified by sodium trimetaphosphate and sodium tripolyphosphate. To investigate the colon-targeting release competence, chemically modified mandua starch film-coated mesalamine tablets were produced using the wet granulation method followed by dip coating. The effect of the coating on the colon-targeted release of the resultant delivery system was inspected in healthy human volunteers and rabbits using roentgenography. The results show that drug release was controlled when the coating level was 10% w/w. The release percentage in the upper gastric phase (pH 1.2, simulated gastric fluid) was less than 6% and reached up to 59.51% w/w after 14 h in simulated colonic fluid. In addition to in vivo roentgenographic studies in healthy rabbits, human volunteer studies proved the colon targeting efficiency of the formulation. These results clearly demonstrated that chemically modified mandua starch has high effectiveness as a novel aqueous coating material for controlled release or colon targeting. Full article
(This article belongs to the Special Issue Polysaccharide-Based Biopolymer: Recent Development and Applications)
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<p>Comparative cumulative drug release (CDR%) of mesalamine in changing over media from native finger millet starch tablet (AMST), chemically modified finger millet starch uncoated tablet (PSTUC), chemically modified finger millet starch tablet with 10% <span class="html-italic">w</span>/<span class="html-italic">w</span> coating of chemically modified mandua starch (PSTCPST10%), marketed tablet (MKTF, mesalamine: 800 mg) (Ref. [<a href="#B22-molecules-29-03208" class="html-bibr">22</a>]).</p>
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<p>Roentgenography study of optimized phosphorylated mandua starch tablets in rabbits. Gastrointestinal transit of the colon-targeted tablets in rabbits: (<b>a</b>) 0 min, no tablet in the stomach; (<b>b</b>) 120 min, tablet approaching the small intestine; (<b>c</b>) 240 min, tablet approaching the small intestine; (<b>d</b>) 360 min, tablet reaches in the colon; and (<b>e</b>) 480 min, tablet in the colon.</p>
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<p>Empty stomach study of chemically modified mandua starch-coated tablet composed of phosphorylated mandua starch.</p>
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<p>Schematic representation of the procedure for the isolation and modification of mandua starch.</p>
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<p>Structure of finger millet starch after the phosphorylation process.</p>
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20 pages, 2426 KiB  
Article
Evaluation of Polyvinyl Alcohol as Binder during Continuous Twin Screw Wet Granulation
by Phaedra Denduyver, Gudrun Birk, Alessandra Ambruosi, Chris Vervaet and Valérie Vanhoorne
Pharmaceutics 2024, 16(7), 854; https://doi.org/10.3390/pharmaceutics16070854 - 25 Jun 2024
Viewed by 1954
Abstract
Binder selection is a crucial step in continuous twin-screw wet granulation (TSWG), as the material experiences a much shorter residence time (2–40 s) in the granulator barrel compared to batch-wise granulation processes. Polyvinyl alcohol (PVA) 4-88 was identified as an effective binder during [...] Read more.
Binder selection is a crucial step in continuous twin-screw wet granulation (TSWG), as the material experiences a much shorter residence time (2–40 s) in the granulator barrel compared to batch-wise granulation processes. Polyvinyl alcohol (PVA) 4-88 was identified as an effective binder during TSWG, but the potential of other PVA grades—differing in polymerization and hydrolysis degree—has not yet been studied. Therefore, the aim of the current study was to evaluate the potential of different PVA grades as a binder during TSWG. The breakage and drying behavior during the fluidized bed drying of drug-loaded granules containing the PVA grades was also studied. Three PVA grades (4-88, 18-88, and 40-88) were characterized and their attributes were compared to previously investigated binders by Vandevivere et al. through principal component analysis. Three binder clusters could be distinguished according to their attributes, whereby each cluster contained a PVA grade and a previously investigated binder. PVA 4-88 was the most effective binder of the PVA grades for both a good water-soluble and water-insoluble formulation. This could be attributed to its high total surface energy, low viscosity, good wettability of hydrophilic and hydrophobic surfaces, and good wettability by water of the binder. Compared to the previously investigated binders, all PVA grades were more effective in the water-insoluble formulation, as they yielded strong granules (friability below 30%) at lower L/S-ratios. This was linked to the high dispersive surface energy of the high-energy sites on the surface of PVA grades and their low surface tension. During fluidized bed drying, PVA grades proved suitable binders, as the acetaminophen (APAP) granules were dried within a short time due to the low L/S-ratio, at which high-quality granules could be produced. In addition, no attrition occurred, and strong tablets were obtained. Based on this study, PVA could be the preferred binder during twin screw granulation due to its high binder effectiveness at a low L/S-ratio, allowing efficient downstream processing. However, process robustness must be controlled by the included excipients, as PVA grades are operating in a narrow L/S-ratio range. Full article
(This article belongs to the Special Issue Impact of Raw Material Properties on Solid Dosage Form Processes)
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Graphical abstract
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<p>Screw configuration with material flow from left to right. Kneading zones consist of 6 kneading elements (length-to-diameter (L/D) 1/4) in a stagger angle of 60°. Granulation liquid was added just before the first kneading zone.</p>
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<p>The score (<b>a</b>) and loading (<b>b</b>) scatter plot of PC 1 versus PC 2. The different colors refer to the binder clusters, which have comparable binder attributes. Cluster 1 (red) contains PVA 4-88 and SOS CO01; cluster 2 (yellow) has PVA 18-88 and PVP K90; cluster 3 (blue) has PVA 40-88 and HPMC E15; and cluster 4 (green) has maltodextrin 6, HP pea starch, PVP K12, and PVP K30.</p>
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<p>The dispersive (<b>top</b>), specific (<b>middle</b>) and total (<b>bottom</b>) surface energy in the function of the fractional coverage for cluster 1, 2, and 3 binders. The specific and total surface energies of HPMC E15 could not be measured due to weak solvent interactions.</p>
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<p>SME values in function of the L/S-ratio for each binder in mannitol- and DCP-based formulations. L/S-ratios depicted are based on the L/S-ratio range from <a href="#pharmaceutics-16-00854-t001" class="html-table">Table 1</a>.</p>
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<p>Friability in function of the L/S-ratio for each binder in the mannitol- and DCP-based formulations. The L/S-ratios depicted are based on the L/S-ratio range from <a href="#pharmaceutics-16-00854-t001" class="html-table">Table 1</a>.</p>
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<p>Moisture content of the granules in function of drying time. Granules were produced on the L/S-ratio mentioned in <a href="#pharmaceutics-16-00854-t003" class="html-table">Table 3</a>.</p>
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<p>Breakage behavior of APAP granules with PVA grades. Solid line represents the particle size distribution of tray-dried granules (TDG). Dashed and dotted lines represent the particle size distribution after fluid bed drying at first and second drying times, respectively.</p>
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<p>Tensile strength in function of main compaction pressure for studied binders in APAP formulation.</p>
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22 pages, 14393 KiB  
Article
Pressure and Liquid Distribution under the Blade of a Basket Extruder of Continuous Wet Granulation of Model Material
by Roman Fekete, Peter Peciar, Martin Juriga, Štefan Gužela, Michaela Peciarová, Dušan Horváth and Marian Peciar
J. Manuf. Mater. Process. 2024, 8(3), 127; https://doi.org/10.3390/jmmp8030127 - 18 Jun 2024
Viewed by 1040
Abstract
This study explores the influence of blade design on the low-pressure extrusion process, which is relevant to techniques like spheronization. We investigate how blade geometry affects the extruded paste and final product properties. A model paste was extruded through a basket extruder with [...] Read more.
This study explores the influence of blade design on the low-pressure extrusion process, which is relevant to techniques like spheronization. We investigate how blade geometry affects the extruded paste and final product properties. A model paste was extruded through a basket extruder with varying blade lengths to create distinct wedge gaps (20°, 26° and 32° contact angles). The theoretical analysis explored paste behavior within the gap and extrudate. A model material enabled objective comparison across blade shapes. Our findings reveal a significant impact of blade design on the pressure profile, directly influencing liquid distribution in the paste and extrudate. It also affects the required torque relative to extruder output. The findings of this study hold significant implications for continuous granulation, a technique employed in the pharmaceutical industry for producing granules with uniform size and properties. Understanding the influence of blade geometry on the extrusion process can lead to the development of optimized blade designs that enhance granulation efficiency, improve product quality, and reduce energy consumption. By tailoring blade geometry, manufacturers can achieve more consistent granule characteristics, minimize process variability, and ultimately produce pharmaceuticals with enhanced efficacy. Full article
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<p>Configuration of the paste skeleton of different materials: (1) sand; (2) very finely ground limestone; (3) a mixture of sand and very finely ground limestone. <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>1</mn> </mrow> </msub> <mo>&gt;</mo> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>2</mn> </mrow> </msub> <mo>&lt;</mo> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>3</mn> </mrow> </msub> </mrow> </semantics></math>, <math display="inline"><semantics> <mrow> <mo>∆</mo> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>1</mn> </mrow> </msub> <mo>&lt;</mo> <mo>∆</mo> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>2</mn> </mrow> </msub> <mo>&gt;</mo> <mo>∆</mo> <msub> <mrow> <mi>ε</mi> </mrow> <mrow> <mn>3</mn> </mrow> </msub> </mrow> </semantics></math>.</p>
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<p>Radial extruder with the different geometries of the extrusion blade: (1) blade; (2) matrix; (3) paste; (4) extrudate.</p>
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<p>Scheme of influences of extrusion parameters.</p>
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<p>Laboratory radial extruder. Main parameters of the extruder: (1) matrix; (2) base plate; (3) bearing; (4) frame; (5) arm; (6) force sensor; (7) blade; (8) rotor with shaft; (9) lid; (10) paste; and (11) pressure sensor.</p>
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<p>The main experimental steps and the definition of control volumes and pressure profile under the blade as a function of the blade position: (<b>a</b>) the extruder chamber filled with colored layers of paste before the experiment; (<b>b</b>) colored streams of the paste in the wedge after the experiment; (<b>c</b>) the wedge of paste from the chamber before cutting; (<b>d</b>) extrudate behind the matrix; (<b>e</b>) definition of control volumes.</p>
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<p>The pressure profiles in the wedge during extrusion: (<b>a</b>) before the conversion as the graphical record of the sensor; (<b>b</b>) after the time interval <math display="inline"><semantics> <mrow> <mo>∆</mo> <mi>t</mi> </mrow> </semantics></math> conversion to the projection length of the blade <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>L</mi> </mrow> <mrow> <mi>M</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>.</p>
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<p>The process of the paste extrusion. The distribution of the extrusion pressure under the blade and the diagram of the principle of extrudate formation depending on the position of the blade, the weight of the extrudate <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>m</mi> </mrow> <mrow> <mi>e</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math> and the mass flow <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>m</mi> </mrow> <mrow> <mi>t</mi> <mi>e</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>.</p>
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<p>Comparing the liquid distribution: (<b>a</b>) in the wedge gap between the blade and the matrix; (<b>b</b>) in the extrudate; (<b>c</b>) interval of scattering of the average values of the moisture in the wedge for all speeds of the rotor; (<b>d</b>) interval of scattering of the average values of the moisture in the extrudate for all speeds of the rotor.</p>
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<p>Balance of extruded paste in the control volumes outside the matrix: (<b>a</b>) weight in individual control volumes <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>V</mi> </mrow> <mrow> <mi>e</mi> <mi>x</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>; (<b>b</b>) weight of paste extruded through the die holes in control volumes <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>V</mi> </mrow> <mrow> <mi>e</mi> <mi>x</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math> per unit time.</p>
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<p>Balance of extruded paste in the control volumes outside the matrix: (<b>a</b>) weight in individual control volumes <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>V</mi> </mrow> <mrow> <mi>e</mi> <mi>x</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>; (<b>b</b>) weight of paste extruded through the die holes in control volumes <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>V</mi> </mrow> <mrow> <mi>e</mi> <mi>x</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math> per unit time.</p>
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<p>Influence of the extrusion pressure <math display="inline"><semantics> <mrow> <mi>P</mi> </mrow> </semantics></math>, blade geometry and rotor speed <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>n</mi> </mrow> <mrow> <mi>R</mi> </mrow> </msub> </mrow> </semantics></math>: (<b>a</b>) on the distribution of the liquid before the matrix <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>w</mi> </mrow> <mrow> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>, in the extrudate <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>w</mi> <mi>e</mi> </mrow> <mrow> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>; (<b>b</b>) on the mass flow of the extrudate through the openings in the matrix <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>m</mi> </mrow> <mrow> <mi>t</mi> <mi>e</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math>.</p>
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<p>Influence of the mass flow of the extrudate through the holes in the matrix <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>m</mi> </mrow> <mrow> <mi>t</mi> <mi>e</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math> on the torque <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>M</mi> </mrow> <mrow> <mi>k</mi> <mi>i</mi> </mrow> </msub> </mrow> </semantics></math> required to drive the rotor with the blade.</p>
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31 pages, 52072 KiB  
Article
Development of Tetramycin-Loaded Core–Shell Beads with Hot-/Wet-Responsive Release Properties for Control of Bacterial Wilt Disease
by Juntao Gao, Guan Lin, Xinmin Deng, Junxian Zou, Yong Liu, Xingjiang Chen and Shiwang Liu
Agronomy 2024, 14(6), 1199; https://doi.org/10.3390/agronomy14061199 - 1 Jun 2024
Cited by 2 | Viewed by 1008
Abstract
Plant bacterial wilt is caused by Ralstonia solanacearum, a soilborne pathogen that infects plant conduits, leading to wilt disease. It is extremely difficult to cure plants infected with Ralstonia solanacearum; however, bactericide-loaded beads with hot-/wet-responsive properties may be able to release [...] Read more.
Plant bacterial wilt is caused by Ralstonia solanacearum, a soilborne pathogen that infects plant conduits, leading to wilt disease. It is extremely difficult to cure plants infected with Ralstonia solanacearum; however, bactericide-loaded beads with hot-/wet-responsive properties may be able to release a biocide in line with the increase in the hot-/wet-associated activity of Ralstonia solanacearum, effectively killing the pathogenic cells and providing high levels of plant protection. A biopesticide, Tetramycin, was embedded in corn kernel powder (CKP)-based cores. An oil-phase mixture was sprayed onto the core surface to form a hot-/wet-responsive intermediate shell (IMS). Subsequently, a layer of ethyl cellulose (EC) and hydroxypropyl methyl cellulose (HPMC) was coated onto the IMS to create a single wet-responsive outer shell (OTS). The ratios of the components in the cores, including the corn kernel powder (CKP), xanthan gum (XG), and Tetramycin, were optimized, as well as those of the IMS, including pentaerythrityl tetrastearate (PETS), pentaerythrityl tetraoleate (PETO), polyethylene glycol stearate (PEG400MS), and polyethylene glycol monooleate (PEG400MO), and those of the outer shell (OTS), including ethyl cellulose (EC) and hydroxypropyl methyl cellulose (HPMC). A texture performance analysis, differential scanning calorimetry (DSC) analysis, thermogravimetric analysis (TGA), temperature and humidity response performance tests, scanning electron microscope (SEM) observations, and a field effectiveness test were conducted to characterize the Tetramycin-loaded beads. The results indicated that the optimal formula for the bead cores comprised a mass ratio of CKP/Tetramycin solution/XG = 13.5:23:2. The preferred mass ratio for IMS was PETS/PETO/PEG400MO = 10:30:10, and the formula for the applicable OTS consisted of a mass ratio of EC/HPMC = 5:1. In soil with a temperature of 30–35 °C and humidity of 30%, the release period of the Tetramycin-loaded beads, with a cumulative release rate of over 95%, could last up to 35 days. Furthermore, the Tetramycin-loaded beads exhibited a gradual and multi-cyclic release process under alternating hot/wet and dry/cold environments. The relative preventive efficacy of 54.74% on tobacco was revealed at a field-testing scale. A significant reduction in the abundance of Ralstonia solanacearum was also observed under treatment with the Tetramycin-loaded beads. The early fungal community structure exhibited higher consistency compared to the control. However, in the later stage, the diversity differences between the soil layers were restored. In conclusion, Tetramycin-loaded beads that could effectively respond to temperature and humidity fluctuations were developed, resulting in enhanced disease prevention efficacy and offering broad prospects for the prevention and control of Ralstonia solanacearum in agricultural settings. Full article
(This article belongs to the Section Pest and Disease Management)
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<p>The simulation of field soil conditions to test the release properties of the Tetramycin-loaded beads. (<b>a</b>) The simulated field soil conditions involved cycling between hot/wet soil (35 °C, 30%) for 12 h and cold/dry soil (20 °C, 10%) for 3 days. (<b>b</b>) The simulated field soil conditions involved cycling between hot/wet soil (35 °C, 30%) for 12 h and hot/dry soil (35 °C, 10%) for 3 days. (<b>c</b>) The simulated field soil conditions involved cycling between hot/wet soil (35 °C, 30%) for 12 h and cold/wet soil (20 °C, 35%) for 3 days. (<b>d</b>) The Tetramycin-loaded beads were placed in air at 20 °C. (<b>e</b>) The Tetramycin-loaded beads were placed in air at 35 °C.</p>
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<p>The one-minute yield and integrity of different formulations of Tetramycin cores. (<b>A1</b>–<b>A5</b>) refer to beads prepared based on formulations (<b>A1</b>–<b>A5</b>), respectively, in <a href="#agronomy-14-01199-t001" class="html-table">Table 1</a>.</p>
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<p>The DSC analysis of IMSs with different ratios of fat materials. PETS, PETO, PEG400MS, and PEG400MO represent the pure components of PETS, PETO, PEG400MS, and PEG400MO, respectively, while samples M1-1 to M2-6 represent different ratios in the IMS. (<b>a</b>): test group of PEG400MS, (<b>b</b>) test group of PEG400MO.</p>
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<p>The TGA analysis of IMSs with different ratios of fat materials. (PETS, PETO, PEG400MS, and PEG400MO represent the pure components of PETS, PETO, PEG400MS, and PEG400MO, and samples MI-1~M2-6 represent different ratios of fat shells.).</p>
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<p>The conditions after soaking M1-4 (<b>a</b>) and M2-1 (<b>b</b>) at different temperatures (20, 25, 30, 35 °C) for 15 days.</p>
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<p>The appearance of beads M1-4 (<b>a</b>) and M2-1 (<b>b</b>) after soaking in water.</p>
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<p>M2-1~M2-6 IMS materials with Beet Red pigment added and soaked in water for 48 h at 35 °C.</p>
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<p>The morphologies of the outer EC/HPMC shells with different ratios (EH1–EH5 arranged from left to right) after 30 days at 35 °C without immersion (<b>a</b>) and after immersion (<b>b</b>).</p>
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<p>The effect of the amount of HPMC added on the hardness, resilience, springiness, and cohesiveness of the EC/HPMC OTS. (<b>a</b>–<b>d</b>) represent the differences in hardness, springiness, cohesiveness, and resilience of different OTS formulations, respectively (The points in the graph are the mean values; error bars represent standard deviations).</p>
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<p>The standard curve of the mass concentrations for Tetramycin A.</p>
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<p>The scanning electron microscope images of the OTS before soaking (<b>a</b>) and after soaking (<b>b</b>). The OTS exhibits the dissolution of the HPMC after immersion in water, allowing pores to appear in the shell layer, at which point the agricultural antibiotic’s release is accelerated.</p>
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<p>The scanning electron microscopy images of the temperature-sensitive material carriers at various temperature and humidity levels: (<b>a</b>) 20 °C without water immersion; (<b>b</b>) 20 °C with water immersion; (<b>c</b>) 35 °C without water immersion; (<b>d</b>) 35 °C with water immersion). The IMS will cause some degree of damage to the shell layer when it encounters either high temperatures or high humidity, and the damage is most severe when both high temperature and high humidity (35 °C 30%) are present, during which the drug is released at the fastest rate.</p>
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<p>A sectional view of the finished Tetramycin controlled-release tablet (<b>a</b>), a structural schematic (<b>b</b>), and an SEM image of the cross-section of a bead at 35× magnification (<b>c</b>). Shell 1 is the IMS; shell 2 is the OTS.</p>
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<p>The release curves of pellets from tablets under different temperature and humidity conditions (<b>a</b>) and the open storage release curves of pellets at room temperature (<b>b</b>). The points in the graph are the mean values; the error bars represent the standard deviations.</p>
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<p>The release curves of the Tetramycin-loaded beads under simulated field soil conditions. (a) The release performance of the Tetramycin-loaded beads under soil conditions simulating the cycle of hot/wet conditions (35 °C, 30%) for 12 h and cold/dry conditions (20 °C, 10%) for 3 days. (b) The release performance of the Tetramycin-loaded beads under soil conditions simulating the cycle of hot/wet conditions (35 °C, 30%) for 12 h and hot/dry conditions (35 °C, 10%) for 3 days. (c) The release performance of the Tetramycin-loaded beads under soil conditions simulating the cycle of hot/wet conditions (35 °C, 30%) for 12 h and cold/wet conditions (20 °C, 35%) for 3 days. (d) The release performance of the Tetramycin-loaded beads in air at 20 °C. (e) The release performance of the Tetramycin-loaded beads in air at 35 °C. The points in the graph are the mean values; the error bars represent the standard deviations.</p>
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<p>The disease index (<b>a</b>) and control efficacy (<b>b</b>) for tobacco bacterial wilt in the untreated control and experimental group. Data are expressed as the mean ± standard deviation, based on three parallel experiments. Letters “a” and “b” indicate significant differences at the level of <span class="html-italic">p</span> &lt; 0.05.</p>
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<p>The wilting of tobacco plants in the untreated control (<b>a</b>) and experimental groups (<b>b</b>), 15 weeks post-transplantation, during the field experiment in 2022.</p>
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<p>The wilting of tobacco plants in the untreated control (<b>a</b>,<b>c</b>,<b>e</b>) and experimental groups (<b>b</b>,<b>d</b>,<b>f</b>), 15 weeks post-transplantation, during the field experiment in 2023.</p>
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<p>The genus-level (<b>a</b>) and species-level (<b>b</b>) distribution frequency of soil bacteria. CK represents the untreated control; Tmn represents the group with Tetramycin pellets; 1, 2, and 3 refer to plants analyzed 10, 13, and 15 weeks after transplantation, respectively; and 10, 20, and 30 refer to the depth of the surface in the soil samples.</p>
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<p>The genus-level (<b>a</b>) and species-level (<b>b</b>) distribution frequency of soil fungi. CK represents the untreated control; Tmn represents the group with Tetramycin pellets; 1, 2, and 3 refer to plants analyzed 10, 13, and 15 weeks after transplantation, respectively; and 10, 20, and 30 refer to the depth of the surface in the soil samples.</p>
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<p>The bacterial (<b>a</b>) and fungal (<b>b</b>) dilution curves. CK represents the untreated control; Tmn represents the group with Tetramycin pellets; 1, 2, and 3 refer to plants analyzed 10, 13, and 15 weeks after transplantation, respectively; and 10, 20, and 30 refer to the depth of the surface in the soil samples.</p>
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<p>The bacterial (<b>a</b>) and fungal (<b>b</b>) OTU flower plot. CK represents the untreated control; Tmn represents the group with Tetramycin pellets; 1, 2, and 3 refer to plants analyzed 10, 13, and 15 weeks after transplantation, respectively; and 10, 20, and 30 refer to the depth of the surface in the soil samples.</p>
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<p>The principal coordinate analysis (PCoA) plot for the analysis of differences in the microbial community structure among various bacterial (<b>a</b>) and fungal (<b>b</b>) samples. CK represents the untreated control; Tmn represents the group with Tetramycin pellets; 1, 2, and 3 refer to plants analyzed 10, 13, and 15 weeks after transplantation, respectively; and 10, 20, and 30 refer to the depth of the surface in the soil samples.</p>
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15 pages, 5730 KiB  
Article
Using Chia Powder as a Binder to Obtain Chewable Tablets Containing Quinoa for Dietary Fiber Supplementation
by Rosana Pereira da Silva, Fanny Judhit Vereau Reyes, Josiane Souza Pereira Daniel, Julia Estevam da Silva Pestana, Samara de Almeida Pires and Humberto Gomes Ferraz
Powders 2024, 3(2), 202-216; https://doi.org/10.3390/powders3020013 - 7 Apr 2024
Viewed by 1356
Abstract
The consumption of fiber in the human diet is a global recommendation to ensure a healthy diet. Quinoa (Chenopodium quinoa Willd.), a gluten-free grain, and chia (Salvia hispanica), a seed, contain a high fiber content, and both have the [...] Read more.
The consumption of fiber in the human diet is a global recommendation to ensure a healthy diet. Quinoa (Chenopodium quinoa Willd.), a gluten-free grain, and chia (Salvia hispanica), a seed, contain a high fiber content, and both have the potential to be used in the development of nutraceutical and pharmaceutical formulations. An interesting characteristic of chia is its ability to form viscous mucilage when in contact with water, making it a potential binder in solid formulations. However, there are no studies on chia as a binder, and therefore, the objective of the present study was to evaluate the feasibility of using chia as a binder to produce quinoa granules and, subsequently, develop chewable tablet formulations. The quinoa and chia were in a powder form and then transformed into a wet mass with the help of mixer torque rheometer (MTR) equipment. In the wet granulation form, the following parameters were tested: multiple additions, 15 g of material, and 25 timepoints for the addition of 1 mL of water. An experimental design was carried out to evaluate the impact of the variables on the MTR results for subsequent granulation. The granulation point was possible for T1–T9, and most formulations gave satisfactory results, such as an acceptable resistance of the granules. In the end, a formulation was selected for the development of chewable tablets containing quinoa and chia fibers. Full article
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<p>Histogram of the particle size distribution of the quinoa and chia powder samples.</p>
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<p>T1–T9 and calculated mean (duplicate) of multiple additions for different proportions of quinoa, MCC PH101 (diluent), and chia (binder).</p>
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<p>Pareto graphs for the analysis of variance of torque and water ratio parameters.</p>
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<p>Response surface graphs indicating the effects on torque (Nm) from diluent and quinoa (<b>A</b>), binder and diluent (<b>B</b>), binder and quinoa (<b>C</b>), and diluent and binder (<b>D</b>). Likewise, the response surface graphs indicate the effect on water demand (mL) from diluent and quinoa (<b>E</b>), binder and diluent (<b>F</b>), quinoa and binder (<b>G</b>), and binder and diluent (<b>H</b>).</p>
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<p>Physical characterization results to evaluate the granule flow for T1–T9: (<b>A</b>) Hausner ratio; (<b>B</b>) Carr Index; and (<b>C</b>) true density. The red line in (<b>A</b>,<b>B</b>) represents the specifications of the American Pharmacopoeia [<a href="#B33-powders-03-00013" class="html-bibr">33</a>].</p>
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<p>Resistance of the T1–T9 granules on the sieves before and after the friability testing of the formulations.</p>
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<p>The average size of the granules using optical microscopy with 30 and 40× magnification. The sizes of the captured images (in width and height) vary from 1500 to 2500 µm.</p>
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27 pages, 4839 KiB  
Article
Investigating the Effects of Mixing Dynamics on Twin-Screw Granule Quality Attributes via the Development of a Physics-Based Process Map
by Lalith Kotamarthy, Subhodh Karkala, Ashley Dan, Andrés D. Román-Ospino and Rohit Ramachandran
Pharmaceutics 2024, 16(4), 456; https://doi.org/10.3390/pharmaceutics16040456 - 25 Mar 2024
Viewed by 1579
Abstract
Twin-screw granulation (TSG) is an emerging continuous wet granulation technique that has not been widely applied in the industry due to a poor mechanistic understanding of the process. This study focuses on improving this mechanistic understanding by analyzing the effects of the mixing [...] Read more.
Twin-screw granulation (TSG) is an emerging continuous wet granulation technique that has not been widely applied in the industry due to a poor mechanistic understanding of the process. This study focuses on improving this mechanistic understanding by analyzing the effects of the mixing dynamics on the granule quality attributes (PSD, content uniformity, and microstructure). Mixing is an important dynamic process that simultaneously occurs along with the granulation rate mechanisms during the wet granulation process. An improved mechanistic understanding was achieved by identifying and quantifying the physically relevant intermediate parameters that affect the mixing dynamics in TSG, and then their effects on the granule attributes were analyzed by investigating their effects on the granulation rate mechanisms. The fill level, granule liquid saturation, extent of nucleation, and powder wettability were found to be the key physically relevant intermediate parameters that affect the mixing inside the twin-screw granulator. An improved geometrical model for the fill level was developed and validated against existing experimental data. Finally, a process map was developed to depict the effects of mixing on the temporal and spatial evolution of the materials inside the twin-screw granulator. This process map illustrates the mechanism of nucleation and the growth of the granules based on the fundamental material properties of the primary powders (solubility and wettability), liquid binders (viscosity), and mixing dynamics present in the system. Furthermore, it was shown that the process map can be used to predict the granule product quality based on the granule growth mechanism. Full article
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<p>Fill level estimated vs. fill level reported in earlier studies. Orange dotted line (<span style="color:#FE9A2E">......</span>) represents the x = y line, green dots (<span style="color:#74DF00"><sup>◆</sup></span>) represent the estimated fill level values, and black dotted lines (<b>- -</b>) represent the 5% error margins.</p>
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<p>(<b>a</b>) Effect of screw speed on RTD, (<b>b</b>) effect of screw speed on PSD, and (<b>c</b>) effect of screw speed on content uniformity.</p>
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<p>Effect of screw speed on the granule microstructure: (<b>a</b>) 300 rpm, (<b>b</b>) 500 rpm, and (<b>c</b>) 700 rpm.</p>
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<p>Microstructure investigation of the granule obtained at a screw speed of 300 rpm.</p>
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<p>Effect of the number of kneading elements on the (<b>a</b>) residence time distribution, (<b>b</b>) particle size distribution, and (<b>c</b>) content uniformity.</p>
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<p>Effects of kneading elements on the granule microstructure: (<b>a</b>) 0 kneading elements/all conveying elements, (<b>b</b>) 2 kneading elements, (<b>c</b>) 4 kneading elements, (<b>d</b>) 6 kneading elements, and (<b>e</b>) 8 kneading elements.</p>
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<p>Positions of the kneading zone relative to the liquid addition zone used in this study.</p>
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<p>Effect of the kneading zone position on the (<b>a</b>) residence time distribution, (<b>b</b>) particle size distribution, and (<b>c</b>) content uniformity.</p>
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<p>Effect of the kneading zone position on the granule microstructure in (<b>a</b>) zone 4, (<b>b</b>) zone 5, (<b>c</b>) zone 6.</p>
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<p>Different stages of liquid saturation in a granule [<a href="#B60-pharmaceutics-16-00456" class="html-bibr">60</a>].</p>
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<p>Mechanistic process map depicting the effects of input parameters on granule quality attributes through mixing and granulation growth mechanisms (red circles represent API particles, black circles represent excipient particles ad blue line over particle clusters represents surface water layer).</p>
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25 pages, 4924 KiB  
Article
Bioethanol Production from A-Starch Milk and B-Starch Milk as Intermediates of Industrial Wet-Milling Wheat Processing
by Aleksandra Katanski, Vesna Vučurović, Damjan Vučurović, Bojana Bajić, Žana Šaranović, Zita Šereš and Siniša Dodić
Fermentation 2024, 10(3), 144; https://doi.org/10.3390/fermentation10030144 - 2 Mar 2024
Viewed by 2576
Abstract
The present work highlights the advances of integrated starch and bioethanol production as an attractive industrial solution for complex wheat exploitation to value-added products focusing on increased profitability. Bioethanol is conventionally produced by dry-milling wheat grain and fermenting sugars obtained by the hydrolysis [...] Read more.
The present work highlights the advances of integrated starch and bioethanol production as an attractive industrial solution for complex wheat exploitation to value-added products focusing on increased profitability. Bioethanol is conventionally produced by dry-milling wheat grain and fermenting sugars obtained by the hydrolysis of starch, while unused nonfermentable kernel compounds remain in stillage as effluents. On the other hand, the wet-milling of wheat flour enables complex wheat processing for the simultaneous production of starch, gluten, and fiber. The intermediates of industrial wheat starch production are A-starch milk, containing mainly large starch granules (diameter > 10 μm), and B-starch milk, containing mainly small starch granules (diameter < 10 μm). The present study investigates different starch hydrolysis procedures using commercial amylase for bioethanol production from A-starch and B-starch milk by batch fermentation using distillers’ yeast Saccharomyces cerevisiae Thermosacc®. Cold hydrolysis with simultaneous liquefaction and saccharification at 65 °C, a pH of 4.5, and a duration of 60 min was the most efficient and energy-saving pretreatment reaching a high conversion rate of starch to ethanol of 93% for both of the investigated substrates. A process design and cost model of bioethanol production from A-starch and B-starch milk was developed using the SuperPro Designer® v.11 (Intelligen Inc., Scotch Plains, NJ, USA) software. Full article
(This article belongs to the Special Issue Biofuels Production and Processing Technology, 3rd Edition)
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<p>The co-production of starch and bioethanol by wet-milling wheat processing.</p>
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<p>Process flow diagram of industrial starch and gluten production by wet-milling wheat flour.</p>
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<p>Applied procedures of wheat starch hydrolysis for bioethanol production.</p>
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<p>Scanning electron micrographs (SEM) images (×1000) of A-starch milk (<b>a</b>) and B-starch milk (<b>b</b>).</p>
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<p>Time profiles of CO<sub>2</sub> production for A-starch milk (<b>a</b>) and B-starch milk (<b>b</b>).</p>
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<p>Average hourly CO<sub>2</sub> production rate (<span class="html-italic">d</span>CO<sub>2</sub>/<span class="html-italic">dt</span>) during the fermentation of A-starch milk (<b>a</b>) and B-starch milk (<b>b</b>).</p>
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<p>Ethanol content (<span class="html-italic">E</span>), ethanol yield per substrate (<span class="html-italic">P</span>), ethanol yield per dry mass of substrate (<span class="html-italic">P<sub>dm</sub></span>), and ethanol yield per starch (<span class="html-italic">P<sub>S</sub></span>) obtained for A-starch milk (<b>a</b>) and B-starch milk (<b>b</b>).</p>
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<p>Utilization of the substrate (<span class="html-italic">U</span>), utilization of the dry matter of the substrate (<span class="html-italic">U<sub>dm</sub></span>), and utilization of the starch (<span class="html-italic">U<sub>s</sub></span>) for ethanol production obtained for A-starch milk (<b>a</b>) and B-starch milk (<b>b</b>).</p>
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<p>Simplified process flow diagram of the upstream process variations in ethanol production from wheat starch milk.</p>
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<p>Economic indices as a function of different pretreatment procedures of wheat starch milk for ethanol production: total capital investment, operating cost, unit production cost, and payback time. Black bar: A-starch milk; gray bar: B-starch milk.</p>
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<p>Raw materials’ cost breakdown for ethanol production from wheat starch milk: black bar, P1; and gray bar, P2–5.</p>
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<p>Bioethanol plant payback time as a function of its starch milk utilization capacity: black circle, A-starch milk; and black rectangle, B-starch milk.</p>
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