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39 pages, 1431 KiB  
Article
The Interplay of Dietary Habits, Economic Factors, and Globalization: Assessing the Role of Institutional Quality
by Mohammad Naim Azimi, Mohammad Mafizur Rahman and Tek Maraseni
Nutrients 2024, 16(18), 3116; https://doi.org/10.3390/nu16183116 (registering DOI) - 15 Sep 2024
Abstract
Background: Dietary habits are pivotal for population health and well-being, yet remain a pressing global issue, particularly in Sub-Saharan Africa (SSA), where economic instability and institutional challenges exacerbate dietary problems. Despite extensive research, there is a notable gap in the literature regarding the [...] Read more.
Background: Dietary habits are pivotal for population health and well-being, yet remain a pressing global issue, particularly in Sub-Saharan Africa (SSA), where economic instability and institutional challenges exacerbate dietary problems. Despite extensive research, there is a notable gap in the literature regarding the direct and interactive effects of institutional quality and inflationary shocks on dietary habits. Methods: This study delves into these complex interplays across 44 SSA nations from 2002 to 2022. Employing an innovative entropy method (EM) and the generalized autoregressive conditional heteroskedasticity (GARCH) modeling, the study introduces an inclusive institutional quality index and an inflationary shock predictor as crucial determinants of dietary habits in the literature. Results: The results from the panel-corrected standard error (PCSE) method and feasible generalized least squares (FGLS) model reveal that per capita GDP, school enrollment rate, government expenditures, globalization index, and urbanization are positively associated with population dietary habits, while inflationary shock, food insecurity, and unemployment rate exert negative influences. Notably, institutional quality acts as a catalyst, amplifying the positive effects of the former group and absorbing the negative impacts of the latter on population dietary habits. Additionally, a dynamic panel causality analysis confirms a bidirectional causality nexus between population dietary habits and all variables, except for inflationary shocks, which demonstrate a unidirectional causality link. Conclusions: These findings carry significant policy implications, underscoring the complex dynamics between institutional quality, inflationary shocks, and dietary habits in the region. The bidirectional causality highlights the need for holistic interventions that address economic, social, and institutional factors simultaneously. Moreover, the unidirectional causality of inflationary shocks on dietary habits suggests that stabilizing inflation is critical to protecting dietary habits. These results provide critical insights for policymakers to design targeted interventions aimed at improving nutrition, bolstering institutional frameworks, and ensuring public health resilience in the face of economic and social shocks. Full article
(This article belongs to the Section Nutrition and Public Health)
11 pages, 2390 KiB  
Article
Catalytic Decontamination of Carbon Monoxide Using Strong Metal–Support Interactions on TiO2 Microparticles
by Avraham Dayan, Jacob Alter and Gideon Fleminger
Catalysts 2024, 14(9), 622; https://doi.org/10.3390/catal14090622 (registering DOI) - 15 Sep 2024
Abstract
The traditional catalytic oxidation of carbon monoxide (CO) using metal oxide catalysts often requires either high temperatures (thermocatalysis) or ultraviolet light (UV) excitation (photocatalysis), limiting practical applications under ambient conditions. Our research aimed to develop a catalytic system capable of oxidizing CO to [...] Read more.
The traditional catalytic oxidation of carbon monoxide (CO) using metal oxide catalysts often requires either high temperatures (thermocatalysis) or ultraviolet light (UV) excitation (photocatalysis), limiting practical applications under ambient conditions. Our research aimed to develop a catalytic system capable of oxidizing CO to CO2 at room temperature and in the dark. Using the Strong Metal–Support Interaction (SMSI) methodology, several titanium oxide (TiO2)-complexed metals were prepared (Ag, Au, Pd, and Pt). The highest catalytic efficiency of CO oxidation at room temperature was demonstrated for the TiO2-Pt complex. Therefore, this complex was further examined structurally and functionally. Two modes of operation were addressed. The first involved applying the catalytic system to remove CO from an individual’s environment (environmental system), while the second involved the installation of the catalysis chamber as a part of a personal protection unit (e.g., a mask). The catalytic activity exhibited a significant reduction in CO levels in both the environmental and personal protection scenarios. The practical application of the system was demonstrated through efficient CO oxidation in air emitted from a controlled fire experiment conducted in collaboration with the Israel Fire and Rescue Authority. Full article
(This article belongs to the Special Issue Catalytic CO Oxidation and Preferential CO Oxidation (PROX) II)
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Figure 1
<p>Structural characteristics of TiO<sub>2</sub>-Pt microparticles. (<b>A</b>)—Visual appearance of microparticle suspensions of TiO<sub>2</sub> (left) and TiO<sub>2</sub>-Pt (right). (<b>B</b>)—TEM micrograph; the Pt clusters are black. (<b>C</b>)—HRSEM micrographs of TiO<sub>2</sub>-Pt microparticles. (<b>D</b>)—Enlargement of (<b>C</b>). The Pt clusters on the TiO<sub>2</sub>-Pt surface are white. (<b>E</b>)—EDS spectrum of point “a” in plate (<b>D</b>). The green arrows are Ti, the orange ones are Pt, and the red one is O. (<b>F</b>)—Reflectance spectra of TiO<sub>2</sub> (blue) and TiO<sub>2</sub>-Pt (red) microparticles; the black TiO<sub>2</sub>-Pt microparticles fail to reflect light.</p>
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<p>(<b>A</b>) Schematic illustration of the environmental model. (a) A stirred container (20 L) fed with CO at a certain concentration from a reservoir (b). The air is pumped by a flow-rate-regulated pump (c) through a flowmeter (d) into a reactor cell (e) and back into the container. The CO concentration in the container is continuously monitored by a CO detector (f). To simulate maximal catalytic efficiency (α = 1), the tubing at point X was disconnected, and fresh air was sucked into the container. (<b>B</b>) A detailed scheme of the reactor cell (4 cm diameter, 3.5 cm height). The bottom-to-top air flow creates a “floating bed” situation, causing a better dispersion of the particles in the reactor.</p>
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<p>The catalytic activity and the efficiencies (α) at various amounts of TiO<sub>2</sub>-Pt in the reactor. The reactor was operated at a flow rate of 3 L per minute at room temperature.</p>
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<p>Generation of CO<sub>2</sub> (triangles) during CO oxidation (circles) in the container.</p>
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<p>The linear system for CO oxidation. The source for CO (blue balloon) is a 20–80 L aluminum inflatable balloon, containing CO at certain concentrations. CO<sub>in</sub> and CO<sub>out</sub> were monitored in parallel streams to avoid interference of the detectors’ pumps with the general flow rate. (<b>A</b>)—A uni-cell unit. (<b>B</b>)—A multi-cell unit.</p>
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<p>Catalytic treatment of CO released by an initiated fire in a sealed room.</p>
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11 pages, 1969 KiB  
Article
Key Components Degradation in Proton Exchange Membrane Fuel Cells: Unraveling Mechanisms through Accelerated Durability Testing
by Keguang Yao, Li Wang, Xin Wang, Xiaowu Xue, Shuai Li, Hanwen Zhang, Zhengnan Li, Yanpu Li, Gangping Peng, Min Wang and Haijiang Wang
Processes 2024, 12(9), 1983; https://doi.org/10.3390/pr12091983 (registering DOI) - 14 Sep 2024
Viewed by 169
Abstract
In the process of promoting the commercialization of proton exchange membrane fuel cells, the long-term durability of the fuel cell has become a key consideration. While existing durability tests are critical for assessing cell performance, they are often time-consuming and do not quickly [...] Read more.
In the process of promoting the commercialization of proton exchange membrane fuel cells, the long-term durability of the fuel cell has become a key consideration. While existing durability tests are critical for assessing cell performance, they are often time-consuming and do not quickly reflect the impact of actual operating conditions on the cell. In this study, improved testing protocols were utilized to solve this problem, which is designed to shorten the testing cycle and evaluate the degradation of the cell performance under real operating conditions more efficiently. Accelerated durability analysis for evaluating the MEA lifetime and performance decay process was carried out through two testing protocols—open circuit voltage (OCV)-based accelerated durability testing (ADT) and relative humidity (RH) cycling-based ADT. OCV-based ADT revealed that degradation owes to a combined mechanical and chemical process. RH cycling-based ADT shows that degradation comes from a mainly mechanical process. In situ fluoride release rate technology was employed to elucidate the degradation of the proton exchange membrane during the ADT. It was found that the proton exchange membrane suffered more serious damage under OCV-based ADT. The loss of F- after the durability test was up to 3.50 × 10−4 mol/L, which was 4.3 times that of the RH cycling-based ADT. In addition, the RH cycling-based ADT had a significant effect on the catalyst layer, and the electrochemically active surface area decreased by 48.6% at the end of the ADT. Moreover, it was observed that the agglomeration of the catalysts was more obvious than that of OCV-based ADT by transmission electron microscopy. It is worth noting that both testing protocols have no obvious influence on the gas diffusion layer, and the contact angle of gas diffusion layers does not change significantly. These findings contribute to understanding the degradation behavior of proton exchange membrane fuel cells under different working conditions, and also provide a scientific basis for developing more effective testing protocols. Full article
20 pages, 1236 KiB  
Article
Photo-Fenton Treatment under UV and Vis Light Reduces Pollution and Toxicity in Water from Madín Dam, Mexico
by Deysi Amado-Piña, Rubi Romero, Emmanuel Salazar Carmona, Armando Ramírez-Serrano, Leobardo Manuel Gómez-Oliván, Gustavo Elizalde-Velázquez and Reyna Natividad
Catalysts 2024, 14(9), 620; https://doi.org/10.3390/catal14090620 (registering DOI) - 14 Sep 2024
Viewed by 171
Abstract
Water from Madín Dam in Mexico has been shown to contain a wide variety of pollutants such as drugs, pesticides, personal care products and compounds that are released into the environment as waste from production processes. In this work, the effect of the [...] Read more.
Water from Madín Dam in Mexico has been shown to contain a wide variety of pollutants such as drugs, pesticides, personal care products and compounds that are released into the environment as waste from production processes. In this work, the effect of the main process variables on the percentage of total organic carbon (TOC) removal in water samples from the Madín reservoir was studied by applying a photo-Fenton treatment catalyzed with iron-pillared clays. The catalyst was characterized by XRD, N2 physisorption, DRS and XPS. The sampling and characterization of the water from the Madín reservoir was carried out according to Mexican standards. The system for treatment tests was 0.1 L of reaction volume and a controlled temperature of 23–25 °C, and the reaction system was kept under constant stirring. After 4 h of treatment time under UV light, the TOC removal was 90%, and it was 60% under Vis light. The main ROS involved in the photo-Fenton process driven by UVC light were hydroxyl radicals, while hydroperoxyl radicals predominate in the Vis-light-driven process. Evidence of superoxide anion participation was not found. The toxicity of untreated and treated water was assessed on Danio rerio specimens, and it was observed to be reduced after the photo-Fenton treatment. Full article
(This article belongs to the Section Photocatalysis)
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<p>Diffractograms of Fe-PILC and bentonite clay.</p>
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<p>Total organic carbon removal efficiency in water samples from Madín reservoir through different treatment processes. Reaction volume: 0.1 L, T: 25 C, pH<sub>o</sub>: 6.02, treatment time: 60 min, UV light: 254 nm, 166 W/m<sup>2</sup>, Vis light: (3 lamps, 100 W/m<sup>2</sup> each).</p>
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<p>Effect of initial oxygen presence (photo-Fenton-N<sub>2</sub>) and addition of radical scavengers (isopropanol, IPA; benzoquinone, BQ) to the photo-Fenton system under (<b>a</b>) UVC light (254 nm, 166 W/m<sup>2</sup>) and (<b>b</b>) Vis light (3 lamps, 100 W/m<sup>2</sup> each). Reaction conditions: volume: 0.1 L, T: 25 °C, pH<sub>o</sub>: 6.02, catalyst loading (W<sub>cat</sub>): 0.500 g/L, reaction time: 60 min for processes in (<b>a</b>) and 240 min for processes in (<b>b</b>).</p>
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<p>Location of the water sampling stations inside the Madín Dam: New Madín (1), Old Madín (2), entrance of the Tlalnepantla River (3), entrance of the San Juan River (4), dam curtain (5).</p>
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18 pages, 4620 KiB  
Article
Fractal Behavior of Nanostructured Pt/TiO2 Catalysts: Synthesis, Characterization and Evaluation of Photocatalytic Hydrogen Generation
by Anca Vasile, Gianina Dobrescu, Veronica Bratan, Mircea Teodorescu, Cornel Munteanu, Irina Atkinson, Catalin Negrila, Florica Papa and Ioan Balint
Catalysts 2024, 14(9), 619; https://doi.org/10.3390/catal14090619 - 13 Sep 2024
Viewed by 291
Abstract
The fractal characterization of supported nanoparticles is a useful tool for obtaining structural and morphological information that strongly impacts catalytic properties. We have synthesized and characterized Pt supported on TiO2 nanostructures. Triblock copolymers with thermosensitive properties were used as templating agents during [...] Read more.
The fractal characterization of supported nanoparticles is a useful tool for obtaining structural and morphological information that strongly impacts catalytic properties. We have synthesized and characterized Pt supported on TiO2 nanostructures. Triblock copolymers with thermosensitive properties were used as templating agents during the synthesis process. In addition to the several techniques used for the characterization of the materials, we carried out fractal analysis. The prepared materials showed a reduction in the band gap of TiO2 from 3.44 to 3.01 eV. The extended absorption in the 500–700 nm regions is mostly attributed to the presence of supported Pt nanoparticles. The ability of the nanostructured Pt/TiO2 catalysts to generate H2 in an aqueous solution was evaluated. The test reaction was carried out in the presence of methanol, as a hole scavenger, under simulated solar light. Pt/TiO2-3TB shows the highest rate of H2 (4.17 mmol h−1 gcat−1) when compared to Pt/TiO2-0TB (3.65 mmol h−1 gcat−1) and Pt/TiO2-6TB (2.29 mmol h−1 gcat−1) during simulated solar light irradiation. Pt/TiO2-3TB exhibits a more structured organization (fractal dimensions of 1.65–1.74 nm at short scales, 1.27–1.30 nm at long scales) and a distinct fractal behavior. The generation of hydrogen via photocatalysis can be linked to the fractal characteristics. Full article
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Figure 1
<p>SEM images of Pt/TiO<sub>2</sub>-0TB (<b>a</b>), Pt/TiO<sub>2</sub>-3TB (<b>b</b>), and Pt/TiO<sub>2</sub>-6TB (<b>c</b>).</p>
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<p>TEM images (<b>A</b>) Pt/TiO<sub>2</sub>-0TB, (<b>B</b>) Pt/TiO<sub>2</sub>-3TB, and (<b>C</b>) Pt/TiO<sub>2</sub>-6TB.</p>
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<p>TEM micrographs of Pt/TiO<sub>2</sub>-0TB (<b>A1</b>,<b>A2</b>), Pt/TiO<sub>2</sub>-3TB (<b>B1</b>,<b>B2</b>), and Pt/TiO<sub>2</sub>-6TB (<b>C1</b>,<b>C2</b>) used to compute fractal dimensions.</p>
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<p>Particle size distribution of Pt nanoparticles for Pt/TiO<sub>2</sub>-0TB (<b>A1</b>,<b>A2</b>), Pt/TiO<sub>2</sub>-3TB (<b>B1</b>,<b>B2</b>), and Pt/TiO<sub>2</sub>-6TB (<b>C1</b>,<b>C2</b>) samples.</p>
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<p>X-ray diffraction patterns of Pt/TiO<sub>2</sub>-0TB, Pt/TiO<sub>2</sub>-3TB, Pt/TiO<sub>2</sub>-6TB, and TiO<sub>2</sub> catalysts.</p>
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<p>(<b>a</b>) Pt 4f and (<b>b</b>) Ti 2p XPS spectra for Pt/TiO<sub>2</sub>-0TB, Pt/TiO<sub>2</sub>-3TB, and Pt/TiO<sub>2</sub>-6TB.</p>
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<p>Kubelka–Munk absorption curves of Pt/TiO<sub>2</sub>-0TB, Pt/TiO<sub>2</sub>-3TB, Pt/TiO<sub>2</sub>-6TB, and TiO<sub>2</sub> as a reference, at room temperature.</p>
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<p>Photocatalytic hydrogen generation in the presence of methanol from the reaction catalyzed by Pt/TiO<sub>2</sub>-0TB, Pt/TiO<sub>2</sub>-3TB, and Pt/TiO<sub>2</sub>-6TB. Reaction conditions: catalyst weight, 0.050 g; temperature, 18 °C; reactant, NO<sub>3</sub><sup>−</sup>, 120 mL; hole scavenger, methanol, 1 mL; Ar, 20 cm<sup>3</sup> min<sup>−1</sup>; solar simulator.</p>
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<p>Illustration of the reaction mechanism for photocatalytic H<sub>2</sub> evolution over Pt supported on TiO<sub>2</sub> nanostructures in the presence of methanol under simulated solar light irradiation.</p>
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15 pages, 4199 KiB  
Article
Ordered versus Non-Ordered Mesoporous CeO2-Based Systems for the Direct Synthesis of Dimethyl Carbonate from CO2
by Nicoletta Rusta, Fausto Secci, Valentina Mameli and Carla Cannas
Nanomaterials 2024, 14(18), 1490; https://doi.org/10.3390/nano14181490 - 13 Sep 2024
Viewed by 309
Abstract
In this work, non-ordered and ordered CeO2-based catalysts are proposed for CO2 conversion to dimethyl carbonate (DMC). Particularly, non-ordered mesoporous CeO2, consisting of small nanoparticles of about 8 nm, is compared with two highly porous (635–722 m2 [...] Read more.
In this work, non-ordered and ordered CeO2-based catalysts are proposed for CO2 conversion to dimethyl carbonate (DMC). Particularly, non-ordered mesoporous CeO2, consisting of small nanoparticles of about 8 nm, is compared with two highly porous (635–722 m2/g) ordered CeO2@SBA-15 nanocomposites obtained by two different impregnation strategies (a two-solvent impregnation method (TS) and a self-combustion (SC) method), with a final CeO2 loading of 10 wt%. Rietveld analyses on XRD data combined with TEM imaging evidence the influence of the impregnation strategy on the dispersion of the active phase as follows: nanoparticles of 8 nm for the TS composite vs. 3 nm for the SC composite. The catalytic results show comparable activities for the mesoporous ceria and the CeO2@SBA-15_SC nanocomposite, while a lower DMC yield is found for the CeO2@SBA-15_TS nanocomposite. This finding can presumably be ascribed to a partial obstruction of the pores by the CeO2 nanoparticles in the case of the TS composite, leading to a reduced accessibility of the active phase. On the other hand, in the case of the SC composite, where the CeO2 particle size is much lower than the pore size, there is an improved accessibility of the active phase to the molecules of the reactants. Full article
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Graphical abstract

Graphical abstract
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<p>WA-XRD (<b>a</b>) and SA-XRD (<b>b</b>) patterns of all the samples.</p>
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<p>Nitrogen physisorption isotherms (<b>a</b>) and BJH pore size distributions (<b>b</b>) of all the samples.</p>
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<p>TEM micrographs of CeO<sub>2</sub>_Meso (<b>a</b>–<b>c</b>).</p>
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<p>TEM micrographs of the SBA-15 support (<b>a</b>–<b>c</b>).</p>
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<p>Bright-field (<b>a</b>–<b>c</b>,<b>g</b>–<b>i</b>) and dark-field (<b>d</b>–<b>f</b>,<b>j</b>–<b>l</b>) micrographs of CeO<sub>2</sub>@SBA-15_TS (<b>a</b>–<b>f</b>) and CeO<sub>2</sub>@SBA-15_SC (<b>g</b>–<b>l</b>).</p>
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<p>Line profile EDX analyses on CeO<sub>2</sub>@SBA-15_TS (<b>a</b>) and CeO<sub>2</sub>@SBA-15_SC (<b>b</b>). The data for Ce, Si, and O have been normalized.</p>
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<p>DMC yield (mmol/g<sub>act</sub>.<sub>ph</sub>) of the catalysts.</p>
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47 pages, 6874 KiB  
Review
Nanoalchemy: Unveiling the Power of Carbon Nanostructures and Carbon–Metal Nanocomposites in Synthesis and Photocatalytic Activity
by Yalini Devi Neelan, Senthil Bakthavatchalam, Shanmugam Mahalingam, Krishnasamy Sreenivason Yoganand, Shunmuga Vadivu Ramalingam, Umamaheswari Rajendran, Rajasekaran Ramu, Tae-Youl Yang, Junghwan Kim and Raji Atchudan
Catalysts 2024, 14(9), 618; https://doi.org/10.3390/catal14090618 - 13 Sep 2024
Viewed by 288
Abstract
Due to a rise in industrial pollutants in modern life, the climate and energy crisis have grown more widespread. One of the best ways to deal with dye degradation, hydrogen production, and carbon dioxide reduction issues is the photocatalytic technique. Among various methods, [...] Read more.
Due to a rise in industrial pollutants in modern life, the climate and energy crisis have grown more widespread. One of the best ways to deal with dye degradation, hydrogen production, and carbon dioxide reduction issues is the photocatalytic technique. Among various methods, catalytic technology has demonstrated tremendous promise in recent years as a cheap, sustainable, and environmentally benign technology. The expeditious establishment of carbon-based metal nanoparticles as catalysts in the disciplines of materials and chemical engineering for catalytic applications triggered by visible light is largely attributed to their advancement. There have been many wonderful catalysts created, but there are still many obstacles to overcome, which include the cost of catalysts being reduced and their effectiveness being increased. Carbon-based materials exhibit a unique combination of characteristics that make them ideal catalysts for various reaction types. These characteristics include an exceptional electrical conductivity, well-defined structures at the nanoscale, inherent water repellency, and the ability to tailor surface properties for specific applications. This versatility allows them to be effective in diverse catalytic processes, encompassing organic transformations and photocatalysis. The emergence of carbon-based nanostructured materials, including fullerenes, carbon dots, carbon nanotubes, graphitic carbon nitride, and graphene, presents a promising alternative to conventional catalysts. This review focuses on the diverse functionalities of these materials within the realm of catalysis materials for degradation, hydrogen production, and carbon dioxide reduction. Additionally, it explores the potential for their commercialization, delving into the underlying mechanisms and key factors that influence their performance. It is anticipated that this review will spur more research to develop high-performance carbon-based materials for environmental applications. Full article
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<p>Illustrating the various features of photocatalysts.</p>
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<p>Illustrates the various roles of the carbon material in photocatalysts.</p>
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<p>Schematic representation of various forms of carbon.</p>
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<p>The image illustrates the different properties of carbon.</p>
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<p>The soccer-ball-like form of the carbon-60 Bucky ball [<a href="#B29-catalysts-14-00618" class="html-bibr">29</a>].</p>
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<p>Various shapes of carbon nanotubes, such as (<b>a</b>) structures of SCNT and CNT and (<b>b</b>) geometrical structures of SCNT and CNT [<a href="#B40-catalysts-14-00618" class="html-bibr">40</a>].</p>
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<p>Illustrates the classification of carbon dots [<a href="#B46-catalysts-14-00618" class="html-bibr">46</a>].</p>
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<p>Various synthesis techniques used in top-down approaches.</p>
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<p>Different synthesis methods for bottom-up approaches.</p>
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<p>Different approaches for improving photocatalyst performance.</p>
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<p>Schematic design of the photodegradation mechanism [<a href="#B116-catalysts-14-00618" class="html-bibr">116</a>].</p>
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<p>Schematic illustration for the mechanism of hydrogen production.</p>
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<p>Schematic illustration for the mechanism of carbon dioxide reduction.</p>
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30 pages, 7987 KiB  
Review
Catalytic Reduction of Aromatic Nitro Compounds to Phenylhydroxylamine and Its Derivatives
by Min Yu, Dachen Ouyang, Liqiang Wang and You-Nian Liu
Molecules 2024, 29(18), 4353; https://doi.org/10.3390/molecules29184353 - 13 Sep 2024
Viewed by 266
Abstract
Phenylhydroxylamine and its derivates (PHAs) are important chemical intermediates. Phenylhydroxylamines are mainly produced via the catalytic reduction of aromatic nitro compounds. However, this catalytic reduction method prefers to generate thermodynamically stable aromatic amine. Thus, designing suitable catalytic systems, especially catalysts to selectively convert [...] Read more.
Phenylhydroxylamine and its derivates (PHAs) are important chemical intermediates. Phenylhydroxylamines are mainly produced via the catalytic reduction of aromatic nitro compounds. However, this catalytic reduction method prefers to generate thermodynamically stable aromatic amine. Thus, designing suitable catalytic systems, especially catalysts to selectively convert aromatic nitro compounds to PHAs, has received increasing attention but remains challenging. In this review, we initially provide a brief overview of the various strategies employed for the synthesis of PHAs, focusing on reducing aromatic nitro compounds. Subsequently, an in-depth analysis is presented on the catalytic reduction process, encompassing discussions on catalysts, reductants, hydrogen sources, and a comprehensive assessment of the merits and drawbacks of various catalytic systems. Furthermore, a concise overview is provided regarding the progress made in comprehending the mechanisms involved in this process of catalytic reduction of aromatic nitro compounds. Finally, the main challenges and prospects in PHAs’ production via catalytic reduction are outlined. Full article
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<p>Non-catalytic reduction methods for preparing PHAs.</p>
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<p>(<b>a</b>) Schematic diagram of selective photo induced reduction of nitroaromatic hydrocarbons to N-PHA. (<b>b</b>) The Mechanism for the photoinduced synthesis of N-PHA from Nitrobenzene. Reproduced with permission from Ref. [<a href="#B57-molecules-29-04353" class="html-bibr">57</a>]. Copyright 2020 American Chemical Society.</p>
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<p>(<b>a</b>) Selective reduction of PHAs under the action of DMSO. (<b>b</b>) Several pathways in the hydrogenation of nitrobenzene. Reproduced with permission from Ref. [<a href="#B64-molecules-29-04353" class="html-bibr">64</a>]. Copyright 1987 American Chemical Society.</p>
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<p>(<b>a</b>) Structures and charge difference of adsorbed DMAP models, and (<b>b</b>) the hypothetical formation mechanism of FLP, (<b>c</b>) the mechanism for Pt-catalyzed catalytic hydrogenation of nitroarene into N-PHA, and (<b>d</b>) continuous-flow reactor setup of hydrogenation of nitroarenes. Reproduced with permission from Ref. [<a href="#B68-molecules-29-04353" class="html-bibr">68</a>]. Copyright 2023 Multidisciplinary Digital Publishing Institute.</p>
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<p>(<b>a</b>) TEM image of Pt/N-CNF-H, reproduced with permission from Ref. [<a href="#B72-molecules-29-04353" class="html-bibr">72</a>]. Copyright 2011 Wiley-VCH. (<b>b</b>) TEM image and (<b>c</b>) synthetic methods of modified cellulose carrier-loaded Pd-catalyst, reproduced with permission from Ref. [<a href="#B73-molecules-29-04353" class="html-bibr">73</a>]. Copyright 2020 Elsevier. (<b>d</b>) The surface electronic effect induced by EDA and (<b>e</b>,<b>f</b>) mechanism of catalytic selectivity of EDA-Pt NWs, reproduced with permission from Ref. [<a href="#B74-molecules-29-04353" class="html-bibr">74</a>]. Copyright 2016 Springer Nature.</p>
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<p>Structures of (<b>a</b>) DANTA and (<b>b</b>) PDADMAC, and (<b>c</b>) Layer-by-layer assembly of the RuCNT, reproduced with permission from Ref. [<a href="#B80-molecules-29-04353" class="html-bibr">80</a>]. Copyright 2015 The Royal Society of Chemistry. (<b>d</b>) Catalytic process and (<b>e</b>) proposed mechanism of semi-hydrogenation of nitroarenes catalyzed by Ir@PS, reproduced with permission from Ref. [<a href="#B84-molecules-29-04353" class="html-bibr">84</a>]. Copyright 2020 Britannica.</p>
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<p>(<b>a</b>) Synthesis and composition of PIIL-stabilized ruthenium nanoparticles, reproduced with permission from Ref. [<a href="#B85-molecules-29-04353" class="html-bibr">85</a>]. Copyright 2022 Elsevier. (<b>b</b>) Composition of polymers and schematic diagram of PEG and PIILP-stabilized gold nanoparticles, reproduced with permission from Ref. [<a href="#B86-molecules-29-04353" class="html-bibr">86</a>]. Copyright 2019 American Chemical Society.</p>
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<p>(<b>a</b>) TEM image. HRTEM of (<b>b</b>) TiO<sub>2</sub> and (<b>c</b>) Ag nanoparticle. (<b>d</b>) SAED pattern of mesoporous 4% Ag/MTA catalyst, the red curve can be attributed to the rutile phase of TiO<sub>2</sub>, while the blue mark can be labelled as the (200) and (311) reflections of cubic Ag. (<b>e</b>) Selective reduction of Ag/MTA catalyst to aniline and PHAs. (<b>f</b>) Chemoselective reduction of nitroarenes into amines and PHAs. Reproduced with permission from Ref. [<a href="#B87-molecules-29-04353" class="html-bibr">87</a>]. Copyright 2016 Multidisciplinary Digital Publishing Institute.</p>
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<p>(<b>a</b>,<b>b</b>) Schematic representation for the formation of -OH-modified PCN under hydrothermal conditions. (<b>c</b>) Photocatalytic activity for the selective reduction of nitrobenzene. (<b>d</b>) Analysis of the reaction mechanism. (<b>e</b>) Mechanism for the hydrogenation of nitrobenzene over the PCN-160 surface. Reproduced with permission from Ref. [<a href="#B97-molecules-29-04353" class="html-bibr">97</a>]. Copyright 2021 The Royal Society of Chemistry.</p>
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<p>Proposed bioreaction pathways for the controllable reduction of nitroarene compounds to the corresponding PHAs. Reproduced with permission from Ref. [<a href="#B102-molecules-29-04353" class="html-bibr">102</a>]. Copyright 2014 The Royal Society of Chemistry.</p>
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<p>Synthesis methods and applications of PHAs.</p>
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<p>Synthesis strategies for hydroxylamine.</p>
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<p>Mechanism of action of different reducing agents. (<b>a</b>) (i) The combination of catalyst and N<sub>2</sub>H<sub>4</sub>, (ii–iv) nitrogen and hydrogen in N<sub>2</sub>H<sub>4</sub> undergo heterolysis, (v) hydrogenation of Nitrobenzene. Reproduced with permission from Ref. [<a href="#B38-molecules-29-04353" class="html-bibr">38</a>]. Copyright 2024 Elsevier. (<b>b</b>) The reaction mechanism of sodium borohydride driven platinum catalyzed reduction of nitro compounds. Reproduced with permission from Ref. [<a href="#B40-molecules-29-04353" class="html-bibr">40</a>]. Copyright 2016 Wiley-VCH. (<b>c</b>) Hydrogen overflow reduction mechanism on the surface of modified Pt nanoparticles. Reproduced with permission from Ref. [<a href="#B42-molecules-29-04353" class="html-bibr">42</a>]. Copyright 2023 Wiley-VCH. (<b>d</b>) The reaction pathway for the N-methylation of amines with methanol over CuCo catalysts. Reproduced with permission from Ref. [<a href="#B44-molecules-29-04353" class="html-bibr">44</a>]. Copyright 2022 The Royal Society of Chemistry.</p>
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<p>(<b>a</b>) The reaction pathways for the reduction of an aromatic nitro compound to the corresponding aniline. (<b>b</b>) The reaction pathway for the preparation of aniline derivatives by hydrogenation of nitrobenzene over Au/TiO<sub>2</sub> catalyst.</p>
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35 pages, 6364 KiB  
Article
Mapping the Influence of Olympic Games’ Urban Planning on the Land Surface Temperatures: An Estimation Using Landsat Series and Google Earth Engine
by Joan-Cristian Padró, Valerio Della Sala, Marc Castelló-Bueno and Rafael Vicente-Salar
Remote Sens. 2024, 16(18), 3405; https://doi.org/10.3390/rs16183405 - 13 Sep 2024
Viewed by 326
Abstract
The Olympic Games are a sporting event and a catalyst for urban development in their host city. In this study, we utilized remote sensing and GIS techniques to examine the impact of the Olympic infrastructure on the surface temperature of urban areas. Using [...] Read more.
The Olympic Games are a sporting event and a catalyst for urban development in their host city. In this study, we utilized remote sensing and GIS techniques to examine the impact of the Olympic infrastructure on the surface temperature of urban areas. Using Landsat Series Collection 2 Tier 1 Level 2 data and cloud computing provided by Google Earth Engine (GEE), this study examines the effects of various forms of Olympic Games facility urban planning in different historical moments and location typologies, as follows: monocentric, polycentric, peripheric and clustered Olympic ring. The GEE code applies to the Olympic Games that occurred from Paris 2024 to Montreal 1976. However, this paper focuses specifically on the representative cases of Paris 2024, Tokyo 2020, Rio 2016, Beijing 2008, Sydney 2000, Barcelona 1992, Seoul 1988, and Montreal 1976. The study is not only concerned with obtaining absolute land surface temperatures (LST), but rather the relative influence of mega-event infrastructures on mitigating or increasing the urban heat. As such, the locally normalized land surface temperature (NLST) was utilized for this purpose. In some cities (Paris, Tokyo, Beijing, and Barcelona), it has been determined that Olympic planning has resulted in the development of green spaces, creating “green spots” that contribute to lower-than-average temperatures. However, it should be noted that there is a significant variation in temperature within intensely built-up areas, such as Olympic villages and the surrounding areas of the Olympic stadium, which can become “hotspots.” Therefore, it is important to acknowledge that different planning typologies of Olympic infrastructure can have varying impacts on city heat islands, with the polycentric and clustered Olympic ring typologies displaying a mitigating effect. This research contributes to a cloud computing method that can be updated for future Olympic Games or adapted for other mega-events and utilizes a widely available remote sensing data source to study a specific urban planning context. Full article
(This article belongs to the Special Issue Urban Planning Supported by Remote Sensing Technology II)
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<p>Location of the Olympic Game cities from 1972 to 2024, which are included in the Google Earth Engine code. The cities used as examples in this paper, representing four Olympic urban planning patterns, are highlighted in yellow. Source: Author’s own elaboration based on data from Open Street Map (@OpenStreetMap contributors) and International Olympic Committee (IOC) information [<a href="#B59-remotesensing-16-03405" class="html-bibr">59</a>].</p>
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<p>Area of interest (city AOI) of the eight cities analysed (red outline), and its corresponding area of interest (Olympic AOI) of the Olympic facilities (yellow outline). (<b>a</b>) In the Paris case, the city AOI is defined by the Ille de France administrative boundaries. (<b>b</b>) In the Tokyo case, the city AOI is defined by some municipalities of the Tokyo Metropolitan Area administrative boundaries. (<b>c</b>) In the Rio case, the city AOI is defined by the Rio de Janeiro Municipality administrative boundaries. (<b>d</b>) In the Beijing case, the city AOI is defined by Beijing’s central urban area. (<b>e</b>) In the Sydney case, the city AOI is defined by some municipalities of the North South Wales administrative boundaries. (<b>f</b>) In the Barcelona case, the city AOI is defined by the administrative boundaries of Barcelonès. (<b>g</b>) In the Seoul case, the city AOI is defined by Keijo Teukbyeolsi administrative boundaries. (<b>h</b>) In the Montreal case, the city AOI is defined by the Champlain, Communauté Urbaine de Montréal and Laval administrative boundaries.</p>
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<p>Overall methodology and processing chain.</p>
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<p>Area of interest (city AOI) of the eight cities analysed (red outline), and the corresponding areas of interest (Olympic AOI) of the Olympic facilities (yellow outline). (<b>a</b>) In the Paris case, the city AOI is defined by the Ille de France administrative boundaries and the Olympic AOI is clustered. (<b>b</b>) In the Tokyo case, the city AOI is defined by some municipalities of the Tokyo Metropolitan Area administrative boundaries and the Olympic AOI is polycentric. (<b>c</b>) In the Rio case, the city AOI is defined by the Rio de Janeiro Municipality administrative boundaries and the Olympic AOI is peripheric. (<b>d</b>) In the Beijing case, the city AOI is defined by Beijing’s central urban area and the Olympic AOI is polycentric. (<b>e</b>) In the Sydney case, the city AOI is defined by some municipalities of North South Wales administrative boundaries and the Olympic AOI is peripheric. (<b>f</b>) In the Barcelona case, the city AOI is defined by Barcelonès administrative boundaries and the Olympic AOI is clustered. (<b>g</b>) In the Seoul case, the city AOI is defined by Keijo Teukbyeolsi administrative boundaries and the Olympic AOI is monocentric. (<b>h</b>) In the Montreal case, the city AOI is defined by the Champlain, Communauté Urbaine de Montréal and Laval administrative boundaries and the Olympic AOI is monocentric.</p>
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<p>Normalized difference vegetation index (NDVI) maps created using the median synthetic image over a 5-year period, for each of the 8 cities analysed in this study. NDVI was calculated using the NIR and red bands of the synthetic image (see Equation (3)). Additionally, there is a focus on the main Olympic facilities. The real data range is [−1 to 1] but this was stretched to [−0.25 to 0.25] in all of the maps for better understanding and visualization. (<b>a</b>) In the Paris case, higher NDVI levels are in the periphery, but some Olympic facilities (i.e. Champs-de-Mars) take advantage of inner green areas. (<b>b</b>) In the Tokyo case, there are sparse but important green spaces in the central area. (<b>c</b>) In the Rio case, there are elevated NDVI levels for the entire urban area, but not in the main Olympic facilities. (<b>d</b>) In the Beijing case, the central urban area has sparse green spaces, with overall moderate NDVI levels, where Olympic facilities where placed. (<b>e</b>) In the Sydney case, elevated NDVI levels suggest that their urban area has a considerable amount of green space, including some parts pf the Olympic Park. (<b>f</b>) In the Barcelona case, sparse green spaces can be found, highlighting Montjuïc Olympic ring area. (<b>g</b>) In the Seoul case, higher NDVI levels are located in the north and the south periphery, not where the Olympic Park was placed. (<b>h</b>) In the Montreal case, the overall urban area presents high NDVI levels, and some of the Olympic Park area was also located in a green area.</p>
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<p>Normalized difference built-up index (NDBI) maps created using the median synthetic image over a 5-year period, for each of the 8 cities analysed in this study. NDBI was calculated using the NIR and SWIR1 bands of the synthetic image (see Equation (4)). Additionally, there is a focus on the main Olympic facilities. The real data range is [−1 to 1] but this was stretched to [−0.25 to 0.25] in all the maps for better understanding and visualization. (<b>a</b>) In the Paris case, radial urban configuration shows a dense urbanised centre with high NDBI levels, such as the Stade de France. (<b>b</b>) In the Tokyo case, the area is densely urbanised, such as the Tokyo Dome complex, but with interstitial green spaces. (<b>c</b>) In the Rio case, there are several densely urbanised focuses with high NDBI levels, such as the Barra Olímpica complex, limited by densely vegetated areas. (<b>d</b>) In the Beijing case, the concentric pattern leads to a densely urbanised city with high NDBI levels, such as the National Stadium. (<b>e</b>) In the Sydney case, the extensive urbanization sprawl is combined with green spaces, such as the Olympic Park. (<b>f</b>) In the Barcelona case, the gridded configuration shows urban continuity and density with very high NDBI levels, such as the Olympic Village. (<b>g</b>) In the Seoul case, the urbanisation is dense around the Han River, with generalized high NDBI levels, such as the Jasmil Sports Complex. (<b>h</b>) In the Montreal case, the gridded pattern presents dense build-up areas combined with inner green spaces, such as the Olympic Park and the adjacent Botanical Garden.</p>
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<p>Normalized land surface temperature (NLST) maps created using the median synthetic image over a 5-year period, for each of the 8 cities analysed in this study. NLST was calculated using the thermal band of the synthetic image and the minimum and maximum LST values in each city (see Equation (4)). Additionally, there was a focus on the main Olympic facilities. The transect used to calculate the thermal profile of the NLST in each city is included. (<b>a</b>) In the Paris case, the relative high temperature focuses are in the central, north and south areas, also some Olympic facilities such as the Stade de France. (<b>b</b>) In the Tokyo case, the relative high temperature focuses are on the port and around the centre of the SUHI, while Olympic facilities are relative lower temperature zones. (<b>c</b>) In the Rio case, the relative low temperature focuses of the forested areas can be seen in the centre of the AOI, and Olympic venues are acting as relative hotspots. (<b>d</b>) In the Beijing case, the relative high temperature focuses are on the south-west, south and east areas, locating the Olympic facilities in relative lower temperature areas. (<b>e</b>) In the Sydney case, the Olympic venues act as hotspots in relation with the surroundings. (<b>f</b>) In the Barcelona case, the Olympic ring is a relative green spot in comparison with the urban area. (<b>g</b>) In the Seoul case, the Olympic facilities are acting as relative high temperature areas in the SUHI. (<b>h</b>) In the Montreal case, the location of the Stade Olympique is part of the relative higher temperature areas.</p>
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<p>Transects created using the NSLT, the NDVI and the NDBI images. A segment was digitized that crossed the city and the Olympic facilities to obtain the thermal profile from the NLST. Additionally, to compare results, the NDVI and the NDBI profiles were added. This was undertaken with the Profile Tool v.4.2.6 QGIS plugin, which essentially intersects the segment with the target raster, and extracts the value of the overlapped pixels. The result is a table with values that can be plotted in the GIS v.3.32 software or exported to another software to edit the graph. (<b>a</b>) In the Paris case, there is a peak in the Stade de France NLST transect graph, indicating a hotspot in this location in relation to the Paris UHI. (<b>b</b>) In the Tokyo case, the thermal peak is located over the Stadium and the Dome. (<b>c</b>) In the Rio case, the thermal peak is located over Barra Olímpica and a secondary peak is found over Maracaná. (<b>d</b>) In the Beijing case, the hottest location is the Beijing National Stadium. (<b>e</b>) In the Sydney case, the extensive and low-density neighbourhoods, with many green spaces, contrasts with the Olympic Stadium and the central and dense downtown, where the thermal peaks are located. (<b>f</b>) In the Barcelona case, the highest surface temperature is in the industrial area, and the Olympic Ring has low relative temperatures due to its vegetated park areas. (<b>g</b>) In the Seoul case, the Han River presents the lowest relative surface temperatures, with the higher temperatures located on dense urban areas and over the Olympic Stadium. (<b>h</b>) In the Montreal case, the higher relative surface temperatures are found on the dense residential areas, and there is observed a peak just over the Olympic Park.</p>
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<p>Boxplots relating the normalized land surface temperature (NLST) within each urban area and within its Olympic facilities. (<b>a</b>) In the Paris case, the boxplot indicates that the Olympic facilities contribute to a slight increase in the relative LST in Paris’s urban area. (<b>b</b>) In the Tokyo case, the boxplot indicates a strong contribution of the Olympic facilities to reducing the overall LST in the Tokyo urban area. (<b>c</b>) In the Rio case, boxplot indicates that the Olympic facilities contribute to increase the overall SUHI LST. (<b>d</b>) In the Beijing case, the boxplot shows a median and average LST lower in the Olympic facilities, thus a strong contribution to the reduced overall LST in the Beijing urban area. (<b>e</b>) In the Sydney case, the NLST median and average values within the Olympic area are much higher than in the overall urban area; thus, the Olympic facilities contribute to the overall increase in LST of the resulting urban area after the games. (<b>f</b>) In the Barcelona case, the median and average LST is lower in the Olympic facilities, which significantly contributes to the overall reduction of LST in the urban area of Barcelona. (<b>g</b>) In the Seoul case, the boxplot suggest that the Olympic facilities have led to a relative rise of LST in the Seoul urban area. (<b>h</b>) In the Montreal case, the average and median values, as well as the higher position of the 1st and 3rd quartile, suggest that the Olympic venues have contributed to an overall relative increase of the LST in the resulting Montreal urban area after the games.</p>
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<p>Linear simple regressions relating the LST and the NLST pixels overlapped by the thermal transect defined in each city. The LST(K) and the NLST are expected to perfectly correlate in a simple linear regression because they are simply converted using the scaling method in all the cases (<b>a</b>–<b>h</b>) (see <a href="#sec2dot3dot1-remotesensing-16-03405" class="html-sec">Section 2.3.1</a>).</p>
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20 pages, 7552 KiB  
Review
Photocatalysis as an Alternative for the Remediation of Wastewater: A Scientometric Review
by Jhoan Mauricio Moreno-Vargas, Laura Maria Echeverry-Cardona, Darwin Augusto Torres-Ceron, Sebastian Amaya-Roncancio, Elisabeth Restrepo-Parra and Kevin Jair Castillo-Delgado
ChemEngineering 2024, 8(5), 95; https://doi.org/10.3390/chemengineering8050095 - 13 Sep 2024
Viewed by 230
Abstract
The objective of this study is to map, describe, and identify “water treatment using catalysts and/or nanomaterials” and their derivable aspects. A comprehensive search was conducted in academic databases such as WoS and Scopus, following the PRISMA methodology, to identify relevant studies published [...] Read more.
The objective of this study is to map, describe, and identify “water treatment using catalysts and/or nanomaterials” and their derivable aspects. A comprehensive search was conducted in academic databases such as WoS and Scopus, following the PRISMA methodology, to identify relevant studies published between 2010 and 2024. Inclusion and exclusion criteria were applied to select articles that address both experimental and theoretical aspects of photocatalysis in wastewater treatment. The methodology is developed through exploratory data analysis and the use of the Tree of Science algorithm. The first results indicate the roots, in which it is possible to gain knowledge of the environment for the implementation of a photoreactor it uses as a photocatalyst agent. A total of 94 relevant articles were identified. The results show that most studies focus on the degradation of organic pollutants using TiO2 as a photocatalyst. Additionally, there has been a significant increase in the number of publications and citations in recent years, indicating growing interest in this field. Then, in the trunk, some more solid ideas in terms of basic concepts, techniques and possible variations for the application of knowledge and development of future research related to the initial topic are indicated. Finally, through the leaves, new modifications and combinations of the photocatalytic materials are obtained, in search of improving their performance in terms of reduction in water contaminants. From the above, centrality in photocatalysis is identified as an alternative for water remediation using different photocatalysts. It is concluded that the total citation network contains, within the most important nodes, articles of high interest in the community, such as those authored by Zhang, Xiaofei; Nezamzadeh-Ejhieh, Alireza; or Li, Jingyi, from countries in the Middle East and the Asian continent, justified not only by the research capabilities of these countries, but also by the needs and problems that these regions face in terms of water scarcity. Future work indicates the need for and interest in improving various characteristics such as photocatalytic performance, the number of cycles that the material supports, and its reduction capacity in the presence of high concentrations of contaminants, with the intention of maximizing the benefits of its applicability in water treatment. Full article
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<p>PRISMA Flow. <b>Source</b>: authors’ construction based on Liberati et al. (2009) [<a href="#B42-ChemEngineering-08-00095" class="html-bibr">42</a>].</p>
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<p>Annual trends in publications and citations in photocatalysis for wastewater treatment. Measurement of scientific production. <b>Source:</b> authors’ construction based on AED.</p>
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<p>Collaboration between countries. <b>Source</b>: authors’ construction based on Biblioshiny and AED.</p>
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<p>Tree of Science. <b>Source:</b> authors’ construction based on AED and ToS [<a href="#B68-ChemEngineering-08-00095" class="html-bibr">68</a>,<a href="#B69-ChemEngineering-08-00095" class="html-bibr">69</a>,<a href="#B70-ChemEngineering-08-00095" class="html-bibr">70</a>,<a href="#B71-ChemEngineering-08-00095" class="html-bibr">71</a>,<a href="#B72-ChemEngineering-08-00095" class="html-bibr">72</a>,<a href="#B73-ChemEngineering-08-00095" class="html-bibr">73</a>,<a href="#B74-ChemEngineering-08-00095" class="html-bibr">74</a>,<a href="#B75-ChemEngineering-08-00095" class="html-bibr">75</a>,<a href="#B76-ChemEngineering-08-00095" class="html-bibr">76</a>].</p>
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<p>Citation network. <b>Source:</b> Authors’ construction based on Gephi and RStudio [<a href="#B74-ChemEngineering-08-00095" class="html-bibr">74</a>,<a href="#B76-ChemEngineering-08-00095" class="html-bibr">76</a>,<a href="#B89-ChemEngineering-08-00095" class="html-bibr">89</a>,<a href="#B90-ChemEngineering-08-00095" class="html-bibr">90</a>,<a href="#B92-ChemEngineering-08-00095" class="html-bibr">92</a>].</p>
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14 pages, 1318 KiB  
Article
Anaerobic Digestion of Food Waste with the Addition of Biochar Derived from Microwave Catalytic Pyrolysis of Solid Digestate
by Sofia Lucero Saucedo and Anthony Lau
Sustainability 2024, 16(18), 7997; https://doi.org/10.3390/su16187997 - 13 Sep 2024
Viewed by 471
Abstract
This study explores the potential of biochar derived from microwave-assisted catalytic pyrolysis of solid digestate as an additive to enhance the stability and performance of the anaerobic digestion process. The focus was placed on the effects of biochar dosage, pyrolysis temperature, and pyrolysis [...] Read more.
This study explores the potential of biochar derived from microwave-assisted catalytic pyrolysis of solid digestate as an additive to enhance the stability and performance of the anaerobic digestion process. The focus was placed on the effects of biochar dosage, pyrolysis temperature, and pyrolysis catalyst on methane production. Biochemical methane potential (BMP) tests using synthetic food waste as the substrate revealed a dosage-dependent relationship with specific methane yield (SMY). At a low biochar dosage of 0.1 g/g total solids (TS), improvement in methane (CH4) production was marginal, whereas a high dosage of 0.6 g/g TS increased CH4 content by at least 10% and improved yield by 35–52%. ANOVA analysis indicated that biochar dosage level significantly influenced CH4 yield, while pyrolysis temperature (400 °C vs. 500 °C) and catalyst (20 wt% K3PO4 vs. 10 wt% K3PO4/10 wt% clinoptilolite) did not lead to significant differences in CH4 yield between the treatments. Correlation analysis results suggested that biochar’s most impactful properties on methane yield would be dosage-adjusted specific surface area (or total surface area per unit volume of substrate) and aromaticity index. The findings underscore the potential of solid-digestate-derived biochar as a beneficial additive for anaerobic digestion and hence the sustainability of food waste management system. Full article
(This article belongs to the Section Pollution Prevention, Mitigation and Sustainability)
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<p>Schematic diagram of experimental setup. Created with BioRender.com.</p>
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<p>Methane generation profiles for the experimental treatments: (<b>a</b>) with a low biochar dosage of 0.1 g/g TS; (<b>b</b>) with a high biochar dosage of 0.6 g/g TS as compared to the control.</p>
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<p>Comparison of specific methane yield (SMY) among the experimental treatments.</p>
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11 pages, 1981 KiB  
Article
Continuous Flow Synthesis of Furfuryl Ethers over Pd/C Catalysts via Reductive Etherification of Furfural in Ethanol
by Ayoub Hassine, Anas Iben Ayad, Aïssa Ould Dris, Denis Luart and Erwann Guénin
Catalysts 2024, 14(9), 617; https://doi.org/10.3390/catal14090617 - 13 Sep 2024
Viewed by 373
Abstract
Furfural has become one of the most promising building blocks directly derived from biomass. It can be transformed into numerous important biobased chemicals. Among them, furfuryl ethers such as furfuryl ethyl ether (FEE) and tetrahydrofurfuryl ethyl ether (THFEE) are considered to be attractive [...] Read more.
Furfural has become one of the most promising building blocks directly derived from biomass. It can be transformed into numerous important biobased chemicals. Among them, furfuryl ethers such as furfuryl ethyl ether (FEE) and tetrahydrofurfuryl ethyl ether (THFEE) are considered to be attractive derivatives, notably as fuel components, due to their high stability and high octane numbers. Therefore, the production of furfuryl ethers from furfural via a hydrogenation route is an important academic and industrial challenge and requires the deployment of new catalytic processes under green and competitive reaction conditions. The existing processes are based on a two-step process combining hydrogenation and reaction with a strong Bronsted acid catalyst in batch conditions. For the first time, a continuous flow one-step process has been elaborated for the conversion of furfural directly into furfuryl ethers based on reductive etherification. The present work explores the catalytic performance in a continuous flow of commercial palladium catalysts supported on activated carbon for the catalytic reductive etherification of furfural with ethanol in the presence of trifluoroacetic acid. The chemical and engineering aspects, such as the mechanisms and reaction conditions, will be discussed. Full article
(This article belongs to the Special Issue Industrial Applications of High-Value Added Biomass Conversion)
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<p>Conversion and product yield over 2 h continuous flow hydrogenation of furfural (0.2 M) in ethanol at 80 °C and 50 Bar H<sub>2</sub> pressure, with a flow rate of 0.5 mL min<sup>−1</sup> using 300 mg of Pd/C (5%) (<b>a</b>) without, and (<b>b</b>) with TFA.</p>
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<p>Screenings of the TFA Loadings. Reaction conditions: 13 mmol FF, 70 mL of ethanol, 25 °C, 90 min.</p>
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<p>TFA loading effect on the yield of product distribution at 90 min from the stream. Reaction conditions: 14 mmol FF, 70 mL of ethanol, 70 °C, and 50 Bar H<sub>2</sub> pressure, with a flow rate of 0.5 mL min<sup>−1</sup> using 300 mg of 5% Pd/C.</p>
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<p>The effect of different hydrogen pressures on the THFEE yield. Reaction conditions: 14 mmol FF, 70 mL of ethanol, 70 °C, with a flow rate of 0.5 mL min<sup>−1</sup> using 300 mg of 5% Pd/C, 30 min on stream.</p>
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<p>Catalyst stability over 4 h. Reaction conditions: furfural (4 mmol) and DOF (10 mmol) with TFA 0.01% in ethanol (70 mL); 70 °C; 15 Bar H<sub>2</sub>; and 100 mg catalyst of 1% Pd/C.</p>
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<p>Reductive etherification pathway of furfural with ethanol under continuous flow condition using Pd/C catalysts.</p>
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<p>Acetalization of furfural using a large excess of ethanol.</p>
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30 pages, 6114 KiB  
Article
Roles of Catalysts and Feedstock in Optimizing the Performance of Heavy Fraction Conversion Processes: Fluid Catalytic Cracking and Ebullated Bed Vacuum Residue Hydrocracking
by Dicho Stratiev, Ivelina Shishkova, Georgi Argirov, Rosen Dinkov, Mihail Ivanov, Sotir Sotirov, Evdokia Sotirova, Veselina Bureva, Svetoslav Nenov, Krassimir Atanassov, Denis Stratiev and Svetlin Vasilev
Catalysts 2024, 14(9), 616; https://doi.org/10.3390/catal14090616 - 12 Sep 2024
Viewed by 208
Abstract
Petroleum refining has been, is still, and is expected to remain in the next decades the main source of energy required to drive transport for mankind. The demand for automotive and aviation fuels has urged refiners to search for ways to extract more [...] Read more.
Petroleum refining has been, is still, and is expected to remain in the next decades the main source of energy required to drive transport for mankind. The demand for automotive and aviation fuels has urged refiners to search for ways to extract more light oil products per barrel of crude oil. The heavy oil conversion processes of ebullated bed vacuum residue hydrocracking (EBVRHC) and fluid catalytic cracking (FCC) can assist refiners in their aim to produce more transportation fuels and feeds for petrochemistry from a ton of petroleum. However, a good understanding of the roles of feed quality and catalyst characteristics is needed to optimize the performance of both heavy oil conversion processes. Three knowledge discovery database techniques—intercriteria and regression analyses, and artificial neural networks—were used to evaluate the performance of commercial FCC and EBVRHC in processing 19 different heavy oils. Seven diverse FCC catalysts were assessed using a cascade and parallel fresh catalyst addition system in an EBVRHC unit. It was found that the vacuum residue conversion in the EBVRHC depended on feed reactivity, which, calculated on the basis of pilot plant tests, varied by 16.4%; the content of vacuum residue (VR) in the mixed EBVRHC unit feed (each 10% fluctuation in VR content leads to an alteration in VR conversion of 1.6%); the reaction temperature (a 1 °C deviation in reaction temperature is associated with a 0.8% shift in VR conversion); and the liquid hourly space velocity (0.01 h-1 change of LHSV leads to 0.85% conversion alteration). The vacuum gas oil conversion in the FCC unit was determined to correlate with feed crackability, which, calculated on the basis of pilot plant tests, varied by 8.2%, and the catalyst ΔCoke (each 0.03% ΔCoke increase reduces FCC conversion by 1%), which was unveiled to depend on FCC feed density and equilibrium FCC micro-activity. The developed correlations can be used to optimize the performance of FCC and EBVRHC units by selecting the appropriate feed slate and catalyst. Full article
(This article belongs to the Section Catalytic Reaction Engineering)
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<p>Variation of the observed H-Oil net conversion and the calculated one using plug flow reactor model with an activation energy of 215 kJ/mol, a reaction order of 1.59, and collision factor of <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>k</mi> </mrow> <mrow> <mn>0</mn> </mrow> </msub> <mo>=</mo> <mn>4.42875</mn> <mo>×</mo> <msup> <mrow> <mn>10</mn> </mrow> <mrow> <mn>15</mn> </mrow> </msup> </mrow> </semantics></math>.</p>
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<p>Agreement between observed and estimated by Equation (1) vacuum residue hydrocracking conversion. A, B, C, D, E, and F are six diverse vacuum residues hydrocracked at the same operating conditions as communicated in [<a href="#B8-catalysts-14-00616" class="html-bibr">8</a>].</p>
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<p>Estimated by Equation (1) conversion at the same hydrocracking operating conditions and subtracted from the Urals vacuum residue conversion (base case) in wt.%.</p>
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<p>Variation of conversion, product yields, and sediment content of the hydrocracked atmospheric residue with reaction temperature enhancement during hydrocracking of the vacuum residue blend 70% Urals/30% Basrah Med at constant LHSV in the laboratory pilot plant (see the flow diagram of the laboratory hydrocracking plant in <a href="#app1-catalysts-14-00616" class="html-app">Figure S4</a>).</p>
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<p>Neural network training performance for prediction of commercial H-Oil hydrocracker vacuum residue net conversion.</p>
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<p>ANN predicted versus observed vacuum residue net conversion in the commercial H-Oil hydrocracker for training, validation, testing and overall dataset.</p>
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<p>Variation of sediment content in hydrocracked atmospheric residue (AR_TSE), weight average bed temperature (WABT) of both reactors, and liquid hourly space velocity (LHSV) at the end of the first H-Oil cycle (2015–2018) and the beginning of the second cycle (2018–2021).</p>
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<p>Variation of sediment content in hydrocracked atmospheric residue (AR_TSE), weight average bed temperature (WABT) of both reactors, and liquid hourly space velocity (LHSV) at the beginning of the third H-Oil cycle (2021–2025).</p>
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<p>Photographs of the catalyst unloaded from the first ebullated bed reactor (the <b>left</b>-hand side picture) and from the second ebullated bed reactor (the <b>right</b>-hand side picture).</p>
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<p>Metal content in the first reactor spent catalyst samples and black powder samples.</p>
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<p>Ratios <math display="inline"><semantics> <mrow> <mstyle scriptlevel="0" displaystyle="true"> <mfrac> <mrow> <mi>V</mi> </mrow> <mrow> <mi>N</mi> <mi>i</mi> </mrow> </mfrac> </mstyle> </mrow> </semantics></math>, <math display="inline"><semantics> <mrow> <mstyle scriptlevel="0" displaystyle="true"> <mfrac> <mrow> <mi>V</mi> </mrow> <mrow> <mi>F</mi> <mi>e</mi> </mrow> </mfrac> </mstyle> </mrow> </semantics></math> in the first reactor spent catalyst samples, black powder samples, and H-Oil feed.</p>
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<p>SEM photograph of spent catalyst surface of catalyst from the first reactor (<b>a</b>), and from the second reactor (<b>b</b>).</p>
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<p>SEM photograph of second reactor spent catalyst showing the presence of thick not homogeneous layer on the outer catalyst particle surface.</p>
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<p>Crackability estimated by Equation (3) of the 19 vacuum gas oils processed in the commercial LNB FCC unit.</p>
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<p>FCC feed conversion alteration with catalyst-to-oil ratio variation at two different reactor temperatures: 526 and 550 °C.</p>
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<p>Neural network training performance for prediction of commercial FCC vacuum gas oil feed conversion. The green circle indicates the point where the minimum mean squared error is obtained.</p>
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<p>ANN predicted versus observed VGO conversion in the commercial FCC unit for training, validation, testing, and overall dataset.</p>
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18 pages, 9854 KiB  
Article
Synthesis and Antimicrobial Activity of (E)-1-Aryl-2-(1H-tetrazol-5-yl)acrylonitrile Derivatives via [3+2] Cycloaddition Reaction Using Reusable Heterogeneous Nanocatalyst under Microwave Irradiation
by Ayashkanta Nanda, Navneet Kaur, Manvinder Kaur, Fohad Mabood Husain, Haesook Han, Pradip K. Bhowmik and Harvinder Singh Sohal
Molecules 2024, 29(18), 4339; https://doi.org/10.3390/molecules29184339 - 12 Sep 2024
Viewed by 249
Abstract
The magnetically recoverable heterogeneous Fe2O3@cellulose@Mn nanocomposite was synthesized by a stepwise fabrication of Mn nanoparticles on cellulose-modified magnetic Fe2O3 nanocomposites, and the morphology of the nanocomposite was characterized through advanced spectroscopic techniques. This nanocomposite was investigated [...] Read more.
The magnetically recoverable heterogeneous Fe2O3@cellulose@Mn nanocomposite was synthesized by a stepwise fabrication of Mn nanoparticles on cellulose-modified magnetic Fe2O3 nanocomposites, and the morphology of the nanocomposite was characterized through advanced spectroscopic techniques. This nanocomposite was investigated as a heterogeneous catalyst for the synthesis of medicinally important tetrazole derivatives through Knoevenagel condensation between aromatic/heteroaromatic aldehyde and malononitrile followed by [3+2] cycloaddition reaction with sodium azide. Thirteen potent (E)-1-aryl-2-(1H-tetrazol-5-yl)acrylonitrile derivatives are reported in this paper with very high yields (up to 98%) and with excellent purity (as crystals) in a very short period (3 min @ 120 W) using microwave irradiation. The present procedure offers several advantages over recent protocols, including minimal catalyst loading, quick reaction time, and the utilization of an eco-friendly solvent. Furthermore, the synthesized (E)-1-aryl-2-(1H-tetrazol-5-yl)acrylonitrile derivatives (4b, 4c, and 4m) are shown to have excellent resistance against various fungal strains over bacterial strains as compared to the standard drugs Cefixime (4 μg/mL) and Fluconazole (2 μg/mL). Full article
(This article belongs to the Special Issue Synthesis of Bioactive Compounds: Volume II)
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Graphical abstract

Graphical abstract
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<p>FT-IR characterization of Fe<sub>2</sub>O<sub>3</sub>, Fe<sub>2</sub>O<sub>3</sub>@cellulose, and Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn nanocomposites.</p>
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<p>SEM images of (<b>a</b>–<b>c</b>) cellulose, (<b>d</b>–<b>f</b>) Fe<sub>2</sub>O<sub>3</sub>, and (<b>g</b>–<b>i</b>) Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn.</p>
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<p>EDS characterization of (<b>a</b>) Fe<sub>2</sub>O<sub>3</sub> and (<b>b</b>) Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn.</p>
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<p>XRD characterization of Fe<sub>2</sub>O<sub>3</sub> and Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn nanocomposites.</p>
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<p>VSM characterization of Fe<sub>2</sub>O<sub>3</sub> and Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn nanocomposites.</p>
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<p>Proposed mechanism for the synthesis of (<span class="html-italic">E</span>)-1-aryl-2-(1H-tetrazol-5-yl)acrylonitrile derivatives <b>4a</b>–<b>m</b> using Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn nanocatalyst.</p>
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<p>Graphical illustration of the synthesis of Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn nanocatalyst.</p>
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<p>Synthesis of (<span class="html-italic">E</span>)-1-aryl-2-(1H-tetrazol-5-yl)acrylonitrile derivatives <b>4a</b>–<b>m</b> using Fe<sub>2</sub>O<sub>3</sub>@cellulose@Mn under MW irradiations.</p>
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14 pages, 240 KiB  
Article
Virtuality and Solidarity: Exploring the New Frontiers of Social Love in the Sign of Collective Wellbeing
by Luisa Nardi
Soc. Sci. 2024, 13(9), 485; https://doi.org/10.3390/socsci13090485 - 12 Sep 2024
Viewed by 299
Abstract
This paper aims to investigate the concept of love and solidarity in human relationships, especially in their manifestation within virtual communities. Solidarity, understood as the highest feeling of connection between individuals, finds new forms of expression in the digital age, where physical distances [...] Read more.
This paper aims to investigate the concept of love and solidarity in human relationships, especially in their manifestation within virtual communities. Solidarity, understood as the highest feeling of connection between individuals, finds new forms of expression in the digital age, where physical distances are overcome by the ability to communicate and share experiences in an immediate and simplified way. The aim is to analyze the renewed sociological perspective on how to explore human interactions as a practical implication of the transition from physical to digital space, which, in spite of divergences, does not seem to reduce the quality of social ties but rather offers new ways of connection and interaction. Indeed, digital technologies can positively influence social dynamics by fostering the construction of community networks that act as catalysts for collective intelligence and knowledge sharing in the pursuit of collective wellbeing. Full article
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