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Search Results (2,748)

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Keywords = zeolite

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26 pages, 6574 KiB  
Review
Research Progress in Microporous Materials for Selective Adsorption and Separation of Methane from Low-Grade Gas
by Dongrui Su, Panpan Chen, Cunlei Li, Yongfei Yan, Ranlei Zhao, Qingyou Yue and Yupeng Qiao
Molecules 2024, 29(18), 4404; https://doi.org/10.3390/molecules29184404 - 16 Sep 2024
Abstract
Given that methane (CH4) and nitrogen (N2) have similar properties, achieving high-purity enrichment of CH4 from nitrogen-rich low-grade gas is extremely challenging and is of great significance for sustainable development in energy and the environment. This paper reviews [...] Read more.
Given that methane (CH4) and nitrogen (N2) have similar properties, achieving high-purity enrichment of CH4 from nitrogen-rich low-grade gas is extremely challenging and is of great significance for sustainable development in energy and the environment. This paper reviews the research progress on carbon-based materials, zeolites, and MOFs as adsorbent materials for CH4/N2 separation. It focuses on the relationship between the composition, pore size, surface chemistry of the adsorbents, CH4/N2 selectivity, and CH4 adsorption capacity. The paper also highlights that controlling pore size and atomic-scale composition and optimizing these features for the best match are key directions for the development of new adsorbents. Additionally, it points out that MOFs, which combine the advantages of carbon-based adsorbents and zeolites, are likely to become the most promising adsorbent materials for efficient CH4/N2 separation. Full article
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Figure 1
<p>The schematic diagram of the six-bed VPSA process [<a href="#B24-molecules-29-04404" class="html-bibr">24</a>].</p>
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<p>Schematic flow diagram of the eight-column VPSA process with SMB mode. Different colors represent changes in different state parameters (pressure, gas composition, etc.), and dotted lines represent the transition of the three areas [<a href="#B26-molecules-29-04404" class="html-bibr">26</a>].</p>
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<p>Illustration of a low-pressure foaming process by bubble growth in tar pitch with and without coal particles as additives [<a href="#B33-molecules-29-04404" class="html-bibr">33</a>].</p>
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<p>Schematic illustration of the synthesis of enhanced N-doped porous carbon [<a href="#B36-molecules-29-04404" class="html-bibr">36</a>].</p>
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<p>3D-printed activated carbon monolith [<a href="#B51-molecules-29-04404" class="html-bibr">51</a>].</p>
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<p>(<b>a</b>) Schematic of the synthesis strategy for PFs. (<b>b</b>–<b>d</b>) SEM image of PF-Ni-1, PF-Co-1, and PF-Mn-1. (<b>e</b>) The recording of Zeta potential and pH changes during the synthesis process. (<b>f</b>) FT-IR spectra of PF-Co-1, Asn, and BC. (<b>g</b>) Photograph of the as-obtained polymeric aerogels [<a href="#B45-molecules-29-04404" class="html-bibr">45</a>].</p>
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<p>Schematic of Ba-ETS-4 structural changes during heat treatment process. Titanium atoms are presented in green. Silicon atoms are presented in blue. Oxygen and chlorine are presented in red and black, respectively [<a href="#B70-molecules-29-04404" class="html-bibr">70</a>].</p>
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<p>N<sub>2</sub> and CH<sub>4</sub> diffusion passes in ZSM-25: (<b>a</b>) 3D view of the ZSM-25 unit cell and (<b>b</b>) four unique channels connected through eight-membered rings as the main routes for gas diffusion consisting of four double-connected cages, namely, (1) grc-opr, (2) pau-opr, (3) phi-oto, and (4) plg-oto. The door-keeping cations are highlighted [<a href="#B82-molecules-29-04404" class="html-bibr">82</a>].</p>
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<p>Synthesis of nanosized K-Chabazite by the seed-passaging route [<a href="#B72-molecules-29-04404" class="html-bibr">72</a>].</p>
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<p>(<b>a</b>) 3D framework of MIL-120Al; (<b>b</b>,<b>c</b>) molecular size of CH<sub>4</sub> and N<sub>2</sub>; (<b>d</b>) illustration of the different kinetic effects of CH<sub>4</sub> and N<sub>2</sub> through the window of MIL-120Al. Color code: C, gray; H, white; O, red; Al, cyan; N, blue [<a href="#B91-molecules-29-04404" class="html-bibr">91</a>].</p>
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<p>The simulated distribution of adsorption density on (<b>a</b>) CAU-10-H, (<b>b</b>) MIL-160, (<b>c</b>) Al-Fum, and (<b>d</b>) MIL-53(Al) during the adsorption process (red regions for CH<sub>4</sub>, green regions for N<sub>2</sub>) [<a href="#B92-molecules-29-04404" class="html-bibr">92</a>].</p>
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<p>Crystallographic structure of UiO-66 unit cell and schematic of organic linkers of UiO-66-X materials [<a href="#B98-molecules-29-04404" class="html-bibr">98</a>].</p>
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<p>(<b>a</b>) XRD patterns of experimental and simulated Ni-Qc-5 MOF (<b>b</b>) Thermogravimetric analysis of Ni-Qc-5 MOF [<a href="#B100-molecules-29-04404" class="html-bibr">100</a>].</p>
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<p>(<b>a</b>) Chemical structure of fumaric acid ligand and Zr<sub>6</sub>(μ3-O)<sub>4</sub>(μ3-OH)<sub>4</sub> cluster in MIP-203-F. (<b>b</b>) Formate-linked Zr6-oxo cluster chain along the a-axis. (<b>c</b>) Framework structure of MIP-203-F with the hydroxyl group-divided dual triangular 1D pore. (<b>d</b>) Connolly surface of MIP-203-F with a probe radius of 1.82 A viewed along the b-axis. (<b>e</b>) Van der Waals surface of MIP-203-F viewed along the a-axis [<a href="#B103-molecules-29-04404" class="html-bibr">103</a>].</p>
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14 pages, 1968 KiB  
Article
Rice Husk as Raw Material in Synthesis of NaA (LTA) Zeolite
by Daniela Novembre, Domingo Gimeno, Lucia Marinangeli, Anna Chiara Tangari, Gianluigi Rosatelli, Michele Ciulla and Pietro di Profio
Molecules 2024, 29(18), 4396; https://doi.org/10.3390/molecules29184396 - 16 Sep 2024
Abstract
The present work deals with the hydrothermal synthesis of a Na-A (LTA) zeolite using rice husk as a starting material. The focus was on defining the most favorable conditions for the synthesis of zeolite Na-A from rice husk in order to economize on [...] Read more.
The present work deals with the hydrothermal synthesis of a Na-A (LTA) zeolite using rice husk as a starting material. The focus was on defining the most favorable conditions for the synthesis of zeolite Na-A from rice husk in order to economize on both energy (i.e., synthesis temperatures) and reaction time and to enlarge the field of the pure and isolated synthesized phase. Four sets of experiments were carried out at environmental pressure temperatures varying from 40 °C to 85 °C with a SiO2/Al2O3 ratio from 1.75 to 3.5. Optimal conditions for crystallization of the Na-A zeolite from rice husk were reached at 60 °C with a SiO2/Al2O3 ratio of 1.75. Sixty degrees Celsius represents the minimum known temperature used for the synthesis of NaA zeolite from rice husk. The products of synthesis were characterized by X-ray diffraction, scanning electron microscopy, infrared and Raman spectroscopy. The purity of the synthesized zeolite is verified here for the first time through quantitative phase analysis using the combined Rietveld and reference intensity ratio methods. Full article
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Figure 1
<p>(<b>a</b>) XRPD pattern of RHA. (<b>b</b>) IR analysis on RHA.</p>
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<p>XRPD data. (<b>a</b>) XRPD pattern of Experiment 1, (<b>b</b>) XRPD pattern of Experiment 2.</p>
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<p>XRPD data. (<b>a</b>) XRPD pattern of Experiment 3, (<b>b</b>) XRD pattern of Experiment 4.</p>
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<p>SEM images of NaA zeolite crystals for Experiment 2. (<b>a</b>) 6 h, (<b>b</b>) 8 h.</p>
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<p>SEM images of zeolite crystals for Experiment 3. (<b>a</b>) 4 h, (<b>b</b>) 8 h.</p>
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<p>SEM images of zeolite crystals for Experiment 4. (<b>a</b>) 4 h, (<b>b</b>) 8 h.</p>
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<p>Rietveld refinement plot: observed (+) and calculated profiles and difference plot for NaA zeolite (8 h, Experiment 2) and corundum NIST 676a with tick marks at the position of the Bragg peaks. From the bottom: NaA zeolite, corundum NIST 676a.</p>
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<p>IR spectrum of the sample at 8 h—Experiment 2.</p>
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<p>Raman spectra of the sample at 8 h—Experiment 2.</p>
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<p>Scheme of experimental protocol.</p>
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12 pages, 2658 KiB  
Article
Research on Modification of Oxygen-Producing Adsorbents for High-Altitude and Low-Pressure Environments
by Ye Li, Huiqing Yue, Quanli Zhang, Dumin Yan, Ziyi Li, Zhiwei Liu, Yingshu Liu, Yongyan Wang, Shifeng Wang and Xiong Yang
Inorganics 2024, 12(9), 250; https://doi.org/10.3390/inorganics12090250 - 14 Sep 2024
Viewed by 202
Abstract
In oxygen production on plateaus, pressure swing adsorption (PSA) oxygen production is currently the most commonly used oxygen production method. In plateau regions, low pressure leads to a decrease in adsorbent nitrogen–oxygen separation performance, which affects the performance of PSA oxygen production, so [...] Read more.
In oxygen production on plateaus, pressure swing adsorption (PSA) oxygen production is currently the most commonly used oxygen production method. In plateau regions, low pressure leads to a decrease in adsorbent nitrogen–oxygen separation performance, which affects the performance of PSA oxygen production, so it is particularly important to enhance adsorbent nitrogen–oxygen separation performance. In this paper, Li-LSX (lithium low-silicon aluminum X zeolite molecular sieve) adsorbents were modified using the liquid phase ion exchange method, and five kinds of modified adsorbents were obtained, namely AgLi-LSX, CaLi-LSX, ZnLi-LSX, CuLi-LSX, and FeLi-LSX, respectively. The influences of different metal ions and modification time lengths on the adsorbent nitrogen adsorption and nitrogen–oxygen separation coefficients were analyzed. Through theoretical calculations, the nitrogen and oxygen adsorption and separation performances of the modified adsorbents at different altitudes and low adsorption pressures were investigated. It is shown that the nitrogen adsorption capacity of the AgLi-LSX-1 adsorbent obtained from the modification experiment reaches 27.92 mL/g, which is 3.24 mL/g higher than that of Li-LSX; the nitrogen–oxygen separation coefficients of S1 and S2 are 19.24 and 7.54 higher, respectively; and the nitrogen–oxygen separation coefficients of S4 are 20.85 and 7.54 higher than those of Li-LSX, respectively. With the increase in altitude from 50 m to 5000 m, the nitrogen–oxygen separation coefficient of the AgLi-LSX-1 adsorbent increased rapidly from 20.85 to 57, and its nitrogen–oxygen separation coefficient S4 exceeded that of the Li-LSX adsorbent to reach 47.61 at an altitude of 4000 m. Therefore, the modified adsorbent AgLi-LSX-1 in this paper can enhance the performance of the PSA oxygen process for oxygen production in plateau applications. Full article
(This article belongs to the Special Issue Inorganic Composites for Gas Separation)
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Graphical abstract

Graphical abstract
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<p>Naming rules for modified adsorbents.</p>
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<p>Schematic diagram of the distribution of cations outside the skeleton of X-type oxygen-producing adsorbent.</p>
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<p>AgLi-LSX adsorption isotherms ((<b>a</b>–<b>d</b>) are AgLi-LSX-1, AgLi-LSX-2, AgLi-LSX-3, and AgLi-LSX-4).</p>
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<p>CaLi-LSX adsorption isotherms ((<b>a</b>–<b>d</b>) are CaLi-LSX-1, CaLi-LSX-2, CaLi-LSX-3, and CaLi-LSX-4).</p>
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<p>AgLi-LSX comparison of nitrogen and oxygen adsorption isotherms of adsorbent and Li-LSX adsorbent under high pressure ((<b>a</b>–<b>d</b>) is AgLi-LSX-1, AgLi-LSX-2, AgLi-LSX-3 and AgLi-LSX-4; BROWN suggests that the adsorption capacity of AgLi-LSX surpasses that of Li-LSX, whereas GREEN indicates the contrary).</p>
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<p>CaLi-LSX comparison of nitrogen and oxygen adsorption isotherms of adsorbent and Li-LSX adsorbent under high pressure ((<b>a</b>–<b>d</b>) is CaLi-LSX-1, CaLi-LSX-2, CaLi-LSX-3 and CaLi-LSX-4; BROWN suggests that the adsorption capacity of CaLi-LSX surpasses that of Li-LSX, whereas GREEN indicates the contrary).</p>
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<p>CaLi-LSX comparison of nitrogen and oxygen adsorption isotherms of adsorbent and Li-LSX adsorbent under high pressure ((<b>a</b>–<b>d</b>) is CaLi-LSX-1, CaLi-LSX-2, CaLi-LSX-3 and CaLi-LSX-4; BROWN suggests that the adsorption capacity of CaLi-LSX surpasses that of Li-LSX, whereas GREEN indicates the contrary).</p>
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18 pages, 6877 KiB  
Article
Performance of Zeolite-Based Soil–Geopolymer Mixtures for Geostructures under Eccentric Loading
by Alaa H. J. Al-Rkaby
Infrastructures 2024, 9(9), 160; https://doi.org/10.3390/infrastructures9090160 - 12 Sep 2024
Viewed by 232
Abstract
Although soil stabilization with cement and lime is widely used to overcome the low shear strength of soft clay, which can cause severe damage to the infrastructures founded on such soils, such binders have severe impacts on the environment in terms of increasing [...] Read more.
Although soil stabilization with cement and lime is widely used to overcome the low shear strength of soft clay, which can cause severe damage to the infrastructures founded on such soils, such binders have severe impacts on the environment in terms of increasing emissions of carbon dioxide and the consumption of energy. Therefore, it is necessary to investigate soil improvement using sustainable materials such as byproducts or natural resources as alternatives to conventional binders—cement and lime. In this study, the combination of cement kiln dust as a byproduct and zeolite was used to produce an alkali-activated matrix. The results showed that the strength increased from 124 kPa for the untreated clay to 572 kPa for clay treated with 30% activated stabilizer agent (activated cement kiln dust). Moreover, incorporating zeolite as a partial replacement of the activated cement kiln dust increased the strength drastically to 960 and 2530 kPa for zeolite ratios of 0.1 and 0.6, respectively, which then decreased sharply to 1167 and 800 kPa with further increasing zeolite/pr to 0.8 and 1.0, respectively. The soil that was improved with the activated stabilizer agents was tested under footings subjected to eccentric loading. The results of large-scale loading tests showed clear improvements in terms of increasing the bearing capacity and decreasing the tilt of the footings. Also, a reduction occurred due to the eccentricity decreasing as a result of increasing the thickness of the treated soil layer beneath the footing. Full article
(This article belongs to the Section Sustainable Infrastructures)
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Figure 1
<p>Particle size distributions of the clay, cement kiln dust, and zeolite used in this study.</p>
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<p>Materials used in this study and the performed tests.</p>
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<p>Materials used in this study and the performed tests.</p>
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<p>Stress–strain relationships of clay improved using different contents of stabilizer agent and zeolite/Pr ratios.</p>
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<p>Stress–strain relationships of clay improved using different contents of stabilizer agent and zeolite/Pr ratios.</p>
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<p>Effect of the stabilizer agent and zeolite on the peak stress of the treated clay.</p>
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<p>Effect of the zeolite/stabilizer agent on the peak stress of the treated clay.</p>
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<p>Comparison of the UCS obtained in the present study with the results obtained in previous work [<a href="#B17-infrastructures-09-00160" class="html-bibr">17</a>,<a href="#B45-infrastructures-09-00160" class="html-bibr">45</a>,<a href="#B46-infrastructures-09-00160" class="html-bibr">46</a>,<a href="#B47-infrastructures-09-00160" class="html-bibr">47</a>,<a href="#B48-infrastructures-09-00160" class="html-bibr">48</a>,<a href="#B49-infrastructures-09-00160" class="html-bibr">49</a>].</p>
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<p>Effect of eccentricity on the ultimate bearing capacity of treated clay.</p>
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<p>Effect of eccentricity on the reduction in the developed ultimate bearing capacity.</p>
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<p>Effect of eccentricity on the developed footing tilt.</p>
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<p>SEM images of untreated and treated soil.</p>
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17 pages, 8267 KiB  
Article
Performance Evaluation of a Romanian Zeolite: A Sustainable Material for Removing Ammonium Ions from Water
by Thaaer Hameed Abed, Daniela Simina Stefan, Daniela Cristina Berger, Nicolaie Cicerone Marinescu and Mircea Stefan
Sustainability 2024, 16(18), 7888; https://doi.org/10.3390/su16187888 - 10 Sep 2024
Viewed by 378
Abstract
Ammonium ion is a chemical species that is found in abundance in natural waters, whether underground or surface, but also in wastewater resulting from agricultural and industrial activities. Even if the removal of the ammonium ion from water has been studied for a [...] Read more.
Ammonium ion is a chemical species that is found in abundance in natural waters, whether underground or surface, but also in wastewater resulting from agricultural and industrial activities. Even if the removal of the ammonium ion from water has been studied for a very long time, it has been found that its removal is far from being solved. In this study, we evaluated the performance of the ammonium ion adsorption process on two adsorbents, zeolite clinoptilolite, ZR, a sustainable material (manufacturer: Zeolite Development SRL, Rupea, Brasov, Romania), and the other granular activated carbon type, Norit GAC 830 W. Zeolite ZR is found in very large deposits in Romania; it is a natural, cheap material with costs between 50 and 100 EUR/ton, compared to other adsorbents that cost over 500 EUR/ton and which can be regenerated and reused in the technological process of water treatment and purification, but also after exhaustion, as an amendment for the soil. In the first step, this paper presents the mineralogic (XRD) and structural (SEM and EDX) characterization of the ZR and the determination of the pH zero-point charge, pHZPC, for all the adsorbents. Studies were carried out in equilibrium and kinetic conditions. The efficiency of the adsorbent was investigated in different experimental conditions by varying the initial concentration, particle size, temperature, pH, ionic strength, and contact time. The mathematical models and parameters specific to the adsorption isotherms that best describe the experimental results were identified. Langmuir, Freundlich, Temkin, and Dubinin–Radushkevich mathematical models were used for comparison. The Langmuir isotherm proved to be the most appropriate to describe the adsorption of ammonium ions on all types of adsorbents used. The adsorption capacity of ammonium ions from synthetic solutions at 20 °C, pH = 6.09, for the range of initial concentrations 0–50 mg/L for Rupea zeolite is in the range of 10.46 mg/g−12.34 mg/g, and for granular activated carbon GAC W830, it is 16.64 mg/g. It was found that the adsorption capacity of the ammonium ion on both activated carbon and zeolite increases with increasing temperature and pH. Also, it was observed that as the ionic strength increases, the adsorption capacity decreases for all four adsorbents. Kinetic models were also identified that best describe the experimental processes. In this sense, pseudo-first order, pseudo-second order, intra-particle diffusion and the Elovich model were used. The results of the investigation showed that second-order kinetics governs the adsorption process on ZR, and pseudo-first order governs activated carbon. Full article
(This article belongs to the Section Sustainable Water Management)
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<p>Characteristic diffractograms for ZR.</p>
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<p>The SEM analysis for ZR at different magnifications levels: (<b>a</b>)—100 times, (<b>b</b>)—1000 times, (<b>c</b>)—10,000 times, and (<b>d</b>)—50,000 times.</p>
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<p>EDX spectrum specific to ZR.</p>
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<p>The pHz<sub>PC</sub> for adsorbants.</p>
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<p>Isotherms of adsorption of ZR and AC.</p>
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<p>Effect of temperature on adsorption capacity of ZR and AC.</p>
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<p>Effect of initial pH on adsorption capacity of ZR and AC.</p>
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<p>Effect of ionic strength on adsorption capacity of ZR and AC.</p>
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<p>Variation of ZR adsorption capacity for ammonium ion over time.</p>
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<p>Variation of AC adsorption capacity for ammonium ion over time.</p>
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16 pages, 3004 KiB  
Article
New Discovery of Natural Zeolite-Rich Tuff on the Northern Margin of the Los Frailes Caldera: A Study to Determine Its Performance as a Supplementary Cementitious Material
by Jorge L. Costafreda, Domingo A. Martín, Miguel A. Sanjuán and Jorge L. Costafreda-Velázquez
Materials 2024, 17(17), 4430; https://doi.org/10.3390/ma17174430 - 9 Sep 2024
Viewed by 279
Abstract
The release of Neogene volcanism in the southeastern part of the Iberian Peninsula produced a series of volcanic structures in the form of stratovolcanoes and calderas; however, other materials also accumulated such as large amounts of pyroclastic materials such as cinerites, ashes, and [...] Read more.
The release of Neogene volcanism in the southeastern part of the Iberian Peninsula produced a series of volcanic structures in the form of stratovolcanoes and calderas; however, other materials also accumulated such as large amounts of pyroclastic materials such as cinerites, ashes, and lapilli, which were later altered to form deposits of zeolites and bentonites. This work has focused on an area located on the northern flank of the San José-Los Escullos zeolite deposit, the only one of its kind with industrial capacity in Spain. The main objective of this research is to characterize the zeolite (SZ) of this new area from the mineral, chemical, and technical points of view and establish its possible use as a natural pozzolan. In the first stage, a study of the mineralogical and chemical composition of the selected samples was carried out using X-ray diffraction (XRD), scanning electron microscopy (SEM), X-ray fluorescence (XRF), and thermogravimetric analysis (TGA); in the second stage, chemical-qualitative and pozzolanicity technical tests were carried out at 8 and 15 days. In addition, a chemical analysis was performed using XRF on the specimens of mortars made with a standardized mixture of Portland cement (PC: 75%) and natural zeolite (SZ: 25%) at the ages of 7, 28, and 90 days. The results of the mineralogical analyses indicated that the samples are made up mainly of mordenite and subordinately by smectite, plagioclase, quartz, halloysite, illite, and muscovite. Qualitative chemical assays indicated a high percentage of reactive silica and reactive CaO and also negligible contents of insoluble residues. The results of the pozzolanicity test indicate that all the samples analyzed behave like natural pozzolans of good quality, increasing their pozzolanic reactivity from 8 to 15 days of testing. Chemical analyses of PC/SZ composite mortar specimens showed how a significant part of SiO2 and Al2O3 are released by zeolite while it absorbs a large part of the SO3 contained in the cement. The results presented in this research could be of great practical and scientific importance as they indicate the continuation of zeolitic mineralization beyond the limits of the San José-Los Escullos deposit, which would result in an increase in geological reserves and the extension of the useful life of the deposit, which is of vital importance to the local mining industry. Full article
(This article belongs to the Special Issue Functional Cement-Based Composites for Civil Engineering (Volume II))
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<p>Location of the research area.</p>
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<p>X-ray diffraction patterns of the samples of natural zeolite-rich tuff.</p>
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<p>SEM micrographs (<b>a</b>–<b>f</b>) of the analyzed samples.</p>
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<p>Behavior of the TGA curves in the samples studied.</p>
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<p>Evolution of the pozzolanic behavior of each sample analyzed at 8 and 15 days.</p>
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<p>Behavior of SiO<sub>2</sub> in the analyzed samples.</p>
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<p>Behavior of the mechanical resistance in the period of 7, 28, and 90 days of curing.</p>
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16 pages, 5825 KiB  
Article
Removal of Remazol Red Dyes Using Zeolites-Loaded Nanofibre Coated on Fabric Substrates
by Siddratul Sarah binti Mohd Hami, Nor Dalila Nor Affandi, Liliana Indrie and Ahmad Mukifza Harun
Coatings 2024, 14(9), 1155; https://doi.org/10.3390/coatings14091155 - 8 Sep 2024
Viewed by 384
Abstract
Nanofibre-based membranes have shown great potential for removing textile wastewater due to their high porosity and surface area. However, nanofibre membranes exhibit lower dye removal efficiency. Hence, this study aims to improve the dye removal performance of nanofibre membranes by incorporating zeolites. The [...] Read more.
Nanofibre-based membranes have shown great potential for removing textile wastewater due to their high porosity and surface area. However, nanofibre membranes exhibit lower dye removal efficiency. Hence, this study aims to improve the dye removal performance of nanofibre membranes by incorporating zeolites. The research involved fabricating composite membranes by electrospinning polyvinyl alcohol (PVA) nanofibres incorporated with zeolites. Mechanical strength was enhanced by placing the PVA/zeolite nanofibre membrane between fusible nonwoven interfacing and woven polyester fabric, followed by heat treatment. Morphological analysis revealed the uniform dispersion of zeolite particles within the PVA nanofibres. EDX analysis confirmed the successful incorporation of zeolites into the fibres. Among all membrane samples, the PZ-0.75 membrane exhibited the highest pure water flux (PWF) with approximately 1358.57 L·m−2·min−1 for distilled water and 499.85 L·m−2·min−1 for batik wastewater. Turbidity of batik wastewater increased proportionally with zeolite concentration, with removal rates of 84.79%, 78.8%, 76.96%, and 74.19% for PZ-0.75, PZ-0.5, PZ-0.25, and PVA membranes, respectively. Furthermore, the UV/Vis spectrophotometer demonstrated that dye removal efficiency increased from 2.22% to 8.89% as the zeolite concentration increased from 0% to 0.75%. In addition, the PZ-0.75 membrane effectively removed RR dye at a concentration of 1 mg/L, with an optimal contact time of approximately 60 min. The adsorption mechanism of the PZ-0.75 membrane aligns with the Freundlich model, with an R2 value of 0.983. Overall, this study demonstrates the efficiency of zeolite in the fabric substrates to improve the filtration and adsorption properties for wastewater treatment, particularly in textile industries. Full article
(This article belongs to the Special Issue Advances in Coated Fabrics and Textiles)
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<p>The schematic view of electrospinning process.</p>
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<p>Arrangement of polyester, nanofibre, and nonwoven interfacing.</p>
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<p>The schematic view of heat treatment.</p>
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<p>FESEM images of (<b>a</b>) PVA nanofibre membranes, (<b>b</b>) PZ-0.25 membrane, (<b>c</b>) PZ-0.5 membrane, (<b>d</b>) PZ-0.75 membrane, and (<b>e</b>) zeolites.</p>
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<p>Fibre diameter of heat-treated membrane of different zeolite loadings.</p>
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<p>The effects of zeolite concentration with pure water flux (PWF) of distilled water and wastewater. Some error bars were omitted due to their low values.</p>
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<p>Turbidity of batik wastewater effluent of different membranes.</p>
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<p>The dye removal of Remazol Red dye of different composite membranes.</p>
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<p>Influence of zeolite concentrations on dye adsorption.</p>
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<p>Remazol Red dye absorption on zeolite.</p>
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<p>UV–vis spectra of liquid filtrate at different dye concentrations.</p>
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<p>Dye removal efficiency against initial dye concentration for PZ-0.75.</p>
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<p>Relationship between dye adsorption over the contact time.</p>
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<p>Dye removal efficiency against contact time for PZ-0.75.</p>
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<p>Relationship between initial dye concentration and dye adsorption capacity for PZ-0.75.</p>
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19 pages, 2897 KiB  
Article
Catalyst Accessibility and Acidity in the Hydrocracking of HDPE: A Comparative Study of H-USY, H-ZSM-5, and MCM-41 Modified with Ga and Al
by Cátia S. Costa, M. Rosário Ribeiro and João M. Silva
Molecules 2024, 29(17), 4248; https://doi.org/10.3390/molecules29174248 - 7 Sep 2024
Viewed by 348
Abstract
Plastic pollution is a critical environmental issue due to the widespread use of plastic materials and their long degradation time. Hydrocracking (HDC) offers a promising solution to manage plastic waste by converting it into valuable products, namely chemicals or fuels. This work aims [...] Read more.
Plastic pollution is a critical environmental issue due to the widespread use of plastic materials and their long degradation time. Hydrocracking (HDC) offers a promising solution to manage plastic waste by converting it into valuable products, namely chemicals or fuels. This work aims to investigates the effect of catalyst accessibility and acidity on the HDC reaction of high density polyethylene (HDPE). Therefore, a variety of materials with significant differences in both textural and acidic properties were tested as catalysts. These include H-USY and H-ZSM.5 zeolites with various Si/Al molar ratios (H-USY: Si/Al = 2.9, 15, 30 and 40; H-ZSM-5: Si/Al = 11.5, 40, 500) and mesostructured MCM-41 materials modified with Ga and Al, also with different Si/metal ratios (Si/Al = 16 and 30; Si/Ga = 63 and 82). Thermogravimetric analysis under hydrogen atmosphere was used as a preliminary screening tool to evaluate the potential of the various catalysts for this application in terms of energy requirements. In addition, batch autoclave reactor experiments (T = 300 °C, PH2 = 20 bar, t = 60 min) were conducted to obtain further information on conversion, product yields and product distribution for the most promising systems. The results show that the catalytic performance in HDPE hydrocracking is determined by a balance between the acidity of the catalyst and its structural accessibility. Accordingly, for catalyst series where the structural and textural properties do not vary with the Si/Al ratio, there is a clear correlation of the HDPE degradation temperature and of the HDPE conversion with the Si/metal ratio (which relates to the acidic properties). In contrast, for catalyst series where the structural and textural properties vary with the Si/Al ratio, no consistent trend is observed and the catalytic performance is determined by a balance between the acidic and textural properties. The product distribution was also found to be influenced by the physical and chemical properties of the catalyst. Catalysts with strong acidity and smaller pores were observed to favor the formation of lighter hydrocarbons. In addition to the textural and acidic properties of the catalyst, the role of coke formation should not be neglected to ensure a comprehensive analysis of the catalytic performance. Full article
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<p>PXRD of Al- and Ga-modified MCM-41 (<b>A</b>) and of H-USY and H-ZSM-5 zeolites (<b>B</b>) with distinct Si/metal ratios.</p>
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<p>Yields in gas and liquid products obtained from the hydrocracking of HDPE over H-ZSM5 and H-USY with distinct Si/Al ratios and Al-MCM-41 (16) (T = 300 °C, t = 60 min, P<sub>H2i</sub> = 20 bar, and HDPE/catalyst mass ratio= 8/2).</p>
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<p>Total products distribution of HDPE hydrocracking over H-ZSM5 and H-USY with distinct Si/Al molar ratios and Al-MCM-41 (16) (T = 300 °C, t = 60min, PH2i = 20 bar, and HDPE/catalyst mass ratio = 8/2).</p>
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<p>Gaseous products distribution of HDPE hydrocracking over H-ZSM-5 and H-USY with distinct Si/Al ratios and Al-MCM-41 (16) (T = 300 °C, t = 60 min, PH2i = 20 bar, and HDPE/catalyst mass ratio = 8/2).</p>
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<p>Liquid products distribution of HDPE hydrocracking over H-ZSM-5 and H-USY with distinct Si/Al ratios and Al-MCM-41 (16) (T = 300 °C, t = 60 min, PH2i = 20 bar, HDPE/catalyst mass ratio = 8/2).</p>
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<p>FTIR spectra (<b>A</b>) from 2700–3100 cm<sup>−1</sup> and (<b>B</b>) from 700–1700 cm<sup>−1</sup> of liquid product obtained from HDPE hydrocracking over H-ZSM5 and H-USY with distinct Si/Al molar ratios and Al-MCM-41 (16) (T = 300 °C, t = 60 min, PH2i = 20 bar, and HDPE/catalyst mass ratio = 8/2).</p>
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<p>Yield in coke of HDPE hydrocracking over H-ZSM5 and H-USY with distinct Si/Al ratios and Al-MCM-41 (16) (T = 300 °C, t = 60 min, PH<sub>2i</sub> = 20 bar, and HDPE/catalyst mass ratio = 8/2).</p>
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17 pages, 3699 KiB  
Article
Application of Immobilized Microorganism Gel Beads in Black-Odor Water with High Nitrogen and Phosphorus Removal Performance
by Fengbin Zhao, Shumin Liu, Xin Fang and Ning Yang
Water 2024, 16(17), 2534; https://doi.org/10.3390/w16172534 - 7 Sep 2024
Viewed by 363
Abstract
Black-odor water, which is caused by the excessive accumulation of nitrogen and phosphorus in water, is a significant problem. Immobilized microorganisms are considered to be an effective technical solution, but there are still many key parameters to be determined, such as organic matter [...] Read more.
Black-odor water, which is caused by the excessive accumulation of nitrogen and phosphorus in water, is a significant problem. Immobilized microorganisms are considered to be an effective technical solution, but there are still many key parameters to be determined, such as organic matter dissolution, insufficient stability, and insufficient phosphorus removal capacity, among other problems. In this study, the optimum raw material ratios of immobilized microorganism gel beads were determined by means of a response surface experiment. The optimal ratio of raw materials was 5% polyvinyl alcohol (PVA), 1% sodium alginate (SA), and 6% bacterial powder. In addition, the nitrogen and phosphorus removal performance of the materials was improved by loading inorganic compounds, such as 0.5 wt.% zeolite, 0.5 wt.% iron powder, and 0.2 wt.% activated carbon. Tolerance analysis determined that these gel beads could maintain a good performance in a series of harsh environments, such as during intense agitation, at high temperatures, and at low pH values, etc. The total nitrogen (TN), ammonia nitrogen (NH3-N), and phosphorus (TP) removal efficiencies were 88.9%, 90%, and 95%. Full article
(This article belongs to the Section Wastewater Treatment and Reuse)
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<p>Schematic diagram of the simulated device for immobilized microorganisms to treat contaminated water.</p>
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<p>The response surface 3D maps of NH<sub>3</sub>-N removal rates with the variation sources (5% bacterial dose (<b>a</b>), 1% SA content (<b>b</b>), and 5% PVA content (<b>c</b>)).</p>
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<p>The covalent immobilization of microbial cells on microchannel surfaces. SEM of common carrier (<b>a</b>) and immobilized microorganism (<b>b</b>) surface; SEM diagram of immobilized gel beads (surface structure (<b>c</b>) and internal structure (<b>d</b>)); the CLSM images of the granules of immobilized beads (living cells (green) (<b>e</b>), dead cells (red) (<b>f</b>), and combined image of living and dead cells (<b>g</b>)).</p>
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<p>The concentration of TOC change curves of the gel beads with time under different cross-linking time conditions (<b>a</b>), concentrations of calcium chloride (<b>b</b>), and PVA viscosities (<b>c</b>).</p>
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<p>Total amounts of nitrogen (<b>a</b>), ammonia nitrogen (<b>b</b>), and phosphorus (<b>c</b>) removed by immobilized microorganism loaded with zeolite; total nitrogen (<b>d</b>), ammonia nitrogen (<b>e</b>), and phosphorus (<b>f</b>) removal by immobilized microorganisms loaded by iron powder; total nitrogen (<b>g</b>), ammonia nitrogen (<b>h</b>), and phosphorus (<b>i</b>) removal by immobilized microorganism loaded with activated carbon.</p>
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<p>The proportion of complete particles and damaged particles in the immobilized microorganism particle oscillation experiment (<b>a</b>) should be changed, and the relationship between the repeated use of immobilized microorganisms and the removal rate of ammonia nitrogen (<b>b</b>).</p>
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<p>Removal of nitrogen and phosphorus pollutants by immobilized microorganisms and non-immobilized agent under different temperature conditions (<b>a</b>) and OD600 changes by immobilized microorganisms and non-immobilized agent under different pH conditions (<b>b</b>).</p>
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<p>The total nitrogen (<b>a</b>), ammonia nitrogen (<b>b</b>), and phosphate (<b>c</b>) concentration changes in black and odorous water.</p>
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<p>Changes in microbial community structure of the black-odor water before and after treatment (genus level).</p>
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17 pages, 5577 KiB  
Article
Y and ZSM-5 Hierarchical Zeolites Prepared Using a Surfactant-Mediated Strategy: Effect of the Treatment Conditions
by Andrea Ruggiu, Ana Paula Carvalho, Elisabetta Rombi, Angela Martins, João Rocha, Pier Parpot, Isabel C. Neves and Maria Giorgia Cutrufello
Materials 2024, 17(17), 4401; https://doi.org/10.3390/ma17174401 - 6 Sep 2024
Viewed by 340
Abstract
Diffusional limitations associated with zeolite microporous systems can be overcome by developing hierarchical zeolites, i.e., materials with a micro- and mesoporous framework. In this work, Y and ZSM-5 zeolites were modified using a surfactant-mediated hydrothermal alkaline method, with NaOH and cetyltrimethylammonium bromide (CTAB). [...] Read more.
Diffusional limitations associated with zeolite microporous systems can be overcome by developing hierarchical zeolites, i.e., materials with a micro- and mesoporous framework. In this work, Y and ZSM-5 zeolites were modified using a surfactant-mediated hydrothermal alkaline method, with NaOH and cetyltrimethylammonium bromide (CTAB). For Y zeolite, after a mild acidic pretreatment, the effect of the NaOH+CTAB treatment time was investigated. For ZSM-5 zeolite, different concentrations of the base and acid solutions were tested in the two-step pretreatment preceding the hydrothermal treatment. The properties of the materials were studied with different physical–chemical techniques. Hierarchical Y zeolites were characterized by 3.3–5 nm pores formed during the alkaline treatment through the structure reconstruction around the surfactant aggregates. The effectiveness of the NaOH+CTAB treatment was highly dependent on the duration. For intermediate treatment times (6–12 h), both smaller and larger mesopores were also obtained. Hierarchical ZSM-5 zeolites showed a disordered mesoporosity, mainly resulting from the pretreatment rather than from the subsequent hydrothermal treatment. High mesoporosity was obtained when the concentration of the pretreating base solution was sufficiently high and that of the acid one was not excessive. Hierarchical materials can be obtained for both zeolite structures, but the pretreatment and treatment conditions must be tailored to the starting zeolite and the desired type of mesoporosity. Full article
(This article belongs to the Section Porous Materials)
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<p>X-ray diffraction patterns of the Y zeolites. Miller indexes are attributed according to the IZA Database of Zeolite Structures (<a href="http://www.iza-structure.org/databases" target="_blank">http://www.iza-structure.org/databases</a>, accessed on 9 July 2024).</p>
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<p>(<b>a</b>) N<sub>2</sub> physisorption isotherms of the Y zeolites (adsorption: full symbols, desorption: open symbols); (<b>b</b>) Cumulative mesopore volume curves of the Y zeolites, obtained with the DFT method.</p>
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<p>TEM micrographs of the Y zeolites: (<b>a</b>) NaY; (<b>b</b>) Y_C2; (<b>c</b>) Y_C6; (<b>d</b>) Y_C12.</p>
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<p>(<b>a</b>) <sup>29</sup>Si MAS-NMR and (<b>b</b>) <sup>27</sup>Al MAS-NMR spectra of commercial and hierarchical Y zeolites.</p>
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<p>X-ray diffraction patterns of the ZSM-5 zeolites. Miller indexes are attributed according to the IZA Database of Zeolite Structures (<a href="http://www.iza-structure.org/databases" target="_blank">http://www.iza-structure.org/databases</a> (accessed on 9 July 2024)).</p>
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<p>N<sub>2</sub> physisorption isotherms of (<b>a</b>) pretreated ZSM-5_P_<span class="html-italic">x</span>/<span class="html-italic">y</span> and (<b>b</b>) final ZSM-5_<span class="html-italic">x</span>/<span class="html-italic">y</span>_C6 zeolites (adsorption: full symbols, desorption: open symbols); Cumulative mesopore volume curves obtained with the DFT method for (<b>c</b>) pretreated ZSM-5_P_<span class="html-italic">x</span>/<span class="html-italic">y</span> and (<b>d</b>) final ZSM-5_<span class="html-italic">x</span>/<span class="html-italic">y</span>_C6 zeolites. Starting NH<sub>4</sub>ZSM-5 data are also reported.</p>
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<p>TEM micrographs of the ZSM-5 zeolites: (<b>a</b>) NH<sub>4</sub>ZSM-5; (<b>b</b>) ZSM-5_P_1/0.6; (<b>c</b>) ZSM-5_1/0.6_C6.</p>
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<p>(<b>a</b>) <sup>29</sup>Si MAS-NMR and (<b>b</b>) <sup>27</sup>Al MAS-NMR spectra of NH<sub>4</sub>ZSM-5 and ZSM-5_1/0.6_C6 zeolites.</p>
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<p>Deconvolution of the <sup>29</sup>Si MAS-NMR spectra of (<b>a</b>) NH<sub>4</sub>ZSM-5 and (<b>b</b>) ZSM-5_1/0.6_C6.</p>
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30 pages, 7262 KiB  
Article
A Selective, Efficient, Facile, and Reusable Natural Clay/Metal Organic Framework as a Promising Adsorbent for the Removal of Drug Residue and Heavy Metal Ions
by Rania Abdelazeem, Heba A. Younes, Zienab E. Eldin, Ahmed A. Allam, Hassan Ahmed Rudayni, Sarah I. Othman, Ahmed A. Farghali, Hamada M. Mahmoud and Rehab Mahmoud
Colloids Interfaces 2024, 8(5), 50; https://doi.org/10.3390/colloids8050050 - 5 Sep 2024
Viewed by 543
Abstract
It is imperative to eliminate heavy metals and pharmaceutical residual pollutants from wastewater to reduce their detrimental effects on the environment. In this work, natural zeolite and a 2-amino terephthalic acid-based multi-metallic organic framework were used to create a new composite that can [...] Read more.
It is imperative to eliminate heavy metals and pharmaceutical residual pollutants from wastewater to reduce their detrimental effects on the environment. In this work, natural zeolite and a 2-amino terephthalic acid-based multi-metallic organic framework were used to create a new composite that can be utilized as an adsorbent for cadmium and safinamide. The adsorption study was examined in a variety of settings (pH, adsorbent dosage, pollutant concentration, and time). Moreover, Zeta potential, BET, SEM, FTIR, XRD, and SEM measurements were used to characterize the adsorbents. The adsorption process was confirmed using FTIR, XRD, and SEM analysis. Various nonlinear adsorption isotherm models were applied to adsorption results. The results showed a significantly better adsorption ability for safinamide and cadmium using zeolite/MOF compared to zeolite. Adsorption kinetics were represented by five models: pseudo first-order, pseudo second-order, intraparticle diffusion, mixed first- and second-order, and the Avrami model. Regarding both adsorbent substances, safinamide adsorption was best represented by the intraparticle diffusion model. In contrast, the pseudo second-order and intraparticle diffusion models for zeolite and zeolite/MOF, respectively, better fit the experimental results in the case of cadmium adsorption. The thermodynamic parameters ΔH°, ΔS°, and ΔG° were investigated through temperature tests carried out at 25, 35, 45, and 55 °C. Exothermic and spontaneous adsorption processes were demonstrated by the computed values. The study of adsorbent regeneration involved the use of several chemical solvents. The DMSO solvent was shown to have the highest adsorbent regeneration method efficiency at 63%. Safinamide elimination was lessened by organic interfering species like cefixime and humic acid compared to inorganic species like chloride, sulphate, and nitrate, most likely as a result of intense competition for the few available active sites. Using zeolite/MOF nanocomposite, the percentage of safinamide removed from spiked real water samples (tap water, Nile River water, and groundwater samples) was 48.80%, 64.30%, and 44.44%, respectively. Based on cytotoxicity results, the highest percentages of cell viability for zeolite and zeolite/MOF at 24 h were 83% and 81%, respectively, in comparison to untreated controls. According to these results, zeolite and zeolite/MOF composites can be used as effective adsorbents for these pollutants in wastewater. Full article
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<p>XRD patterns of pure Cu/Ni/Co ABDC (MOF) and Zeolite/MOF samples.</p>
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<p>FTIR analysis of (<b>a</b>) zeolite, MOF, and zeolite/MOF. (<b>b</b>) Zeolite/MOF after safinamide adsorption (zeolite/MOF/Safinamide), and zeolite/MOF after cadmium adsorption (zeolite/MOF/Cd) samples.</p>
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<p>SEM micrographs of (<b>a</b>) zeolite, (<b>b</b>) pure MOF, and (<b>c</b>) Zeolite/MOF samples. (<b>d</b>,<b>e</b>) EDX analysis of zeolite and zeolite/MOF samples, respectively, (<b>f</b>) for the Zeolite/MOF sample after Cd <sup>2+</sup> adsorption, N<sub>2</sub> adsorption–desorption isotherms of (<b>g</b>) Zeolite, (<b>h</b>) Zeolite/MOF samples and (<b>i</b>) pore size distribution of Zeolite/MOF.</p>
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<p>SEM micrographs of (<b>a</b>) zeolite, (<b>b</b>) pure MOF, and (<b>c</b>) Zeolite/MOF samples. (<b>d</b>,<b>e</b>) EDX analysis of zeolite and zeolite/MOF samples, respectively, (<b>f</b>) for the Zeolite/MOF sample after Cd <sup>2+</sup> adsorption, N<sub>2</sub> adsorption–desorption isotherms of (<b>g</b>) Zeolite, (<b>h</b>) Zeolite/MOF samples and (<b>i</b>) pore size distribution of Zeolite/MOF.</p>
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<p>(<b>a</b>) zeta potential and (<b>b</b>) Size distribution of zeolite/MOF material. (<b>c</b>,<b>d</b>) are the zeta potentials of zeolite and MOF samples, respectively.</p>
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<p>Effect of pH on the adsorption percentage of (<b>A</b>) safinamide and (<b>B</b>) Cd<sup>2+</sup> onto zeolite and zeolite/MOF.</p>
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<p>Effect of adsorbent dose on the adsorption of (<b>A</b>) safinamide and (<b>B</b>) Cd (II) onto zeolite and zeolite/MOF.</p>
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<p>Best fit isotherm model for safinamide adsorption onto (<b>a</b>) zeolite and (<b>b</b>) zeolite/MOF; best-fit isotherm model for Cd<sup>2+</sup> adsorption onto (<b>c</b>) zeolite and (<b>d</b>) zeolite/MOF.</p>
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<p>Kinetic model fitting for safinamide adsorption onto (<b>a</b>) zeolite and (<b>b</b>) zeolite/MOF; kinetic model fitting for Cd<sup>2+</sup> adsorption onto (<b>c</b>) zeolite and (<b>d</b>) zeolite/MOF.</p>
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<p>(<b>a</b>) Desorption of safinamide using different eluents, (<b>b</b>) reuse of Co/Ni/Cu-NH<sub>2</sub>BDC MOF/zeolite nanocomposite, and (<b>c</b>) XRD diffractograms of zeolite/MOF adsorbent before and after recycling.</p>
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<p>(<b>a</b>) Desorption of safinamide using different eluents, (<b>b</b>) reuse of Co/Ni/Cu-NH<sub>2</sub>BDC MOF/zeolite nanocomposite, and (<b>c</b>) XRD diffractograms of zeolite/MOF adsorbent before and after recycling.</p>
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<p>Removal percentage of zeolite/MOF for safinamide in the presence of different competing adsorbates (<b>a</b>) with different initial concentrations and (<b>b</b>) at 100 mg/L initial concentration.</p>
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<p>The study of variations in K<sub>d</sub> with temperature enables us to estimate the thermodynamic parameters.</p>
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<p>Possible adsorption mechanism of safinamide onto (<b>a</b>) zeolite and (<b>b</b>) zeolite/MOF and Possible adsorption mechanism of Cd onto (<b>c</b>) zeolite and (<b>d</b>) zeolite/MOF.</p>
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<p>Possible adsorption mechanism of safinamide onto (<b>a</b>) zeolite and (<b>b</b>) zeolite/MOF and Possible adsorption mechanism of Cd onto (<b>c</b>) zeolite and (<b>d</b>) zeolite/MOF.</p>
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<p>Cell viability (%) of zeolite and zeolite/MOF at different concentrations after (<b>a</b>) 24 h and (<b>b</b>) 48 h (n = 3) ± SD.</p>
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31 pages, 7095 KiB  
Article
Evaluation of a Volume-Averaged Species Transport Model with Micro–Macro Coupling for Breakthrough Curve Prediction
by Parham Mobadersani, Naine Tarun Bharat and Krishna M. Pillai
Molecules 2024, 29(17), 4218; https://doi.org/10.3390/molecules29174218 - 5 Sep 2024
Viewed by 497
Abstract
In porous water filters, the transport and entrapment of contaminants can be modeled as a classic mass transport problem, which employs the conventional convection–dispersion equation to predict the transport of species existing in trace amounts. Using the volume-averaging method (VAM), the upscaling has [...] Read more.
In porous water filters, the transport and entrapment of contaminants can be modeled as a classic mass transport problem, which employs the conventional convection–dispersion equation to predict the transport of species existing in trace amounts. Using the volume-averaging method (VAM), the upscaling has revealed two possible macroscopic equations for predicting contaminant concentrations in the filters. The first equation is the classical convection–dispersion equation, which incorporates a total dispersion tensor. The second equation involves an additional transport coefficient, identified as the adsorption-induced vector. In this study, the aforementioned equations were solved in 1D for column tests using 3D unit cells. The simulated breakthrough curves (BTCs), using the proposed micro–macro-coupling-based VAM model, are compared with the direct numerical simulation (DNS) results based on BCC-type unit cells arranged one-after-another in a daisy chain manner, as well as with three previously reported experimental works, in which the functionalized zeolite and zero-valent iron fillings were used as an adsorbent to remove phosphorous and arsenic from water, respectively. The disagreement of VAM BTC predictions with DNS and experimental results reveals the need for an alternative closure formulation in VAM. Detailed investigations reveal time constraint violations in all the three cases, suggesting this as the main cause of VAM’s failure. Full article
(This article belongs to the Special Issue New Insights into Porous Materials in Adsorption and Catalysis)
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<p>A schematic showing the relationship between the macroscopic region (where averaged equations apply) and the averaging volume (also called representative elementary volume or REV). In VAM, the REV is replaced by a unit cell after applying some assumptions. (σ-phase: solid particles; β-phase: incompressible fluid; L: column length).</p>
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<p>Sketch of the computational domain for the 3D system used to perform the direct numerical simulations (DNS) along with the applied boundary conditions.</p>
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<p>Flow chart for the VAM simulation process.</p>
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<p>Some important boundary conditions applied to the unit cell for Stoke’s flow simulation. On the side walls, symmetry conditions were employed where the appropriate velocity gradients were set to zero.</p>
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<p>Mesh structures in unit cell studied for grid independence. (<b>A</b>) coarse, (<b>B</b>) normal, (<b>C</b>) fine, (<b>D</b>) finer, and (<b>E</b>) extra fine.</p>
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<p>The BTC by the present VAM execution is compared with BTC predicted by VAM in [<a href="#B51-molecules-29-04218" class="html-bibr">51</a>]. The triangle symbols represent the result from the present study while the dashed line is for the work conducted in [<a href="#B51-molecules-29-04218" class="html-bibr">51</a>].</p>
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<p>(<b>a</b>) The unit cell obtained from the micro-CT scans of zeolite-based porous filter [<a href="#B23-molecules-29-04218" class="html-bibr">23</a>]. (<b>b</b>) A comparison of the effluent phosphorous concentrations measured in the experiments and predicted using VAM [<a href="#B23-molecules-29-04218" class="html-bibr">23</a>].</p>
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<p>The structure of the unit cell for solving the closure formulation. The fluid domain is shown in light blue color while the solid phase in the form of a spherical particle is shown in brown.</p>
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<p>Grid independence study for Case II.</p>
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<p>Streamline and velocity distribution in a few unit cells arranged in daisy-chain manner behind one another.</p>
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<p>Schematic representation of the three sets of faces of the unit cell where the periodic boundary conditions of the closure formulation, Equations (21c) and (22c), are applied.</p>
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<p>The BTCs predicted by VAM, DNS, and the experiments are compared for Case II. The inserted figure shows the plot at an enlarged time scale for the VAM result.</p>
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<p>BCC-type unit cell with a central solid-phase (ZVI) particle of spherical shape located at the center of a cube.</p>
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<p>Result of grid-independence study for Case III.</p>
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<p>VAM, DNS, and experimental result comparison. The inserted figure shows the enlarged time scale for the present VAM.</p>
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<p>Comparison plot for the induced concentration and characteristic time (τ), represented by dashed color line, for Cases I, II, and III.</p>
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<p>Boundary conditions for the CFD simulation conducted for estimating the characteristic time.</p>
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<p>Characteristic time for Cases I, II, and III estimated by solving the species transport convection–diffusion equation within the unit cell.</p>
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1 pages, 147 KiB  
Correction
Correction: Belal et al. Therapeutic Potential of Zeolites/Vitamin B12 Nanocomposite on Complete Freund’s Adjuvant-Induced Arthritis as a Bone Disorder: In Vivo Study and Bio-Molecular Investigations. Pharmaceuticals 2023, 16, 285
by Amany Belal, Rehab Mahmoud, Mohamed Taha, Fatma Mohamed Halfaya, Ahmed Hassaballa, Esraa Salah Elbanna, Esraa Khaled, Ahmed Farghali, Fatma I. Abo El-Ela, Samar M. Mahgoub, Mohammed M. Ghoneim and Mohamed Y. Zaky
Pharmaceuticals 2024, 17(9), 1172; https://doi.org/10.3390/ph17091172 - 5 Sep 2024
Viewed by 222
Abstract
In the original publication [...] Full article
15 pages, 14229 KiB  
Article
Trade-Off between Degradation Efficiency and Recyclability: Zeolite-Enhanced Ni3−xCoxS4 Catalyst for Photocatalytic Degradation of Methylene Blue
by Rachel Anne E. Lagunay, Ritche Roi B. Adalim, Aruzhan Tleubekova, Diana Suleimenova, Marvin Jose F. Fernandez, Robert J. O’Reilly and Mannix P. Balanay
Molecules 2024, 29(17), 4167; https://doi.org/10.3390/molecules29174167 - 3 Sep 2024
Viewed by 506
Abstract
We herein report successful syntheses of both nickel cobalt sulfide (NCS) and its composite with zeolite (NCS@Z) using a solvothermal method. Techniques such as EDX analysis, SEM, and molar ratio determination were used for product characterization. The incorporation of NCS significantly changed the [...] Read more.
We herein report successful syntheses of both nickel cobalt sulfide (NCS) and its composite with zeolite (NCS@Z) using a solvothermal method. Techniques such as EDX analysis, SEM, and molar ratio determination were used for product characterization. The incorporation of NCS significantly changed the surface roughness and active sites of the zeolite, improving the efficiency of methylene blue degradation and its reusability, especially under UV irradiation. In comparing the pseudo-first order rates, the highest degradation efficiency of methylene blue was achieved with NCS-2@Z, having a degradation extent of 91.07% under UV irradiation. This environmentally friendly approach offers a promising solution for the remediation of methylene blue contamination in various industries. Full article
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<p>Comparison of resonance structures depicting the oxidized form of MB alongside its reduced leuco form.</p>
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<p>SEM images and EDX spectra with the elemental compositions of (<b>a</b>,<b>b</b>) NCS-1 and (<b>c</b>,<b>d</b>) NCS-2.</p>
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<p>XRD spectra of NCS-1 and NCS-2.</p>
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<p>(<b>a</b>,<b>d</b>,<b>g</b>) Influence of initial MB concentration on the photocatalytic degradation efficiency of NCS-1 and NCS-2 catalysts. Plots illustrating the (<b>b</b>,<b>e</b>,<b>h</b>) pseudo-first order and (<b>c</b>,<b>f</b>,<b>i</b>) pseudo-second order kinetics for the degradation of MB utilizing NCS-1 and NCS-2 catalysts under different light conditions. The dotted lines in the kinetic plots represent linear regression fittings of the experimental data.</p>
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<p>(<b>a</b>,<b>c</b>) Influence of the amount of NCS-1 and NCS-2 catalysts on the degradation efficiency (%) of MB and the diagrams of the (<b>b</b>,<b>d</b>) pseudo-first order degradation of MB using different amounts of NCS-1 and NCS-2 catalysts under UV irradiation (254 nm). The dotted lines in the kinetic diagrams represent the linear regression fit of the kinetic data.</p>
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<p>(<b>a</b>,<b>c</b>) Influence of the amount of NCS-1 and NCS-2 catalysts on the degradation efficiency (%) of MB and the diagrams of the (<b>b</b>,<b>d</b>) pseudo-first order degradation of MB using different amounts of NCS-1 and NCS-2 catalysts under light. The dotted lines in the kinetic diagrams represent the linear regression fit of the kinetic data.</p>
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<p>Influence of different scavengers on the pseudo-first order photocatalytic degradation efficiency of MB (H<sub>2</sub>O<sub>2</sub>-assisted) under UV light (254 nm) using 15 mg of NCS-2. The dotted lines in the kinetic diagrams represent the linear regression fit of the kinetic data.</p>
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<p>SEM images of NCS-2 after exposure to different scavengers: (<b>a</b>) SN, (<b>b</b>) KI, and (<b>c</b>) t-B scavengers.</p>
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<p>XRD pattern of NCS-2 after exposure to different scavengers.</p>
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<p>(<b>a</b>) Recyclability investigation of NCS-2 for the degradation of MB dye. (<b>b</b>) SEM image of NCS-2 after photocatalytic degradation. (<b>c</b>) XRD pattern before and after photocatalytic degradation.</p>
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<p>SEM images and EDX spectra with the elemental composition of (<b>a</b>,<b>b</b>) pure zeolite and (<b>c</b>,<b>d</b>) NCS-2@Z.</p>
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<p>XRD spectra of pure zeolite and NCS-2@Z.</p>
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<p>(<b>a</b>) Recyclability investigation of NCS-2@Z for the degradation of MB dye. (<b>b</b>) SEM image of NCS-2@Z after photocatalytic degradation. (<b>c</b>) XRD pattern before and after photocatalytic degradation.</p>
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17 pages, 3414 KiB  
Article
Impact of PEG400–Zeolite Performance as a Material for Enhancing Strength of the Mechanical Properties of LECA/Foamed Lightweight Concrete
by Hebah Mohammad Al-Jabali, Walid Fouad Edris, Shady Khairy, Ghada N. Mohamed, Hebatallah A. Elsayed and Ahmed A. El-Latief
Infrastructures 2024, 9(9), 149; https://doi.org/10.3390/infrastructures9090149 - 2 Sep 2024
Viewed by 549
Abstract
A versatile building material, foamed concrete is made of cement, fine aggregate, and foam combined with coarse aggregate. This study provides a description of how constant coarse aggregate replacement (50%) of LECA and foamed concrete, which are lightweight concrete types, by zeolite as [...] Read more.
A versatile building material, foamed concrete is made of cement, fine aggregate, and foam combined with coarse aggregate. This study provides a description of how constant coarse aggregate replacement (50%) of LECA and foamed concrete, which are lightweight concrete types, by zeolite as a filler and PEG-400 as a plasticizer, water retention agent, and strength enhancer affect the mechanical properties of the cement. A study that examined the characteristics of cellular lightweight concrete in both its fresh and hardened forms was carried out for both foamed concrete and LECA concrete. In order to do this, a composite of zeolite and polyethylene glycol 400 was made using the direct absorption method, and no leakage was seen. Zeolite was loaded to a level of 10% and 20% of the total weight in cement, while 400 g/mol PEG was used at levels of 1%, 1.5%, and 2% of the cement’s weight. Various mixtures having a dry density of 1250 kg/m3 were produced. Properties like dry density, splitting tensile strength, and compressive strength were measured. An increase in the amount of PEG400–zeolite was seen to lower the workability, or slump, of both foamed and LECA concrete, while the replacement of aggregate by zeolite resulted in an exponential drop in both compressive and flexural strengths. Full article
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<p>Platforms in contrast to Infra lightweight concrete [<a href="#B32-infrastructures-09-00149" class="html-bibr">32</a>].</p>
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<p>ILC family home in Berlin’s outside walls were built in 2007.</p>
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<p>Ggathered leftover EPS foams.</p>
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<p>Used LECA [BGN company-Egypt].</p>
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<p>Three images are shown: (<b>a</b>) a dense matrix image of structural lightweight concrete (LC); (<b>b</b>) an open pore image of lightweight aggregate concrete (LAC); and (<b>c</b>) an image of LAC with a porous matrix filling the open pore structure. Based on expanded clay from a single manufacturer, all three varieties of lightweight concrete are known as LECA.</p>
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<p>Distribution of particle sizes in natural coarse aggregate (NA), Foam and Leca.</p>
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<p>Image of the PEG-400 as solution.</p>
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<p>Distribution of particle sizes in zeolite and cement.</p>
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<p>Casted and Cured samples prior to performing different tests.</p>
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<p>Slump of both LWLC and FWLC mixtures.</p>
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<p>Comparison between Target density and obtained density for both LWLC and FWLC mixtures.</p>
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<p>Density of both LWLC and FWLC mixtures.</p>
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<p>Compressive strength Vs splitting tensile strength of both LWLC and FWLC mixtures.</p>
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<p>Water absorption of both LWLC and FWLC mixtures.</p>
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