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Search Results (17,982)

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12 pages, 3098 KiB  
Article
Effect of Potassium on the Co-Combustion Process of Coal Slime and Corn Stover
by Jing Zheng, Chuanchuan Cai, Tao Ge and Mingxu Zhang
Energies 2024, 17(20), 5185; https://doi.org/10.3390/en17205185 (registering DOI) - 18 Oct 2024
Abstract
In this study, the combined combustion characteristics and gaseous product emissions of coal slime and corn stover were compared at different blending ratios. The TG-DTG curves indicate that the optimal performance is achieved when the corn straw blending ratio is 20%. Furthermore, the [...] Read more.
In this study, the combined combustion characteristics and gaseous product emissions of coal slime and corn stover were compared at different blending ratios. The TG-DTG curves indicate that the optimal performance is achieved when the corn straw blending ratio is 20%. Furthermore, the TG-FTIR coupling results demonstrated an increase in gas species as the blending ratio increased. The composition analysis of ash samples formed at various combustion temperatures using XRD and XRF indicated that a portion of KCl in the fuel was released as volatile matter, while another part reacted with Al2O3 and SiO2 components in the slime to form silica–aluminate compounds and other substances. Notably, interactions between the components of slime and potassium elements in corn stover primarily occurred within the temperature range of 800–1000 °C. These findings contribute to a comprehensive understanding of biomass and coal co-firing combustion chemistry, offering potential applications for enhancing energy efficiency and reducing emissions in industrial processes. Full article
(This article belongs to the Section I2: Energy and Combustion Science)
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Figure 1

Figure 1
<p>Thermogravimetric profile of slime and corn stover combustion alone: (<b>a</b>) slime and (<b>b</b>) corn stover.</p>
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<p>Thermogravimetric profile of mixed combustion of slime and corn stover: (<b>a</b>) TG curve and (<b>b</b>) DTG curve.</p>
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<p>TG-FTIR profiles of gases released during combustion at different blending ratios: (<b>a</b>) blend ratio 20%, (<b>b</b>) blend ratio 40%, and (<b>c</b>) blend ratio 60%.</p>
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<p>XRF analysis pattern of gray sample: (<b>a</b>) corn stover, (<b>b</b>) coal slime, and (<b>c</b>) mixture of corn stover and coal slime.</p>
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<p>XRD patterns of ash samples after different combustion temperatures: (<b>a</b>) raw materials, (<b>b</b>) corn stover, (<b>c</b>) coal slime, and (<b>d</b>) mixture of corn stover and coal slime. A—Al<sub>4</sub>(OH)<sub>8</sub>(Si<sub>4</sub>O<sub>10</sub>); B—SiO<sub>2</sub>; C—MgFeSiAlOOH; D—Mg<sub>7</sub>Si<sub>8</sub>O<sub>22</sub>(OH)<sub>2</sub>; E—Pb<sub>4</sub>(S<sub>2</sub>O<sub>3</sub>)O<sub>2</sub>(OH)<sub>2</sub>; F—Al<sub>2</sub>Si<sub>2</sub>O<sub>5</sub>(OH)<sub>4</sub>; G—Al<sub>2</sub>Si<sub>2</sub>O<sub>5</sub>; H—KCl; I—SnO<sub>2</sub>; J—CaMgSi<sub>2</sub>O<sub>6</sub>; K—Al<sub>2</sub>O<sub>3</sub>; O—KAlSiO<sub>4</sub>; P—CaCO<sub>3</sub>; Q—KAl<sub>2</sub>(AlSi<sub>3</sub>O<sub>10</sub>)(OH)<sub>2</sub>; R—KAlSi<sub>3</sub>O<sub>8</sub>; S—TiO<sub>2</sub>; T—Pb<sub>2</sub>O(SO<sub>4</sub>); U—CaSiBO<sub>5</sub>H; V—K<sub>2</sub>Ca<sub>2</sub>Mg(SO<sub>4</sub>)<sub>4</sub>; W—Si<sub>3</sub>N<sub>4</sub>; X—Na(AlSi<sub>3</sub>O<sub>8</sub>); Y—Al<sub>2</sub>(SiO<sub>4</sub>)(OH)<sub>2</sub>; Z—KAl<sub>3</sub>(SiO<sub>4</sub>)(OH)<sub>6</sub>.</p>
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<p>Possible transformation pathways of elemental K during combustion of slime and corn stover.</p>
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17 pages, 1856 KiB  
Article
Experimental Evaluation of Blockage Resistance and Position Caused by Microparticle Migration in Water Injection Wells
by Jifei Yu, Huan Chen, Yanfeng Cao, Min Wen, Xiaopeng Zhai, Xiaotong Zhang, Tongchuan Hao, Jianlin Peng and Weitao Zhu
Processes 2024, 12(10), 2275; https://doi.org/10.3390/pr12102275 - 17 Oct 2024
Abstract
Offshore oil field loose sandstone reservoirs have high permeability. However, during the water injection process, water injection blockage occurs, causing an increase in injection pressure, making it impossible to continue injecting water on site. Current research mainly focuses on the factors causing water [...] Read more.
Offshore oil field loose sandstone reservoirs have high permeability. However, during the water injection process, water injection blockage occurs, causing an increase in injection pressure, making it impossible to continue injecting water on site. Current research mainly focuses on the factors causing water injection blockage, with less attention given to the blockage locations and the pressure increase caused by water injection. There is a lack of research on the change in the law of injection capacity. This paper establishes a simulation experiment for water injection blockage that can accommodate both homogeneous and heterogeneous cores. The experimental core is 1 m long and capable of simulating the blockage conditions in the near-well zone during water injection, thereby analyzing the core blockage position and blockage pressure. The study clarifies the influence of water quality indicators, heterogeneity, and core length on the blockage patterns in reservoirs during water injection. The research findings are as follows: I. The reservoir blockage samples were characterized using scanning electron microscopy (SEM), casting thin sections, and X-ray diffraction (XRD) analysis. The results indicate that the main factors causing blockage are clay, silt, and fine particulate suspensions, with the fine particles mainly consisting of hydrated silicates and alkali metal oxides. The primary cause of blockage in loose sandstone is identified as the mechanism of migration and accumulation of clay, fine rock particles, and suspended matter in the injected water. II. By monitoring pressure and permeability changes in the core flooding experiments, the impact of reservoir heterogeneity on water injection capacity was evaluated. The evaluation results show that the blockage locations and lengths in heterogeneous cores are twice those in homogeneous cores. III. For heterogeneous reservoirs, if the initial permeability at the inlet is lower than in other segments of the core, significant blockage resistance occurs, with the final resistance being 1.27 times that of homogeneous cores. If the initial permeability at the inlet is higher than in other parts, the final blockage resistance is close to that of homogeneous cores. This study provides theoretical support for the analysis of blockage locations and pressures in loose sandstone water injection and offers technical support for the design of unplugging ranges and pressures after blockage in heterogeneous formations. At the same time, it provides a theoretical basis for selecting the direction of acidizing after blockage occurs in loose sandstone. Full article
(This article belongs to the Section Energy Systems)
20 pages, 3495 KiB  
Article
Characterization of the Evolution with Temperature of the Structure and Properties of Geopolymer-Cordierite Composites
by Franklin Casarrubios, Alexandre Marlier, Charlotte Lang, Sandra Abdelouhab, Isabella Mastroianni, Geoffroy Bister and Maurice-François Gonon
Ceramics 2024, 7(4), 1513-1532; https://doi.org/10.3390/ceramics7040098 - 17 Oct 2024
Abstract
This work is part of a research project aimed at producing ceramic-like materials, without the need for an initial sintering, for potential applications in catalysis or filtration at temperatures up to 1000 °C. In that context, cordierite-derived materials were prepared from recycled cordierite [...] Read more.
This work is part of a research project aimed at producing ceramic-like materials, without the need for an initial sintering, for potential applications in catalysis or filtration at temperatures up to 1000 °C. In that context, cordierite-derived materials were prepared from recycled cordierite powder (automotive industry waste) bonded with metakaolin-potassium silicate geopolymer. The principle is that these materials, prepared at temperatures below 100 °C, acquire their final properties during the high-temperature commissioning. The focus is on the influence of the K/Al ratio and cordierite fraction on the stability of the dimensions and porosity during heating at 1000 °C, and on the final Young’s modulus and coefficient of thermal expansion. Conventional and high-temperature XRD evidenced the absence of crystallization of the geopolymer binder and interaction with the cordierite filler during the heating stage when K/Al = 1 or 0.75. By contrast, crystallization of kalsilite and leucite, and diffusion of potassium ions in the structure of cordierite is evidenced for K/Al = 1.5 and 2.3. These differences strongly influence the shrinkage due to sintering and the final properties. It is shown that a K/Al ratio of 0.75 or 1 is favorable to the stability of the porosity, around 25 to 30%. Moreover, a low coefficient of thermal expansion of 4 to 4.5 10−6 K−1 and a Young’s modulus of 40 to 45 GPa is obtained. Full article
(This article belongs to the Special Issue Innovative Manufacturing Processes of Silicate Materials)
19 pages, 10316 KiB  
Article
Properties of Sn-Doped PBZT Ferroelectric Ceramics Sintered by Hot-Pressing Method
by Dagmara Brzezińska, Dariusz Bochenek, Maciej Zubko, Przemysław Niemiec and Izabela Matuła
Materials 2024, 17(20), 5072; https://doi.org/10.3390/ma17205072 - 17 Oct 2024
Abstract
This work investigated the structure, microstructure, and ferroelectric and dielectric behavior of (Pb0.97Ba0.03)(Zr0.98Ti0.02)1−xSnxO3 (PBZT_xSn) solid solution with variable tin content in the range x = 0.00–0.08. Synthesis [...] Read more.
This work investigated the structure, microstructure, and ferroelectric and dielectric behavior of (Pb0.97Ba0.03)(Zr0.98Ti0.02)1−xSnxO3 (PBZT_xSn) solid solution with variable tin content in the range x = 0.00–0.08. Synthesis was carried out using the powder calcination method, and sintering was carried out using the hot-pressing method. For all the PBZT_xSn samples at room temperature, X-ray diffractograms confirmed the presence of an orthorhombic (OR) crystal structure with space group Pnnm, and the microstructure is characterized by densely packed and properly shaped grains with an average size of 1.36 µm to 1.73 µm. At room temperature, PBZT_xSn materials have low permittivity values ε′ ranging from 265 to 275, whereas, at the ferroelectric–paraelectric phase transition temperature (RE–C), the permittivity is high (from 8923 to 12,141). The increase in the tin dopant in PBZT_xSn lowers permittivity and dielectric loss and changes the scope of occurrence of phase transitions. The occurring dispersion of the dielectric constant and dielectric loss at low frequencies, related to the Maxwell–Wagner behavior, decreases with increasing tin content in the composition of PBZT_xSn. Temperature studies of the dielectric and ferroelectric properties revealed anomalies related to the phase transitions occurring in the PBZT_xSn material. With increasing temperature in PBZT_xSn, phase transitions occur from orthorhombic (OR) to rhombohedral (RE) and cubic (C). The cooling cycle shifts the temperatures of the phase transitions towards lower temperatures. The test results were confirmed by XRD Rietveld analysis at different temperatures. The beneficial dielectric and ferroelectric properties suggest that the PBZT_xSn materials are suitable for micromechatronic applications as pulse capacitors or actuator elements. Full article
(This article belongs to the Special Issue Mechanical and Thermal Properties Analysis of Ceramic Composites)
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Figure 1

Figure 1
<p>XRD patterns of the PBZT_<span class="html-italic">x</span>Sn ceramic powders at room temperature.</p>
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<p>Microstructures and statistical results of the grain size distribution of PBZT_<span class="html-italic">x</span>Sn ceramic samples obtained using HP technology: PBZT_0Sn (<b>a</b>,<b>f</b>), PBZT_2Sn (<b>b</b>,<b>g</b>), PBZT_4Sn (<b>c</b>,<b>h</b>), PBZT_6Sn (<b>d</b>,<b>i</b>), PBZT_8Sn (<b>e</b>,<b>j</b>); (<b>k</b>) EDS analysis image of the element distribution for the PBZT_<span class="html-italic">x</span>Sn ceramic samples.</p>
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<p>(<b>a</b>) <span class="html-italic">P</span>–<span class="html-italic">E</span> hysteresis loops for PBZT_<span class="html-italic">x</span>Sn ceramic samples at room temperature and <span class="html-italic">E</span> = 4 kV/mm, (<b>b</b>) temperature <span class="html-italic">P–E</span> loop for PBZT_6Sn sample, (<b>c</b>) temperature dependence of remnant polarization and (<b>d</b>) coercive field, and (<b>e</b>) temperature <span class="html-italic">P</span>–<span class="html-italic">E</span> loop for PBZT_6Sn sample with shift in results by a constant value along the OX axis.</p>
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<p>The variation in the dielectric permittivity as a function of frequency for PBZT_<span class="html-italic">x</span>Sn ceramic samples.</p>
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<p>Permittivity (<b>a</b>) and dielectric tangent loss (<b>b</b>) vs. temperature of PBZT_<span class="html-italic">x</span>Sn ceramics.</p>
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<p><span class="html-italic">ε</span>(<span class="html-italic">T</span>) graph for PBZT_<span class="html-italic">x</span>Sn material measured at 1 kHz in the heating cycle.</p>
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<p>Temperature studies of dielectric properties (<b>a</b>) <span class="html-italic">ε</span>(<span class="html-italic">T</span>) and (<b>b</b>) tan<span class="html-italic">δ</span>(<span class="html-italic">T</span>) for the PBZT_6Sn sample measured at 1 kHz in the heating and cooling cycles.</p>
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<p>Temperature-dependent XRD patterns of the PBZT_<span class="html-italic">x</span>Sn ceramics; (<b>a</b>) full measurement range for 2<span class="html-italic">θ</span> angles (14°–90°); (<b>b</b>) the reflection peaks around 2<span class="html-italic">θ</span> = 54°. The beginning of the heating cycle from 30 °C to 230 °C and then the cooling cycle to 60 °C.</p>
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<p>(<b>a</b>) The reflection positions of the Rietveld refinements for each XRD pattern of the PBZT_6Sn ceramics and (<b>b</b>) the evolution of the pseudo-cubic lattice parameters in the heating and cooling cycles.</p>
Full article ">
30 pages, 1637 KiB  
Article
Titanium Nanoparticles (TiO2-NPs) as Catalysts for Enhancing Drought Tolerance in Grapevine Saplings
by Selda Daler, Ozkan Kaya, Nesrin Korkmaz, Tuğba Kılıç, Ahmet Karadağ and Harlene Hatterman-Valenti
Horticulturae 2024, 10(10), 1103; https://doi.org/10.3390/horticulturae10101103 - 17 Oct 2024
Abstract
Drought is a major stress that hinders plant growth and causes water stress, posing a significant threat to global food security. While nanotechnology, particularly the use of nanoparticles such as TiO2, offers a promising solution by enhancing plants’ resilience to drought [...] Read more.
Drought is a major stress that hinders plant growth and causes water stress, posing a significant threat to global food security. While nanotechnology, particularly the use of nanoparticles such as TiO2, offers a promising solution by enhancing plants’ resilience to drought stress, improving nutrient absorption, and promoting growth under adverse conditions, its application in viticulture remains underexplored. The objective of this research was to investigate the effects of titanium dioxide nanoparticles (TiO2-NPs; 100, 10, 1, and 0 ppm (control)) on various physiological, biochemical, and morphological parameters in grapevine saplings. Three different rootstock varieties, 41 B/Crimson Seedless (CS), 1103 P/CS, and 5 BB/CS, were included in the experiment to assess how rootstock variety influences the response of grapevine saplings to TiO2-NPs under drought stress (40–50%) and well-irrigated (90–100%) conditions. Young vines grown in pots under greenhouse conditions were used in this study. Applications of 10 ppm TiO2-NPs improved growth parameters and the SPAD index and enhanced stomatal conductance, relative water content, and protein content in grapevine saplings under both drought and well-irrigated conditions. Conversely, oxidative stress parameters, including the membrane damage index, hydrogen peroxide, drought index, and lipid peroxidation levels, were significantly reduced following 10 ppm TiO2-NP applications under drought conditions. Furthermore, total phenolic content, proline content, and ascorbate peroxidase, catalase, and superoxide dismutase activities, which increased significantly with drought stress, were reduced to lower levels, paralleling the alleviation of drought-induced oxidative stress. Our results suggest that the primary role of TiO2 nanoparticles in enhancing drought tolerance is due to their beneficial effects in alleviating damage caused by drought stress. This finding applies not only to grapevines but may also be relevant for other agricultural crops. Full article
(This article belongs to the Special Issue Advances in Rootstocks for Grape Production)
23 pages, 7325 KiB  
Article
Dissolution of Volcanic Ash in Alkaline Environment for Cold Consolidation of Inorganic Binders
by Giovanni Dal Poggetto, Philippe Douwe, Antonio Stroscio, Elie Kamseu, Isabella Lancellotti, Antoine Elimbi and Cristina Leonelli
Materials 2024, 17(20), 5068; https://doi.org/10.3390/ma17205068 - 17 Oct 2024
Abstract
A systematic study on the dissolution in concentrated alkali of two volcanic ashes from Cameroon, denoted as DAR and VN, is presented here. One volcanic ash, DAR, was 2 wt% richer in Fe and Ca and 4 wt% lower in Si than the [...] Read more.
A systematic study on the dissolution in concentrated alkali of two volcanic ashes from Cameroon, denoted as DAR and VN, is presented here. One volcanic ash, DAR, was 2 wt% richer in Fe and Ca and 4 wt% lower in Si than the other, designated as VN. Such natural raw materials are complex mixtures of aluminosilicate minerals (kaersutite, plagioclase, magnetite, diopside, thenardite, forsterite, hematite, and goethite) with a good proportion of amorphous phase (52 and 74 wt% for DAR and VN, respectively), which is more reactive than the crystalline phase in alkaline environments. Dissolution in NaOH + sodium silicate solution is the first step in the geopolymerisation process, which, after hardening at room temperature, results in solid and resistant building blocks. According to XRD, the VN finer ash powders showed a higher reactivity of Al-bearing soluble amorphous phases, releasing Al cations in NaOH, as indicated by IPC-MS. In general, dissolution in a strong alkaline environment did not seem to be affected by the NaOH concentration, provided that it was kept higher than 8 M, or by the powder size, remaining below 75 µm, while it was affected by time. However, in the time range studied, 1–120 min, the maximum element release was reached at about 100 min, when an equilibrium was reached. The hardened alkali activated materials show a good reticulation, as indicated by the low weight loss in water (10 wt%) when a hardening temperature of 25 °C was assumed. The same advantage was found for of the room-temperature consolidated specimens’ mechanical performance in terms of resistance to compression (4–6 MPa). The study of the alkaline dissolution of volcanic ash is, therefore, an interesting way of predicting and optimising the reactivity of the phases of which it is composed, especially the amorphous ones. Full article
(This article belongs to the Special Issue Advances in Natural Building and Construction Materials)
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Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>Comparison of particle size distribution curves of pure DAR (orange) and pure VN (blue) volcanic ash powders.</p>
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<p>Chemical composition of the 3 different fractions of each volcanic ash: DAR (red colours) and VN (green colours). Numerical values are given in <a href="#materials-17-05068-t001" class="html-table">Table 1</a>.</p>
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<p>FT-IR spectra of DAR volcanic ash: as-ground (blue) and after immersion in NaOH 12 M for 2 h (red).</p>
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<p>FT-IR spectra of VN volcanic ash: as-ground (blue) and after immersion in NaOH 12 M for 2 h (red).</p>
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<p>Leaching of metals of volcanic ash powder, DAR, after 8, 10, and 12 M after 120 min. The grain size used for the test is 5–75 µm.</p>
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<p>Leaching of metals of volcanic ash powder, VN, after 8, 10, and 12 M after 120 min. The grain size used for the test is 5–75 µm.</p>
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<p>Leaching of metals of volcanic ash powders, DAR and VN, after immersion in NaOH 12 M as a function of time. The grain size used for the test is 5–75 µm.</p>
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<p>Al released from DAR volcanic ash at different grain size after NaOH 12 M over a period of 2 h.</p>
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<p>Al released from VN volcanic ash at different grain size after NaOH 12 M over a period of 2 h.</p>
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<p>Si released from DAR volcanic ash at different grain size after NaOH 12 M over a period of 2 h.</p>
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<p>Si released from VN volcanic ash at different grain size after NaOH 12 M over a period of 2 h.</p>
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<p>XRD patterns of DAR powders before and after immersion in NaOH at different molar ratios for 120 min. di = diopside (PDF: 19–0239); hem = hematite (PDF: 89–2810); An = Anorthite (PDF: 71–0748); Ka = Kaersutite (PDF: 44–1450); gibb = gibbsite (PDF: 96–101–1082); ght = goethite (PDF: 81–0462); Mg = Magnetite (PDF: 89–3854); Fo = Forsterite (PDF: 87–0619); Au = Augite (PDF: 71–1070); * = zincite (standard).</p>
Full article ">Figure 13
<p>XRD patterns of VN powders before and after immersion in NaOH at different molar ratios for 120 min. di = diopside (PDF: 19–0239); hem = hematite (PDF: 89–2810); An = Anorthite (PDF: 71–0748); Ka = Kaersutite (PDF: 44–1450); gibb = gibbsite (PDF: 96–101–1082); ght = goethite (PDF: 81–0462); Mg = Magnetite (PDF: 89–3854); Fo = Forsterite (PDF: 87–0619); Au = Augite (PDF: 71–1070); * = zincite (standard).</p>
Full article ">Figure 14
<p>Weight loss of GP-DAR and GP-VN geopolymers cured for 24 h at two different temperatures (25 °C and 45 °C).</p>
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<p>Ionic conductivity of geopolymer with DAR and VN made with different NaOH concentrations (8, 10, and 12 M), cured at 25 °C.</p>
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<p>ESEM backscattered images of freshly fractured samples: (<b>A</b>) GPDAR 12 T25 and (<b>B</b>) GPVN 12 T25.</p>
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<p>Comparison of mechanical properties of GPDAR samples made at different NaOH concentrations and different temperatures after 28 days of curing.</p>
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<p>Comparison of mechanical properties of GPVN samples made at different NaOH concentrations and different temperatures after 28 days of curing.</p>
Full article ">
18 pages, 3919 KiB  
Article
Sublingual Fast-Dissolving Thin Films of Loratadine: Characterization, In Vitro and Ex Vivo Evaluation
by Yahya Alhamhoom, Ashitha Kakarlapudi Said, Avichal Kumar, Shivakumar Hagalavadi Nanjappa, Divya Wali, Mohamed Rahamathulla, Syeda Ayesha Farhana, Mohammed Muqtader Ahmed and Thippeswamy Boreddy Shivanandappa
Polymers 2024, 16(20), 2919; https://doi.org/10.3390/polym16202919 - 17 Oct 2024
Abstract
Loratadine (LOR) is a second-generation antihistamine that exhibits a low and variable oral bioavailability (10–40%) and delayed onset owing to poor solubility and an extensive first-pass effect. Therefore, in light of the clinical need, the main goal of the present study was to [...] Read more.
Loratadine (LOR) is a second-generation antihistamine that exhibits a low and variable oral bioavailability (10–40%) and delayed onset owing to poor solubility and an extensive first-pass effect. Therefore, in light of the clinical need, the main goal of the present study was to develop sublingual fast-dissolving thin films of LOR–citric acid co-amorphous systems (LOR-CAs) with the aim of eliciting a faster onset and improving the bioavailability. We formulated sublingual fast-dissolving thin films of LOR by a film-casting technique using hydrophilic polymers like hydroxypropyl methylcellulose (HPMC E15), polyvinyl pyrrolidone K30 (PVP K30), and hydroxypropyl cellulose EL (HPC-EF) and citric acid as a pH modulator, while glycerin served as a plasticizer. The sublingual fast-dissolving thin films were characterized by FTIR, SEM, DSC, and XRD and evaluated for in vitro dissolution and ex vivo mucoadhesion. The best formulation (F1) developed using HPMC E15 as a polymer, glycerin as a plasticizer, and citric acid as a pH modulator was found to be the optimized formulation as it was smooth, clear, flexible, and displayed good mucoadhesion (11.27 ± 0.418 gm/cm2) and uniform thickness (0.25 ± 0.02 mm). The formulation F1 was found to display a significantly shorter DT (30.30 ± 0.6 s) and rapid release of LOR (92.10 ± 2.3% in 60 min) compared to other formulations (ANOVA, p < 0.001). The results indicated that the prepared sublingual films are likely to elicit a faster therapeutic effect, avoid first-pass metabolism, and improve the bioavailability. Full article
(This article belongs to the Special Issue Polymer Thin Films and Their Applications)
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Figure 1

Figure 1
<p>Bright field microscopy image of films composed of LOR (<b>A</b>) and LOR-CA (<b>B</b>) under a magnification of 100×. SEM analysis report of the F1-casted film (<b>C</b>) with a scale bar of 200 µm.</p>
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<p>Fourier transform infrared (FTIR) spectra of (<b>A</b>) F1, (<b>B</b>) physical mixture, (<b>C</b>) PVP K30, (<b>D</b>) HPC EF, (<b>E</b>) HPMC E15, and (<b>F</b>) LOR.</p>
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<p>Differential scanning calorimetric thermograms of (<b>A</b>) LOR, (<b>B</b>) HPMC E15, (<b>C</b>) physical mixture, and (<b>D</b>) F1.</p>
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<p>X-ray diffractograms of (<b>A</b>) F1, (<b>B</b>) physical mixture, (<b>C</b>) HPMC E15, and (<b>D</b>) LOR.</p>
Full article ">Figure 5
<p>Percent cumulative release profiles of fast-dissolving films of LOR in simulated saliva (6.8 pH). The release at 60 min was significantly higher (ANOVA, <span class="html-italic">p</span> &lt; 0.001) for F1 compared to the other formulations.</p>
Full article ">Figure 6
<p>Grouped column representation of stability analysis of optimized film (F1) from the initial day up to the third month. (<b>A</b>) surface pH, moisture content, (<b>B</b>) thickness, weight, and (<b>C</b>) folding endurance (FE), disintegration time (DT), drug content (DC), and drug release (DR).</p>
Full article ">
20 pages, 10780 KiB  
Article
Regulation of Reactivity of Calcined Ultrafine Kaolin Products
by Hui Yin, Huajie Liu, Yuhuan Bu, Weiqing Chen, Fuquan Ding, Wenxiang Lin and Yuwei Zhang
Processes 2024, 12(10), 2268; https://doi.org/10.3390/pr12102268 - 17 Oct 2024
Abstract
This study explored the potential of ultrafine kaolin as a geopolymer raw material, focusing on the reactivity of calcined kaolin products and its influencing factors. Through a series of analytical techniques, including thickening experiments, particle size analysis, SEM, XRD, and FT-IR, the effects [...] Read more.
This study explored the potential of ultrafine kaolin as a geopolymer raw material, focusing on the reactivity of calcined kaolin products and its influencing factors. Through a series of analytical techniques, including thickening experiments, particle size analysis, SEM, XRD, and FT-IR, the effects of calcination temperature, time, and Si-Al ratio were evaluated. The results indicated that calcination temperature significantly impacts reactivity, with optimal conditions found between 600 °C and 800 °C, yielding metakaolin with thickening times of 12 to 43 min. Temperatures above 900 °C led to the formation of low-reactivity phases like mullite. The Si-Al ratio also influenced thickening time, with durations varying from 97 min at 0.85 to 43 min at 0.9 and increasing to 157 min at 0.95. Calcination time had the smallest effect, with thickening times ranging from 10 to 25 min over 4 to 8 h. Additionally, calcination altered particle size, initially expanding due to thermal expansion and later shrinking due to lattice distortion above 700 °C. By adjusting these parameters, the reactivity of calcined kaolin could be tailored to suit specific needs. This research provides a theoretical foundation for metakaolin’s application in construction materials and offers novel insights into geopolymer preparation. Full article
(This article belongs to the Section Chemical Processes and Systems)
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<p>TG-DSC diagram of kaolin.</p>
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<p>Particle size distribution of kaolin products with different calcination temperatures (calcined for 4 h).</p>
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<p>Effect of calcination temperature on particle size index of calcined products.</p>
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<p>Infrared spectra of calcined products. a: Si-O bending vibration. b: Si-Al stretching vibration. c: Si-Si stretching vibration. d: Si-O stretching vibration. e: Al-O-H bending vibration. f: Si-O stretching vibration. g: OH vibration at the wafer bonding surface. h: O-H bond absorption peak. i: tetra-coordinated Al-O vibration.</p>
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<p>XRD images of the products at different calcination temperatures.</p>
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<p>SEM images of kaolin and calcined products at different temperatures.</p>
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<p>Thickening curves of calcined kaolin products at different calcination temperatures.</p>
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<p>Particle size distribution of calcined kaolin products with different calcination times (calcined at 600 °C).</p>
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<p>Effect of calcination time on particle size index of calcined products.</p>
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<p>Infrared spectra of calcined products. a: Si-O bending vibration. b: Si-Al stretching vibration. c: Si-Si stretching vibration. d: Si-O stretching vibration. e: Al-O-H bending vibration. f: Si-O stretching vibration. g: OH vibration at the wafer bonding surface. h: O-H bonding absorption peaks.</p>
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<p>XRD images of calcined products.</p>
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<p>SEM images of calcined products obtained from kaolin with different calcination times.</p>
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<p>SEM images of calcined products obtained from kaolin with different calcination times.</p>
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<p>Thickening curves of calcined kaolin products at different calcination times.</p>
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<p>Thickening curves of metakaolin systems with different Si-Al ratios.</p>
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20 pages, 24444 KiB  
Article
Preparation and Photocatalytic Performance of In2O3/Bi2WO6 Type II Heterojunction Composite Materials
by Xiuping Zhang, Fengqiu Qin, Yuanyuan Zhong, Tian Xiao, Qiang Yu, Xiaodong Zhu, Wei Feng and Zhiyong Qi
Molecules 2024, 29(20), 4911; https://doi.org/10.3390/molecules29204911 - 17 Oct 2024
Abstract
Bismuth-based photocatalytic materials have been widely used in the field of photocatalysis in recent years due to their unique layered structure. However, single bismuth-based photocatalytic materials are greatly limited in their photocatalytic performance due to their poor response to visible light and easy [...] Read more.
Bismuth-based photocatalytic materials have been widely used in the field of photocatalysis in recent years due to their unique layered structure. However, single bismuth-based photocatalytic materials are greatly limited in their photocatalytic performance due to their poor response to visible light and easy recombination of photogenerated charges. At present, constructing semiconductor heterojunctions is an effective modification method that improves quantum efficiency by promoting the separation of photogenerated electrons and holes. In this study, the successful preparation of an In2O3/Bi2WO6 (In2O3/BWO) II-type semiconductor heterojunction composite material was achieved. XRD characterization was performed to conduct a phase analysis of the samples, SEM and TEM characterization for a morphology analysis of the samples, and DRS and XPS testing for optical property and elemental valence state analyses of the samples. In the II-type semiconductor junction system, photogenerated electrons (e) on the In2O3 conduction band (CB) migrate to the BWO CB, while holes (h+) on the BWO valence band (VB) transfer to the In2O3 VB, promoting the separation of photoinduced charges, raising the quantum efficiency. When the molar ratio of In2O3/BWO is 2:6, the photocatalytic degradation degree of rhodamine B (RhB) is 59.4% (44.0% for BWO) after 60 min illumination, showing the best photocatalytic activity. After four cycles, the degradation degree of the sample was 54.3%, which is 91.4% of that of the first photocatalytic degradation experiment, indicating that the sample has good reusability. The XRD results of 2:6 In2O3/BWO before and after the cyclic experiments show that the positions and intensities of its diffraction peaks did not change significantly, indicating excellent structural stability. The active species experiment results imply that h+ is the primary species. Additionally, this study proposes a mechanism for the separation, migration, and photocatalysis of photoinduced charges in II-type semiconductor junctions. Full article
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<p>XRD patterns of samples.</p>
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<p>SEM images of samples, with different magnifications: BWO (<b>a</b>,<b>b</b>), In<sub>2</sub>O<sub>3</sub> (<b>c</b>,<b>d</b>), 1:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>e</b>,<b>f</b>), 2:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>g</b>,<b>h</b>), 3:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>i</b>,<b>j</b>), and 4:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>k</b>,<b>l</b>).</p>
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<p>SEM images of samples, with different magnifications: BWO (<b>a</b>,<b>b</b>), In<sub>2</sub>O<sub>3</sub> (<b>c</b>,<b>d</b>), 1:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>e</b>,<b>f</b>), 2:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>g</b>,<b>h</b>), 3:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>i</b>,<b>j</b>), and 4:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>k</b>,<b>l</b>).</p>
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<p>(<b>a</b>) SEM image of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO; (<b>b</b>–<b>e</b>) element mappings of Bi, O, W, In; (<b>f</b>) EDS analysis of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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<p>TEM and HRTEM images of samples: BWO (<b>a</b>,<b>c</b>) and 2:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>b</b>,<b>d</b>).</p>
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<p>TEM and HRTEM images of samples: BWO (<b>a</b>,<b>c</b>) and 2:6 In<sub>2</sub>O<sub>3</sub>/BWO (<b>b</b>,<b>d</b>).</p>
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<p>XPS spectra of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO: (<b>a</b>) total spectrum; (<b>b</b>) Bi 4f; (<b>c</b>) O 1s; (<b>d</b>) W 4f; and (<b>e</b>) In 3d.</p>
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<p>XPS spectra of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO: (<b>a</b>) total spectrum; (<b>b</b>) Bi 4f; (<b>c</b>) O 1s; (<b>d</b>) W 4f; and (<b>e</b>) In 3d.</p>
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<p>N<sub>2</sub> adsorption–desorption isotherms and pore size distribution curve of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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<p>UV–visible diffuse reflectance spectrum (<b>a</b>) and bandgap diagram (<b>b</b>) of In<sub>2</sub>O<sub>3</sub>.</p>
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<p>PL patterns of samples.</p>
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<p>Time-resolved transient PL decay of BWO and 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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<p>Photodegradation curves (<b>a</b>) and kinetic fitting curves (<b>b</b>) of samples.</p>
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<p>The reuse experiment of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO for RhB degradation.</p>
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<p>XRD patterns of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO before and after the photocatalytic experiment.</p>
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<p>SEM images of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO at 10,000× magnification (<b>a</b>) and 100,000× magnification (<b>b</b>) after cycling experiments.</p>
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<p>XPS spectra of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO before and after the photocatalytic experiment: (<b>a</b>) Bi 4f; (<b>b</b>) W 4f; (<b>c</b>) In 3d.</p>
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<p>XPS spectra of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO before and after the photocatalytic experiment: (<b>a</b>) Bi 4f; (<b>b</b>) W 4f; (<b>c</b>) In 3d.</p>
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<p>Photocurrent response curves (<b>a</b>) and electrochemical impedance spectroscopy curves (<b>b</b>) of BWO and 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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<p>Photocurrent response curves (<b>a</b>) and electrochemical impedance spectroscopy curves (<b>b</b>) of BWO and 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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<p>The degradation degrees of 2:6 In<sub>2</sub>O<sub>3</sub>/BWO in the presence of different scavengers.</p>
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<p>Schematic diagram of photogenerated charge transfer and formation of free radicals in 2:6 In<sub>2</sub>O<sub>3</sub>/BWO.</p>
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13 pages, 7532 KiB  
Article
The Effects of Support Specific Surface Area and Active Metal on the Performance of Biphenyl Selective Hydrogenation to Cyclohexylbenzene
by Jie Fan, Wei Li, Jingyi Yang, Tao Yang, Zhongyi Liu and Meng Zhang
Catalysts 2024, 14(10), 727; https://doi.org/10.3390/catal14100727 - 17 Oct 2024
Abstract
With the rapid development of modern society, the consumption of fossil fuels during the industrial production process produces a significant amount of carcinogens. Converting the highly toxic biphenyl (BP) to the valuable product cyclohexylbenzene (CHB) can decrease the emission of carcinogenic aromatic hydrocarbons. [...] Read more.
With the rapid development of modern society, the consumption of fossil fuels during the industrial production process produces a significant amount of carcinogens. Converting the highly toxic biphenyl (BP) to the valuable product cyclohexylbenzene (CHB) can decrease the emission of carcinogenic aromatic hydrocarbons. In this study, we prepared a series of 20%Ni/SiO2 catalysts with different specific surface areas (SSAs) using the over-volume impregnation method, as well as 20%M/SiO2 (M = Fe, Cu, Co, and Ni) catalysts to highlight the effects of support SSAs and active metal on the performance of BP selective hydrogenation to CHB. The catalysts were characterized by XRD, N2 physisorption, TEM, and H2-TPR, which demonstrated that a high SSA would be helpful for the dispersion of the active metal. The evaluation results revealed that 20%Ni/SiO2-300 exhibited excellent activity and stability in the selective hydrogenation of BP to CHB (BP conversion: 99.6%, CHB yield: 99.3% at the conditions of 200 °C, 3 MPa, 4 h and isopropanol as the solvent) among the catalysts with different SSAs, which was also superior to the performance over the catalysts with other transition metals as the active sites. The structure–activity relationship of the employed catalysts for the selective hydrogenation of BP to CHB was also discussed. Full article
(This article belongs to the Special Issue Feature Papers in "Industrial Catalysis" Section)
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<p>XRD patterns of the calcined 20%Ni/SiO<sub>2</sub> catalysts with different SSAs.</p>
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<p>H<sub>2</sub>-TPR of 20%Ni/SiO<sub>2</sub> catalysts with different SSAs.</p>
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<p>XRD patterns of 20%Ni/SiO<sub>2</sub> catalysts with different SSAs after reduction.</p>
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<p>N<sub>2</sub> adsorption–desorption isotherms (<b>a</b>) and pore size distribution (<b>b</b>) of 20%Ni/SiO<sub>2</sub> catalysts with different SSAs.</p>
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<p>TEM images (<b>a</b>,<b>c</b>,<b>e</b>,<b>g</b>), along with the particle size distribution histograms (<b>b</b>,<b>e</b>,<b>f</b>,<b>h</b>) of 20%Ni/SiO<sub>2</sub> catalysts with different SSAs. (<b>a</b>,<b>b</b>) 20% Ni/SiO<sub>2</sub>-100, (<b>c</b>,<b>d</b>) 20% Ni/SiO<sub>2</sub>-200, (<b>e</b>,<b>f</b>) 20% Ni/SiO<sub>2</sub>-300 and (<b>g</b>,<b>h</b>) 20% Ni/SiO<sub>2</sub>-400.</p>
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<p>XRD patterns of the calcined 20%M/SiO<sub>2</sub> (M = Cu, Co, Fe) catalysts.</p>
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<p>H<sub>2</sub>-TPR curves of 20%M/SiO<sub>2</sub> (M = Cu, Co, Fe) catalysts.</p>
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<p>XRD patterns of the reduced 20%M/SiO<sub>2</sub> (M = Cu, Co, Fe) catalysts.</p>
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<p>N<sub>2</sub> adsorption–desorption isotherms (<b>a</b>) and pore size distributions (<b>b</b>) of 20%M/SiO<sub>2</sub> (M = Cu, Co, Fe) catalysts.</p>
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<p>Catalytic performance of 20%Ni/SiO<sub>2</sub> catalysts for the selective hydrogenation of BP (<b>a</b>) 20%Ni/SiO<sub>2</sub>-100, (<b>b</b>) 20%Ni/SiO<sub>2</sub>-200, (<b>c</b>) 20%Ni/SiO<sub>2</sub>-300 and (<b>d</b>) 20%Ni/SiO<sub>2</sub>-400.</p>
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<p>BP conversion, CHB selectivity, and CHB yield over 20%M/SiO<sub>2</sub> catalysts: (<b>a</b>) 20%Co/SiO<sub>2</sub>, (<b>b</b>) 20%Ni/SiO<sub>2</sub>, (<b>c</b>) 20%Fe/SiO<sub>2</sub>, and (<b>d</b>) 20%Cu/SiO<sub>2</sub>.</p>
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<p>The recycling ability of 20% Ni/SiO<sub>2</sub>-300 catalyst in BP hydrogenation. Reaction conditions: M<sub>catalyst</sub>:M<sub>BP</sub> = 0.1, 40 mL of isopropanol, 2.0 MPa, T = 120 °C, t = 80 min, and stirring rate of 800 rpm.</p>
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19 pages, 3256 KiB  
Article
Synthesis and Characterization of CMC/PAM-Amy Hydrogel and Its Efficacy in Apple Juice Clarification
by Taleeha Roheen, Rimsha Ramzan, Muhammad Nadeem, Farhan Ahmad Atif, Masooma Munir and Tahir Mahmood Qureshi
Processes 2024, 12(10), 2264; https://doi.org/10.3390/pr12102264 - 17 Oct 2024
Viewed by 101
Abstract
The high amount of starch in fruits is responsible for its post-processing cloudiness. In the current study, α-amylase from porcine pancreases was immobilized onto carboxymethyl cellulose/polyacrylamide (CMC/PAM) hydrogel. This in-house-built CMC/PAM-Amy hydrogel offers a more efficient and sustainable solution for apple juice clarification. [...] Read more.
The high amount of starch in fruits is responsible for its post-processing cloudiness. In the current study, α-amylase from porcine pancreases was immobilized onto carboxymethyl cellulose/polyacrylamide (CMC/PAM) hydrogel. This in-house-built CMC/PAM-Amy hydrogel offers a more efficient and sustainable solution for apple juice clarification. To acquire the best immobilization efficiency, the concentration of glutaraldehyde crosslinker was optimized. Biocatalytic characterization studies were brought into consideration for free and immobilized α-amylase. The synthesized native and immobilized CMC/PAM-Amy hydrogels were also characterized using SEM, FTIR and XRD. Under ideal circumstances, the activity of CMC/PAM-Amy was up to 604 μmolmin−1, and its immobilization efficiency was 96.29 ± 1.15%. A kinetic parameters study resulted in a conspicuously lowered Km value for immobilized amylase, signifying its higher affinity for its substrate. CMC/PAM-Amy showed a half-life (t1/2) 3.5 times higher than free-Amy at 50, 55 and 60 °C. The higher values of the inactivation rate constant (kd), free energy of inactivation (ΔG*), enthalpy of inactivation (ΔH*) and change in entropy (ΔS*) of CMC/PAM-Amy manifested the enhanced thermal stability of amylase after immobilization. A reusability study revealed that immobilized amylase retained roughly 70% of its initial catalytic activity after six successive repetitions of the process. CMC/PAM-Amy displayed improved recycling ability operational stability and biocatalytic activity, rendering it an auspicious tool in decreasing the starch content of crude apple juice to about 61% of its total starch content before treatment. Moreover, the values of Brix, viscosity, acidity and turbidity were also decreased in CMC/PAM-Amyclarified apple juice. Therefore, immobilized amylases with other industrial enzymes could be an efficient tool for potential industrial application. Full article
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<p>Influence of pH (<b>a</b>) and temperature (<b>b</b>) on the catalytic activity of free and CMC/PAM-Amy.</p>
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<p>Lineweaver–Burk plot of free and immobilized amylase for varying substrate concentrations.</p>
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<p>Pseudo first-order plots of free and immobilized α-amylase for denaturation at (<b>a</b>) 50 °C; (<b>b</b>) 55 °C; (<b>c</b>) 60 °C.</p>
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<p>Reusability of CMC/PAM-Amy hydrogel.</p>
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<p>SEM images of CMC/PAM hydrogel (<b>A</b>) without incorporated amylase; (<b>B</b>) with incorporated amylase (Amylase incorporated on the surface of CMC/PAM hydrogel is shown by the arrow).</p>
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<p>FTIR peak of (<b>A</b>) CMC hydrogel; (<b>B</b>) CMC/PAM-amylase.</p>
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<p>Thermogram of CMC/PAM hydrogel.</p>
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<p>XRD for (<b>a</b>) CMC/PAM-Amy; (<b>b</b>) CMC/PAM hydrogel.</p>
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<p>Complete scheme of synthesis of CMC/PAM hydrogel, immobilization of α-amylase onto hydrogel, biocatalytic characterization (Influence of pH on free and immobilized α-amylase) characterization studies of native and immobilized hydrogel (SEM image (A) without incorporated Amylase (B) with incorporated Amylase (shown by the arrow) and application of CMC/PAM-Amy in the clarification of apple juice. CMC (Carboxymethyl cellulose), AA (Acrylamide), MBA (1% N,N’-methylene bis-acrylamide). APS (ammonium persulfate).</p>
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21 pages, 5379 KiB  
Article
Artificial Neural Network Modeling of the Removal of Methylene Blue Dye Using Magnetic Clays: An Environmentally Friendly Approach
by Asude Ates, Hülya Demirel, Esra Altintig, Dilay Bozdag, Yasin Usta and Tijen Over Ozçelik
Processes 2024, 12(10), 2262; https://doi.org/10.3390/pr12102262 - 17 Oct 2024
Viewed by 211
Abstract
In this study, the effectiveness of Fe3O4-based clay as a cost-effective material for removing methylene blue (MB) dye from aqueous solutions was evaluated. The structural properties of the clay and Fe3O4-based clay were analyzed using [...] Read more.
In this study, the effectiveness of Fe3O4-based clay as a cost-effective material for removing methylene blue (MB) dye from aqueous solutions was evaluated. The structural properties of the clay and Fe3O4-based clay were analyzed using SEM, XRF, BET, XRD, FTIR, and TGA techniques. In this research, the effects of various aspects, such as adsorbent amount, contact time, solution pH, adsorption temperature, and initial dye concentration, on the adsorption of Fe3O4-based clay are investigated. The experiments aimed at understanding the adsorption mechanism of Fe3O4-based clay have shown that the adsorption kinetics are accurately described by the pseudo-second order kinetic model, while the equilibrium data are well represented by the Langmuir isotherm model. The maximum adsorption capacity (qm) was calculated as 52.63 mg/g at 25 °C, 53.48 mg/g at 30 °C, and 54.64 mg/g at 35 °C. All variables affecting the MB adsorption process were systematically optimized in a controlled experimental framework. The effectiveness of the artificial neural network (ANN) model was refined by modifying variables such as the quantity of neurons in the latent layer, the number of inputs, and the learning rate. The model’s accuracy was assessed using the mean absolute percentage error (MAPE) for the removal and adsorption percentage output parameters. The coefficient of determination (R2) values for the dyestuff training, validation, and test sets were found to be 99.40%, 92.25%, and 96.30%, respectively. The ANN model demonstrated a mean squared error (MSE) of 0.614565 for the training data. For the validation dataset, the model recorded MSE values of 0.99406 for the training data, 0.92255 for the validation set, and 0.96302 for the test data. In conclusion, the examined Fe3O4-based clays offer potential as effective and cost-efficient adsorbents for purifying water containing MB dye in various industrial settings. Full article
(This article belongs to the Section Environmental and Green Processes)
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<p>Explicit formula of MB dyestuff.</p>
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<p>SEM images: (<b>a</b>) clay, (<b>b</b>) C-Fe<sub>3</sub>O<sub>4</sub> before adsorption, and (<b>c</b>) C-Fe<sub>3</sub>O<sub>4</sub> after adsorption.</p>
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<p>TGA-DTA analysis data: (<b>a</b>) raw clay and (<b>b</b>) C-Fe<sub>3</sub>O<sub>4</sub>.</p>
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<p>(<b>a</b>) Clay (<b>b</b>) C-Fe<sub>3</sub>O<sub>4</sub> (<b>c</b>) X-ray diffraction image of C-Fe<sub>3</sub>O<sub>4</sub> after adsorption.</p>
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<p>(<b>a</b>) Clay (<b>b</b>) before adsorption C-Fe<sub>3</sub>O<sub>4</sub> (<b>c</b>) C-Fe<sub>3</sub>O<sub>4</sub> FTIR spectrum after adsorption.</p>
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<p>ANN model.</p>
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<p>(<b>a</b>) Influence of initial pH on C-Fe<sub>3</sub>O<sub>4</sub> adsorption (MB concentrations of 50, 100, and 200 mg/L; adsorbent dosage of 0.1 g/L; the temperature at 25 °C; and adsorption duration of 60 min). (<b>b</b>) The effect of contact time on C-Fe<sub>3</sub>O<sub>4</sub> adsorption (MB concentration: 50, 100, and 200 mg/L; adsorbent amount: 0.1 g/L; temperature: 25 °C). (<b>c</b>) The impact of adsorbent quantity on C-Fe<sub>3</sub>O<sub>4</sub> adsorption (MB concentration, 50, 100, and 200 mg/L; contact time, 60 min; temperature, 25 °C).</p>
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<p>(<b>a</b>) Artificial neural network with a 5-15-1 structure, (<b>b</b>) validation performance, and (<b>c</b>) training parameters. (<b>d</b>) Comparison of percent removal estimation output with actual output, (<b>e</b>) histogram graph, and (<b>f)</b> regression plots.</p>
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<p>(<b>a</b>) Artificial neural network with a 5-15-1 structure, (<b>b</b>) validation performance, and (<b>c</b>) training parameters. (<b>d</b>) Comparison of percent removal estimation output with actual output, (<b>e</b>) histogram graph, and (<b>f)</b> regression plots.</p>
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<p>Langmuir isotherm model of C-Fe<sub>3</sub>O<sub>4</sub> (<b>a</b>): 25 °C, (<b>b</b>): 30 °C, (<b>c</b>): 35 °C.</p>
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<p>Freundlich isotherm model of K-Fe<sub>3</sub>O<sub>4</sub> (<b>a</b>): 25 °C, (<b>b</b>): 30 °C, (<b>c</b>): 35 °C.</p>
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<p>(<b>a</b>) Pseudo-first order kinetics of the adsorption of 25 °C MB with C-Fe<sub>3</sub>O<sub>4</sub>; (<b>b</b>) pseudo-second order kinetics.</p>
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<p>(<b>a</b>) Temperature effect on the adsorption of MB on C-Fe<sub>3</sub>O<sub>4</sub> (contact time: 60 min, pH: 7, adsorbent amount: 0.5 g 100 mL<sup>−1</sup>); (<b>b</b>) Van’t Hoff plot for the adsorption of MB dyestuff onto C-Fe<sub>3</sub>O<sub>4</sub> (adsorbent amount 0.2 g/L, pH 7, solution volume 100 mL and stirring speed 250 rpm).</p>
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<p>MB on C-Fe<sub>3</sub>O<sub>4</sub> after six recovery cycles.</p>
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23 pages, 10596 KiB  
Article
Advanced Nuclear Magnetic Resonance, Fourier Transform–Infrared, Visible-NearInfrared and X-ray Diffraction Methods Used for Characterization of Organo-Mineral Fertilizers Based on Biosolids
by Ramona Crainic, Elena Mihaela Nagy, Gabriel Fodorean, Mihai Vasilescu, Petru Pascuta, Florin Popa and Radu Fechete
Agriculture 2024, 14(10), 1826; https://doi.org/10.3390/agriculture14101826 - 16 Oct 2024
Viewed by 339
Abstract
Biosolids from stabilized sludge present a high fertilization potential, due to their rich content of nutrients and organic matter. The intrinsic and subtle properties of such fertilizers may greatly influence the fertilization efficiency. In this sense, the utility, advantages and limitations of advanced [...] Read more.
Biosolids from stabilized sludge present a high fertilization potential, due to their rich content of nutrients and organic matter. The intrinsic and subtle properties of such fertilizers may greatly influence the fertilization efficiency. In this sense, the utility, advantages and limitations of advanced characterization methods, for the investigation of structural and dynamic properties at the microscopic scale of slightly different formulations of fertilizers were assessed. For that, three formulas of organo-mineral fertilizers based on biosolids (V1, V2 and V3), having at least 2% N, 2% P2O5, and 2% K2O, were characterized by advanced methods, such as 1H NMR relaxometry, 1H MAS and 13C CP-MAS NMR spectroscopy, 1H double-quantum NMR and FT-IR spectroscopy. Advanced structural characterization was performed using SEM, EDX and X-ray diffraction. Four dynamical components were identified in the NMR T2 distribution showing that the rigid component has a percentage larger than 90%, which explains the broad band of NMR spectra confirmed by the distributions of many components in residual dipolar coupling as were revealed by 1H DQ-NMR measurements. SEM and EDX measurements helped the identification of components from crystalline-like X-ray diffraction patterns. To evaluate the release properties of organo-mineral fertilizers, dynamic measurements of classical electric conductivity and pH were performed by placing 0.25 g of the formulas (V1, V2 and V3) in 200 mL of distilled water. The content of N and P were quantified using specific reactants, combined with VIS-nearIR spectroscopy. Two release mechanisms were observed and characterized. It was found that V3 presents the smallest release velocity but releases the largest number of fertilizers. Full article
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<p><sup>1</sup>H NMR <span class="html-italic">T</span><sub>1</sub> distributions of measured fertilizers V1, V2, and V3.</p>
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<p><sup>1</sup>H NMR <span class="html-italic">T</span><sub>2</sub> distributions and deconvolution of measured fertilizers (<b>a</b>) V1, (<b>b</b>) V2, and (<b>c</b>) V3.</p>
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<p>(<b>a</b>) <sup>1</sup>H NMR DQ build-up curve and (<b>b</b>) the distributions of residual dipolar couplings, <math display="inline"><semantics> <mrow> <msub> <mrow> <mover accent="true"> <mrow> <mi>ω</mi> </mrow> <mo>¯</mo> </mover> </mrow> <mrow> <mi>D</mi> </mrow> </msub> </mrow> </semantics></math> measured for the V1, V2, and V3 fertilizers.</p>
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<p>(<b>a</b>) 20 kHz MAS <sup>1</sup>H NMR and (<b>b</b>) 10 kHz MAS <sup>13</sup>C NMR spectra measured for V1, V2 and V3 organo-mineral fertilizers.</p>
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<p>FT-IR spectra of fertilizers V1, V2, and V3.</p>
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<p>SEM-EDX map images of the most abundant elements in the V1, V2 and V3 fertilizers (left) and EDX spectra measured from the EDX maps.</p>
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<p>XRD pattern measured for V1, V2 and V3 organo-mineral fertilizers and assignments of peaks.</p>
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<p>(<b>a</b>) pH; (<b>b</b>) electric conductivity (EC) and (<b>c</b>) total dissolved solids (TDS) measured for granular organo-mineral fertilizers.</p>
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<p>Turbidity measurements for quantitative assessment of potassium content for V1, V2 and V3 fertilizers.</p>
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<p>VIS-nearIR spectra used for the quantitative assessment of nitrogen (<b>a</b>,<b>b</b>) and phosphorus (<b>c</b>,<b>d</b>) content and for V1-V3 fertilizers measured at 6 min (<b>a</b>,<b>c</b>) and 23 min (<b>b</b>,<b>d</b>).</p>
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<p>VIS-nearIR spectra used for the quantitative assessment of nitrogen (<b>a</b>,<b>b</b>) and phosphorus (<b>c</b>,<b>d</b>) content and for V1-V3 fertilizers measured at 6 min (<b>a</b>,<b>c</b>) and 23 min (<b>b</b>,<b>d</b>).</p>
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<p>(<b>a</b>) Electrical conductivity build-up curves and (<b>b</b>) pH decay curves measured for V1–V3 organo-mineral fertilizers during dissolution in distilled water.</p>
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<p>(<b>a</b>) The degree of fertilizers release; (<b>b</b>) the specific release time and (<b>c</b>) the velocity of release determined from electric conductivity build-up curves.</p>
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14 pages, 5326 KiB  
Article
Carbon Materials with Different Dimensions Supported Pt Catalysts for Selective Hydrogenation of 3,4-Dichloronitrobenzene to 3,4-Dichloroaniline
by Nannan Zhan, Yan Xiao, Xingkun Chen, Yuan Tan and Yunjie Ding
Catalysts 2024, 14(10), 724; https://doi.org/10.3390/catal14100724 - 16 Oct 2024
Viewed by 352
Abstract
In this study, carbon materials with different dimensions, including the typical one-dimensional (1D) carbon nanotube (CNT), two-dimensional (2D) graphene (GF), and three-dimensional (3D) activated carbon (AC), were investigated as a support for Pt catalysts for the selective hydrogenation of 3,4-dichloronitrobenzene (3,4-DCNB) to 3,4-dichloroaniline [...] Read more.
In this study, carbon materials with different dimensions, including the typical one-dimensional (1D) carbon nanotube (CNT), two-dimensional (2D) graphene (GF), and three-dimensional (3D) activated carbon (AC), were investigated as a support for Pt catalysts for the selective hydrogenation of 3,4-dichloronitrobenzene (3,4-DCNB) to 3,4-dichloroaniline (3,4-DCAN). Notably, the Pt/CNT catalyst with the lowest dimension exhibited the best conversion of 3,4-DCNB under mild reaction conditions, followed by Pt/GF. Comprehensive characterizations, including XRD, TEM, XPS, and in situ CO DRIFTS, reveal that the dimension of carbon supports plays an important role in the particle size and electronic properties of Pt species, consequently affecting the catalytic performances of Pt catalysts. According to the results, electron-deficient Pt particles with small sizes are more favorable for the hydrogenation of 3,4-DCNB to 3,4-DCAN. In addition, dynamic tests and in situ DRIFTS of 3,4-DCNB indicated that the carbonaceous supports will largely influence the adsorption and activation capacity of the Pt catalysts, so that Pt loaded on CNT and GF are superior to that on the AC. We believe this study will provide good guidance for designing efficient carbon-supported metal catalysts for selective hydrogenation. Full article
(This article belongs to the Section Nanostructured Catalysts)
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<p>(<b>a</b>) N<sub>2</sub> adsorption–desorption isotherms. (<b>b</b>) BJH pore size distributions.</p>
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<p>(<b>a</b>) XRD patterns and (<b>b</b>) Raman spectra of different supported Pt catalysts.</p>
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<p>SEM images of different supported Pt catalysts: (<b>a</b>) Pt/AC; (<b>b</b>) Pt/GF; and (<b>c</b>) Pt/CNT.</p>
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<p>TEM and HRTEM images of different supported Pt catalysts: (<b>a</b>,<b>d</b>) Pt/AC; (<b>b</b>,<b>e</b>) Pt/GF; and (<b>c</b>,<b>f</b>) Pt/CNT.</p>
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<p>(<b>a</b>) Pt 4f and (<b>b</b>) O 1s XPS spectra of different carbon materials supported Pt catalysts.</p>
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<p>In situ DRIFT spectra of adsorbed CO on different Pt catalysts.</p>
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<p>Dependence of reaction rates on different factors for the hydrogenation of 3,4-DCNB over the Pt/AC, Pt/GF, and Pt/CNT catalysts: (<b>a</b>) reaction temperature, (<b>b</b>) Arrhenius plots, (<b>c</b>) the concentration of DCNB, and (<b>d</b>) the pressure of H<sub>2</sub>. The reaction rates were calculated based on the weight of transformed 3,4-DCNB (g) per unit of catalyst (g) per hour, with the conversion of 3,4-DCNB kept below 20%.</p>
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<p>In situ DRIFTS of 3,4-DCNB at 85 °C, over the (<b>a</b>) AC, (<b>b</b>) GF, and (<b>c</b>) CNT supports.</p>
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<p>In situ DRIFTS of 3,4-DCNB at 85 °C, over the (<b>a</b>) Pt/AC, (<b>b</b>) Pt/GF, and (<b>c</b>) Pt/CNT catalysts.</p>
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<p>The radar plot of the conversion of 3,4-DCNB, selectivity of 3,4-DCAN, specific reaction rates, Pt particle sizes, and Pt<sup>0</sup>/Pt<sup>2+</sup> ratio of presented Pt catalysts.</p>
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17 pages, 4527 KiB  
Article
Performance of Cobalt-Doped C3N5 Electrocatalysis Nitrate in Ammonia Production
by Boyu Liang, Yueqi Wu, Jing Han, Wenqiang Deng, Xinyao Zhang, Runrun Li, Yan Hong, Jie Du, Lichun Fu and Runhua Liao
Coatings 2024, 14(10), 1327; https://doi.org/10.3390/coatings14101327 - 16 Oct 2024
Viewed by 313
Abstract
In this experiment, C3N5 was synthesized by pyrolysis of 3-amino-1,2,4 triazole material, and then 1% Co-C3N5, 3% Co-C3N5, 5% Co-C3N5, 7% Co-C3N5, and 9% [...] Read more.
In this experiment, C3N5 was synthesized by pyrolysis of 3-amino-1,2,4 triazole material, and then 1% Co-C3N5, 3% Co-C3N5, 5% Co-C3N5, 7% Co-C3N5, and 9% Co-C3N5 were synthesized by varying the mass ratio of cobalt chloride to C3N5 by stirring and ultrasonic shaking. SEM, XPS, and XRD tests were performed on the synthesized materials. The experimental results showed that Co atoms were successfully doped into C3N5. The electrocatalytic reduction experiments were performed to evaluate their NH3 yields and electrochemical properties. The results showed that the ammonia yield obtained by the electrolysis of the 9% Co-C3N5 catalyst as the working electrode in a mixed electrolytic solution of 0.1 mol/L KNO3 and 0.1 mol/L KOH for 1 h at a potential of −1.0 V vs. RHE was 0.633 ± 0.02 mmol∙h−1∙mgcat−1, and the Faraday efficiency was 65.98 ± 2.14%; under the same experimental conditions, the ammonia production rate and Faraday efficiency of the C3N5 catalyst were 0.049 mmol∙h−1∙mgcat−1 and 16.41%, respectively, and the ammonia production rate of the C3N5 catalyst was nearly 13-fold worse than the 9% Co-C3N5, which suggests that Co can improve the Faraday efficiency and ammonia yield of the electrocatalytic reduction of NO3. This is due to the strong synergistic effect between the cobalt and C3N5 components, with C3N5 providing abundant and homogeneous sites for nitrogen coordination and the Co-N species present in the material being highly efficient active sites. The slight change in current density after five trials of 9% Co-C3N5 and the decrease in ammonia yield by about 12% in five repetitions of the experiment indicate that 9% Co-C3N5 can be recycled and work stably in electrocatalytic reactions and has good application prospects. Full article
(This article belongs to the Special Issue Advanced Materials for Electrocatalysis and Energy Storage)
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<p>NH<sub>4</sub><sup>+</sup> standard mass concentration profile.</p>
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<p>XRD diffractograms of C<sub>3</sub>N<sub>5</sub> and Co-C<sub>3</sub>N<sub>5</sub> for each doping ratio.</p>
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<p>(<b>a</b>) FT-IR comparison between C<sub>3</sub>N<sub>5</sub> and composites; (<b>b</b>) T-IR magnification of both 1% Co-C<sub>3</sub>N<sub>5</sub> and 9% Co-C<sub>3</sub>N<sub>5.</sub></p>
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<p>(<b>a</b>) XPS full spectrum of C<sub>3</sub>N<sub>5</sub>, 1% Co-C<sub>3</sub>N<sub>5</sub> and 3% Co-C<sub>3</sub>N<sub>5</sub>; (<b>b</b>) XPS full spectrum of 5% Co-C<sub>3</sub>N<sub>5</sub>, 7% Co-C<sub>3</sub>N<sub>5</sub> and 9% Co-C<sub>3</sub>N<sub>5</sub>; (<b>c</b>) C1s spectrum of 1% Co-C<sub>3</sub>N<sub>5</sub>, 3% Co-C<sub>3</sub>N<sub>5</sub> and 9% Co-C<sub>3</sub>N<sub>5</sub>; (<b>d</b>) N1s spectrum of 1% Co-C<sub>3</sub>N<sub>5</sub>, 3% Co-C<sub>3</sub>N<sub>5</sub> and 9% Co-C<sub>3</sub>N<sub>5</sub>; (<b>e</b>) Co2p spectrum of 1% Co-C<sub>3</sub>N<sub>5</sub>, 3% Co-C<sub>3</sub>N<sub>5</sub> and 9% Co-C<sub>3</sub>N<sub>5.</sub></p>
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<p>(<b>a</b>) Scanning electron microscope image of C<sub>3</sub>N<sub>5</sub>; (<b>b</b>) scanning electron microscope image of Co-C<sub>3</sub>N<sub>5</sub>; (<b>c</b>) copper element distribution of Co-C<sub>3</sub>N<sub>5.</sub></p>
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<p>(<b>a</b>) Scanning electron microscope image of C<sub>3</sub>N<sub>5</sub>; (<b>b</b>) scanning electron microscope image of Co-C<sub>3</sub>N<sub>5</sub>; (<b>c</b>) copper element distribution of Co-C<sub>3</sub>N<sub>5.</sub></p>
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<p>9% Co-C<sub>3</sub>N<sub>5</sub> energy-dispersive spectrum.</p>
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<p>LSV plot of catalysts possessing electrocatalytic nitrate activity in electrolytes.</p>
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<p>(<b>a</b>) Plot of NH<sub>3</sub> yield rate and Faraday efficiency of catalysts at −0.5~−1.0V vs. RHE potentials; (<b>b</b>) comparison of NH<sub>3</sub> yield rate of catalysts; (<b>c</b>) comparison of Faraday efficiency of catalysts; (<b>d</b>) NH<sub>3</sub> yield rate of catalysts at −0.8 V vs. RHE potentials.</p>
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<p>(<b>a</b>) Plot of NH<sub>3</sub> yield rate and Faraday efficiency of 9% Co-C<sub>3</sub>N<sub>5</sub> at −1.0 V vs. RHE potential cycling test repeated 5 times; (<b>b</b>) Plot of LSV of 9% Co-C<sub>3</sub>N<sub>5</sub> at −1.0 V vs. RHE potential test repeated 5 times.</p>
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<p>(<b>a</b>) Comparison of LSV before and after 12 h of electrolysis of 9% Co-C<sub>3</sub>N<sub>5</sub> at −1.0 V vs. RHE potential; (<b>b</b>) Comparison of NH<sub>3</sub> yield rate and Faraday efficiency before and after 12 h of electrolysis of 9% Co-C<sub>3</sub>N<sub>5</sub> at −1.0 V vs. RHE potential.</p>
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