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Chemical Technologies for Environmental Analysis and Pollution Removal

A special issue of Molecules (ISSN 1420-3049). This special issue belongs to the section "Applied Chemistry".

Deadline for manuscript submissions: closed (31 March 2024) | Viewed by 15172

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Department of Biological and Pharmaceutical Environmental Sciences and Technologies (DISTABIF), University of Campania Luigi Vanvitelli, Naples, Italy
Interests: environmental analysis; removal of environmental pollutants; wastewater treatment; environmental chemistry; advanced oxidation processes
Special Issues, Collections and Topics in MDPI journals

Special Issue Information

Dear Colleagues,

Environmental pollution, particularly in water, is a significant global concern due to its impact on human health and the ecosystem. The presence of various pollutants in wastewater, such as pharmaceuticals and personal care products, heavy metals, organic compounds, micro- and nanoplastics, surfactants, and pathogens, has resulted in severe consequences, including the contamination of drinking water sources, the destruction of aquatic habitats, and the spread of waterborne diseases.

To address this problem, numerous chemical technologies have been developed for the analysis and removal of pollutants in water, including advanced oxidation processes, membrane filtration, adsorption, and biological treatment, among others. These technologies have demonstrated great potential in effectively removing various types of pollutants from water, either alone or in combination with other methods.

This Special Issue invites original research papers and reviews reporting on recent progress in the development of chemical technologies for environmental analysis and pollution removal in water. The Issue will cover a broad range of topics, including the development of new methods for environmental analysis, the characterization of pollutants in water, the application of advanced oxidation processes, membrane filtration, and new adsorption materials for water treatment, as well as the evaluation of the performance and efficiency of these technologies. Additionally, focused review articles are welcome to examine the state of the art, identify emerging trends, and suggest future directions for developing new applications in this field.

Dr. Pasquale Iovino
Guest Editor

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Keywords

  • advanced oxidation processes
  • wastewater treatment
  • adsorbents
  • emerging technologies
  • removal of environmental pollutants
  • analysis techniques
  • emerging pollutant

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Related Special Issue

Published Papers (9 papers)

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14 pages, 14049 KiB  
Article
Fabrication of Nitrogen Based Magnetic Conjugated Microporous Polymer for Efficient Extraction of Neonicotinoids in Water Samples
by Zhenzhen Xia, Xinghua Teng, Yuqi Cheng, Yujie Huang, Liwen Zheng, Lei Ji and Leilei Wang
Molecules 2024, 29(10), 2189; https://doi.org/10.3390/molecules29102189 - 8 May 2024
Viewed by 571
Abstract
Facile and sensitive methods for detecting neonicotinoids (NEOs) in aquatic environments are crucial because they are found in extremely low concentrations in complex matrices. Herein, nitrogen-based magnetic conjugated microporous polymers (Fe3O4@N-CMP) with quaternary ammonium groups were synthesized for efficient [...] Read more.
Facile and sensitive methods for detecting neonicotinoids (NEOs) in aquatic environments are crucial because they are found in extremely low concentrations in complex matrices. Herein, nitrogen-based magnetic conjugated microporous polymers (Fe3O4@N-CMP) with quaternary ammonium groups were synthesized for efficient magnetic solid-phase extraction (MSPE) of NEOs from tap water, rainwater, and lake water. Fe3O4@N-CMP possessed a suitable specific surface area, extended π-conjugated system, and numerous cationic groups. These properties endow Fe3O4@N-CMP with superior extraction efficiency toward NEOs. The excellent adsorption capacity of Fe3O4@N-CMP toward NEOs was attributed to its π–π stacking, Lewis acid–base, and electrostatic interactions. The proposed MSPE-HPLC-DAD approach based on Fe3O4@N-CMP exhibited a wide linear range (0.1–200 µg/L), low detection limits (0.3–0.5 µg/L), satisfactory precision, and acceptable reproducibility under optimal conditions. In addition, the established method was effectively utilized for the analysis of NEOs in tap water, rainwater, and lake water. Excellent recoveries of NEOs at three spiked levels were in the range of 70.4 to 122.7%, with RSDs less than 10%. This study provides a reliable pretreatment method for monitoring NEOs in environmental water samples. Full article
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<p>SEM images of Fe<sub>3</sub>O<sub>4</sub> (<b>A</b>), Fe<sub>3</sub>O<sub>4</sub>@N-CMP (<b>B</b>); TEM images of Fe<sub>3</sub>O<sub>4</sub> (<b>C</b>), and Fe<sub>3</sub>O<sub>4</sub>@N-CMP (<b>D</b>).</p>
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<p>(<b>A</b>) FT-IR spectra; (<b>B</b>) N 1s XPS spectra; (<b>C</b>) magnetization curves (the inset shows magnetic separation of Fe<sub>3</sub>O<sub>4</sub>@N-CMP; (<b>D</b>) N<sub>2</sub> adsorption-desorption isotherm of Fe<sub>3</sub>O<sub>4</sub>@N-CMP (inset: pore size distribution curve).</p>
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<p>Optimization of MSPE conditions: (<b>A</b>) Fe<sub>3</sub>O<sub>4</sub>@N-CMP amount; (<b>B</b>) extraction time; (<b>C</b>) NaCl concentration; (<b>D</b>) pH; (<b>E</b>) type of elution solvent; (<b>F</b>) elution time (n = 3).</p>
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<p>Reusability of Fe<sub>3</sub>O<sub>4</sub>@N-CMP on the extraction of five NEOs.</p>
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<p>HPLC−DAD chromatograms of enriched NEOs from rainwater spiked with 0 (a), 5 (b), 50 (c), and 100 (d) μg/L, respectively.</p>
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<p>Illustration of the synthesis of Fe<sub>3</sub>O<sub>4</sub>@N-CMP and its MSPE procedure.</p>
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30 pages, 13773 KiB  
Article
Influence of Hydrothermal Modification on Adsorptive Performance of Clay Minerals for Malachite Green
by Enwen Wang, Teng Huang, Qian Wu, Lanchun Huang, Desong Kong and Hai Wang
Molecules 2024, 29(9), 1974; https://doi.org/10.3390/molecules29091974 - 25 Apr 2024
Viewed by 655
Abstract
Artificially modified adsorbing materials mainly aim to remedy the disadvantages of natural materials as much as possible. Using clay materials such as rectorite, sodium bentonite and metakaolinite (solid waste material) as base materials, hydrothermally modified and unmodified materials were compared. CM-HT and CM [...] Read more.
Artificially modified adsorbing materials mainly aim to remedy the disadvantages of natural materials as much as possible. Using clay materials such as rectorite, sodium bentonite and metakaolinite (solid waste material) as base materials, hydrothermally modified and unmodified materials were compared. CM-HT and CM (adsorbing materials) were prepared and used to adsorb and purify wastewater containing malachite green (MG) dye, and the two materials were characterized through methods such as BET, FT-IR, SEM and XRD. Results: (1) The optimal conditions for hydrothermal modification of CM-HT were a temperature of 150 °C, a time of 2 h, and a liquid/solid ratio 1:20. (2) Hydrothermal modification greatly increased the adsorptive effect. The measured maximum adsorption capacity of CM-HT for MG reached 290.45 mg/g (56.92% higher than that of CM). The theoretical maximum capacity was 625.15 mg/g (186.15% higher than that of CM). (3) Because Al-OH and Si-O-Al groups were reserved in unmodified clay mineral adsorbing materials with good adsorbing activity, after hydrothermal modification, the crystal structure of the clay became loosened along the direction of the c axis, and the interlayer space increased to partially exchange interlayer metal cations connected to the bottom oxygen, giving CM-HT higher electronegativity and creating more crystal defects and chemically active adsorbing sites for high-performance adsorption. (4) Chemical adsorption was the primary way by which CM-HT adsorbed cationic dye, while physical adsorption caused by developed pore canal was secondary. The adsorption reaction occurred spontaneously. Full article
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<p>Standard curve of pyrite.</p>
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<p>XRD of rectorite.</p>
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<p>Standard curve of quartz.</p>
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<p>XRD of montmorillonite.</p>
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<p>Influence of hydrothermal modification temperature on adsorption efficiency of CM-HT for MG.</p>
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<p>Influence of hydrothermal modification time on adsorption efficiency of CM-HT on MG.</p>
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<p>Influence of liquid/solid ratio on adsorption efficiency for CM-HT on MG.</p>
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<p>Pore size distribution diagrams for the CM and CM-HT samples.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms for CM and CM-HT samples.</p>
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<p>XRD diagram for three raw and hydrothermally modified clay minerals.</p>
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<p>XRD diagram for three raw and hydrothermally modified clay minerals.</p>
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<p>Diagram comparing the precursors of CM-HT before and after hydrothermal modification.</p>
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<p>Comparison diagram between CM-HT and its calcination precursor.</p>
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<p>SEM micrograph for the two adsorbents (1 and 2: surface images; 3 and 4: cross-section images).</p>
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<p>SEM micrograph for the two adsorbents (1 and 2: surface images; 3 and 4: cross-section images).</p>
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<p>FT-IR spectra of CM, CM-HT and calcination precursor.</p>
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<p>Influence of CM-HT concentration on MG removal rate and equilibrium adsorption capacity (<span class="html-italic">q</span><sub>e</sub>).</p>
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<p>Influence of MG initial concentration on removal rate by CM-HT and equilibrium adsorption capacity (<span class="html-italic">q<sub>e</sub></span>).</p>
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<p>Influence of adsorption time on adsorption capacity (<span class="html-italic">q<sub>t</sub></span>) by CM-HT.</p>
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<p>Influence of pH<sub>0</sub> on equilibrium CM-HT adsorption capacity (<span class="html-italic">q<sub>e</sub></span>) and equilibrium pH (pH<sub>e</sub>).</p>
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<p>Surface and cross-section SEM micrographs of CM-HT following adsorption and desorption.</p>
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<p>SEM micrographs of surface and cross-section of CM following adsorption and desorption.</p>
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<p>Influence of recycling cycles on adsorptive capacity of CM-HT.</p>
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<p>Schematic diagram for hydrothermal modification of montmorillonite and interlayer adsorption.</p>
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<p>Schematic diagram for CM-HT adsorbing cationic dye.</p>
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<p>FT-IR spectra of CM-HT (<b>a</b>): before MG adsorption; (<b>b</b>): after MG adsorption.</p>
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<p>MG adsorption isotherms for both adsorbents (35 ± 1 °C).</p>
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<p>Relation curve for <span class="html-italic">R<sub>L</sub></span> of both adsorbents vs. initial concentration of MG.</p>
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<p>Fits of kinetic models describing CM and CM-HT adsorbing MG at 35 ± 1 °C.</p>
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<p>Relation between Δ<span class="html-italic">G</span> and T for CM and CM-HT adsorbing MG dye.</p>
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17 pages, 1762 KiB  
Article
A Study on the Adsorption of Rhodamine B onto Adsorbents Prepared from Low-Carbon Fossils: Kinetic, Isotherm, and Thermodynamic Analyses
by Aleksandra Bazan-Wozniak, Aleksandra Jędrzejczak, Robert Wolski, Sławomir Kaczmarek, Agnieszka Nosal-Wiercińska, Judyta Cielecka-Piontek, Sultan Yagmur-Kabas and Robert Pietrzak
Molecules 2024, 29(6), 1412; https://doi.org/10.3390/molecules29061412 - 21 Mar 2024
Cited by 1 | Viewed by 1307
Abstract
The aim of this study was to obtain a series of activated carbon samples by the chemical activation of low-rank coal. The precursor was impregnated with a NaOH solution. Activated carbons were characterized by determining their textural parameters and content of surface oxygen [...] Read more.
The aim of this study was to obtain a series of activated carbon samples by the chemical activation of low-rank coal. The precursor was impregnated with a NaOH solution. Activated carbons were characterized by determining their textural parameters and content of surface oxygen functional groups and by using an elemental analysis. The carbons were tested as potential adsorbents for the removal of liquid pollutants represented by rhodamine B. The effectiveness of rhodamine B removal from water solutions depended on the initial concentration of the dye, the mass of rhodamine B, and the pH and temperature of the reaction. The isotherm examination followed the Langmuir isotherm model. The maximum adsorption capacity of the rhodamine B was 119 mg/g. The kinetic investigation favored the pseudo-second-order model, indicating a chemisorption mechanism. The thermodynamic assessment indicated spontaneous and endothermic adsorption, with decreased randomness at the solid–liquid interface. The experiment revealed that a 0.1 M HCl solution was the most effective regenerative agent. Full article
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<p>Pore distribution of the activated carbons.</p>
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<p>The nitrogen adsorption/desorption isotherms for activated carbons.</p>
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<p>Adsorption of iodine on the activated carbons.</p>
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<p>Effect of dosage (<b>a</b>) and adsorption efficiency (<b>b</b>) on Rhodamine B adsorption.</p>
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<p>Effect of shaking speed on Rhodamine B adsorption by activated carbon.</p>
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<p>Effect of contact time, activated carbon, and rhodamine B on adsorption capacity.</p>
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<p>Effect of process temperature on rhodamine B removal efficiency.</p>
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<p>The impact of pH on rhodamine B adsorption.</p>
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18 pages, 1575 KiB  
Article
Enhanced Sorption Performance of Natural Zeolites Modified with pH-Fractionated Humic Acids for the Removal of Methylene Blue from Water
by Stefano Salvestrini, Jean Debord and Jean-Claude Bollinger
Molecules 2023, 28(20), 7083; https://doi.org/10.3390/molecules28207083 - 14 Oct 2023
Cited by 1 | Viewed by 1052
Abstract
This work explores the effect of humic acids (HA) fractionation on the sorption ability of a natural zeolite (NYT)—HA adduct. HA were extracted from compost, fractionated via the pH fractionation method, and characterized via UV-Vis spectroscopy and gel permeation chromatography. The HA samples [...] Read more.
This work explores the effect of humic acids (HA) fractionation on the sorption ability of a natural zeolite (NYT)—HA adduct. HA were extracted from compost, fractionated via the pH fractionation method, and characterized via UV-Vis spectroscopy and gel permeation chromatography. The HA samples were immobilized onto NYT via thermal treatment. The resulting adducts (NYT-HA) were tested for their ability to remove methylene blue (MB) from an aqueous solution. It was found that the sorption performance of NYT-HA strongly depends on the chemical characteristics of humic acids. Sorption capacity increased with the molecular weight and hydrophobicity degree of the HA fractions. Hydrophobic and π–π interactions are likely the primary mechanisms by which MB interacts with HA. The sorption kinetic data conform to the pseudo-second-order model. The Freundlich isotherm model adequately described the sorption equilibrium and revealed that the uptake of MB onto NYT-HA is endothermic in nature. Full article
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<p>High-pressure gel permeation chromatograms of extracted HA samples: (<b>A</b>) unfractionated HA; (<b>B</b>) fraction of HA soluble at pH 3; (<b>C</b>) fraction of HA insoluble at pH 3 and dissolved at pH 5; (<b>D</b>) residual fraction of HA insoluble at pH 5 and dissolved at pH 7.</p>
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<p>Dependence of the MB aqueous concentration on time in the presence of NYT; <span class="html-italic">C</span><sub>0</sub> = initial MB concentration in the liquid phase; <span class="html-italic">T</span> = 20 °C. The curves in the figure were obtained via non-linear regression of the data using the Vermeulen model.</p>
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<p>Comparison of the sorption kinetics regarding the sorption of MB onto various sorbents. Initial concentration of MB = 11.9 mg L<sup>−1</sup>; <span class="html-italic">T</span> = 20 °C. The curves in the figure were obtained via nonlinear regression analysis using the PSO model, with the exception of the NYT data set modelled using the Vermeulen equation.</p>
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<p>Sorption isotherms regarding the sorption of MB onto various sorbents. <span class="html-italic">T</span> = 20 °C. The curves in the figure were obtained via nonlinear regression analysis using the Freundlich model, with the exception of NYT data set modelled using the Langmuir equation.</p>
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<p>Sorption isotherms regarding the sorption of MB onto NYT-HA<sub>7</sub> at various temperatures. The curves in the figure were obtained via non-linear regression analysis using the Freundlich isotherm model.</p>
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<p>Plot of 1/<span class="html-italic">n</span> against 1/<span class="html-italic">T</span> for the estimation of the standard sorption enthalpy (<math display="inline"><semantics> <mrow> <mi mathvariant="sans-serif">Δ</mi> <mi>H</mi> <mo>°</mo> </mrow> </semantics></math>) and the standard sorption entropy (<math display="inline"><semantics> <mrow> <mi mathvariant="sans-serif">Δ</mi> <mi>S</mi> <mo>°</mo> </mrow> </semantics></math>).</p>
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15 pages, 1087 KiB  
Article
Identification of the Contamination Sources by PCBs Using Multivariate Analyses: The Case Study of the Annaba Bay (Algeria) Basin
by Soumeya Khaled-Khodja, Hassen Cheraitia, Karima Rouibah, Hana Ferkous, Gaël Durand, Semia Cherif, Gamal A. El-Hiti, Krishna Kumar Yadav, Alessandro Erto and Yacine Benguerba
Molecules 2023, 28(19), 6841; https://doi.org/10.3390/molecules28196841 - 28 Sep 2023
Cited by 1 | Viewed by 1262
Abstract
Persistent Organic Pollutants (POPs), particularly the indicator polychlorinated biphenyls (PCBs), were first quantified in water and sediments of two wadis, Boujemaâ and Seybouse, as well as in the effluents from a fertilizer and phytosanitary production industrial plant (Fertial). Since these contaminated discharges end [...] Read more.
Persistent Organic Pollutants (POPs), particularly the indicator polychlorinated biphenyls (PCBs), were first quantified in water and sediments of two wadis, Boujemaâ and Seybouse, as well as in the effluents from a fertilizer and phytosanitary production industrial plant (Fertial). Since these contaminated discharges end in Annaba Bay (Algeria) in the Mediterranean Sea, with a significant level of contamination, all the potential sources should be identified. In this work, this task is conducted by a multivariate analysis. Liquid–liquid extraction and gas chromatography/mass spectrometry (GC–MS) methods were applied to quantify seven PCB congeners, usually taken as indicators of contamination. The sum of the PCB concentrations in the sediments ranged from 1 to 6.4 μg/kg dw (dry weight) and up to 0.027 μg/L in waters. Principal component analysis (PCA) and hierarchical cluster analysis (HCA) were used for the multivariate analysis, indicating that the main sources of PCB emissions in the bay are urban/domestic and agricultural/industrial. The outfalls that mostly contribute to the pollution of the gulf are the Boujemaâ wadi, followed by the Seybouse wadi, and finally by the Fertial cluster and more precisely the annex basin of the plant. Although referring to a specific site of local importance, the work aims to present a procedure and a methodological analysis that can be potentially applicable to further case studies all over the world. Full article
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<p>PCA applied on PCBs (variables) (<b>a</b>) and individuals (stations) (<b>b</b>) in sediments from various stations (First axis: Dim 1 and Second axis: Dim 2).</p>
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<p>Distribution of the stations and clusters (axes F1 × F2).</p>
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<p>Location of study sites and stations in Annaba Gulf (1. Boujemaâ wadi, 2. Anx Fertial, 3. PB Fertial, 4. Seybouse wadi).</p>
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14 pages, 4808 KiB  
Article
Removal of Hexamethyldisiloxane via a Novel Hydrophobic (3–Aminopropyl)Trimethoxysilane-Modified Activated Porous Carbon
by Siqi Lv, Yingrun Wang, Yanhui Zheng and Zichuan Ma
Molecules 2023, 28(18), 6493; https://doi.org/10.3390/molecules28186493 - 7 Sep 2023
Viewed by 1251
Abstract
Volatile methyl siloxanes (VMS) must be removed because the formation of silica in the combustion process seriously affects the resource utilization of biogas. Herein, a series of APTMS ((3–aminopropyl)trimethoxysilane)-modified activated porous carbon (APC) adsorbents (named APTMS@APC) were prepared for VMS efficient removal. The [...] Read more.
Volatile methyl siloxanes (VMS) must be removed because the formation of silica in the combustion process seriously affects the resource utilization of biogas. Herein, a series of APTMS ((3–aminopropyl)trimethoxysilane)-modified activated porous carbon (APC) adsorbents (named APTMS@APC) were prepared for VMS efficient removal. The as-prepared adsorbents were characterized using SEM, FTIR, Raman, X-ray diffraction analyses, and N2 adsorption/desorption. The results showed that the surface modification with APTMS enhanced the hydrophobicity of APC with the water contact angle increasing from 74.3° (hydrophilic) to 127.1° (hydrophobic), and meanwhile improved its texture properties with the SBET increasing from 981 to 1274 m2 g−1. The maximum breakthrough adsorption capacity of APTMS@APC for hexamethyldisiloxane (L2, model pollutant) was 360.1 mg g−1. Effects of an inlet L2 concentration (31.04–83.82 mg L−1) and a bed temperature (0–50 °C) on the removal of L2 were investigated. Meanwhile, after five adsorption–desorption cycles, the APTMS@APC demonstrated a superior cycling performance. This indicated that the hydrophobic APTMS@APC has a great significance to remove VMS. Full article
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<p>Structural formula of APTMS.</p>
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<p>SEM images (<b>a</b>–<b>d</b>), FTIR spectra (<b>e</b>), XRD patterns (<b>f</b>), and Raman spectra (<b>g</b>) of APC and APTMS@APC–0.125.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms and the pore size distribution profiles (inner) of APCs.</p>
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<p>Contact angle of APC (<b>a</b>), APTMS@APC–0.0625 (<b>b</b>), APTMS@APC–0.125 (<b>c</b>), APTMS@APC–0.25 (<b>d</b>), APTMS@APC–0.5 (<b>e</b>), and APTMS@APC–1 (<b>f</b>).</p>
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<p>Working mechanism of APTMS@APC adsorbent formation.</p>
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<p>Breakthrough adsorption curves and fitted trajectories of the APCs for L2.</p>
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<p>Relationship between <span class="html-italic">Q</span><sub>B,th</sub> and CA (<b>a</b>), <span class="html-italic">S</span><sub>BET</sub> (<b>b</b>), <span class="html-italic">V</span><sub>meso</sub> (<b>c</b>), and <span class="html-italic">V</span><sub>tot</sub> (<b>d</b>) for APTMS@APC–0.125.</p>
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<p>Breakthrough adsorption curves and fitted trajectories of the APCs in different solvents for L2 (<b>a</b>) and the trends of <span class="html-italic">Q</span><sub>B,th</sub> and CA with EtOH volume (<b>b</b>).</p>
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<p>Experimental breakthrough curves and model fitted trajectories for APTMS@APC–0.125 at different inlet concentrations (<b>a</b>) and temperatures (<b>b</b>).</p>
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<p><span class="html-italic">t</span><sub>B,th</sub> and <span class="html-italic">Q</span><sub>B,th</sub> of APTMS@APC–0.125 for L2 after each cycle.</p>
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20 pages, 4503 KiB  
Article
Experimental and Theoretical Estimations of Atrazine’s Adsorption in Mangosteen-Peel-Derived Nanoporous Carbons
by Juan Matos, Claudia P. Amézquita-Marroquín, Johan D. Lozano, Jhon Zapata-Rivera, Liliana Giraldo, Po S. Poon and Juan C. Moreno-Piraján
Molecules 2023, 28(13), 5268; https://doi.org/10.3390/molecules28135268 - 7 Jul 2023
Cited by 1 | Viewed by 1209
Abstract
Nanoporous carbons were prepared via chemical and physical activation from mangosteen-peel-derived chars. The removal of atrazine was studied due to the bifunctionality of the N groups. Pseudo-first-order, pseudo-second-order, and intraparticle pore diffusion kinetic models were analyzed. Adsorption isotherms were also analyzed according to [...] Read more.
Nanoporous carbons were prepared via chemical and physical activation from mangosteen-peel-derived chars. The removal of atrazine was studied due to the bifunctionality of the N groups. Pseudo-first-order, pseudo-second-order, and intraparticle pore diffusion kinetic models were analyzed. Adsorption isotherms were also analyzed according to the Langmuir and Freundlich models. The obtained results were compared against two commercially activated carbons with comparable surface chemistry and porosimetry. The highest uptake was found for carbons with higher content of basic surface groups. The role of the oxygen-containing groups in the removal of atrazine was estimated experimentally using the surface density. The results were compared with the adsorption energy of atrazine theoretically estimated on pristine and functionalized graphene with different oxygen groups using periodic DFT methods. The energy of adsorption followed the same trend observed experimentally, namely the more basic the pH, the more favored the adsorption of atrazine. Micropores played an important role in the uptake of atrazine at low concentrations, but the presence of mesoporous was also required to inhibit the pore mass diffusion limitations. The present work contributes to the understanding of the interactions between triazine-based pollutants and the surface functional groups on nanoporous carbons in the liquid–solid interface. Full article
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<p>(<b>a</b>) N<sub>2</sub> adsorption–desorption isotherms at −196 °C; (<b>b</b>) pore size distributions. The figure inset shows the cumulative pore volume on the activated carbons.</p>
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<p>SEM images of the homemade carbons: (<b>a</b>) MPB-CO<sub>2</sub>; (<b>b</b>) MPB-P50.</p>
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<p>Evolution of pH of activated carbons as a function of contact time.</p>
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<p>Kinetics of atrazine adsorption (q<sub>t</sub>) as a function of the initial concentration: (<b>a</b>) AC<sub>M</sub>; (<b>b</b>) AC<sub>PC</sub>; (<b>c</b>) MPB-CO<sub>2</sub>; (<b>d</b>) MPB-P50.</p>
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<p>Adsorption isotherms of atrazine: (<b>a</b>) ACM; (<b>b</b>) ACPC; (<b>c</b>) MPB-CO<sub>2</sub>; (<b>d</b>) MPB-P50.</p>
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<p>Optimized geometries of adsorbed systems in 1/1 monolayer using one atrazine molecule on a 5 × 5 graphene surface unit cell. O, N, Cl, and H atoms correspond to red, blue, green, and grey spheres, respectively.</p>
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<p>DOS (black line) and projected DOS on the pristine G<sub>Pristine</sub> graphene (green line) and atrazine (blue line) with the PBE functional.</p>
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<p>Schematic model for the atrazine adsorption on porous carbons: (<b>a</b>) low ATZ concentration. (<b>b</b>) high ATZ concentration.</p>
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17 pages, 3190 KiB  
Article
Untreated Opuntia ficus indica for the Efficient Adsorption of Ni(II), Pb(II), Cu(II) and Cd(II) Ions from Water
by Marcella Barbera, Serena Indelicato, David Bongiorno, Valentina Censi, Filippo Saiano and Daniela Piazzese
Molecules 2023, 28(9), 3953; https://doi.org/10.3390/molecules28093953 - 8 May 2023
Cited by 3 | Viewed by 1986
Abstract
The raw cladode of Opuntia ficus indica (OFI) was evaluated as a sustainable biosorbent for the removal of heavy metals (Ni, Pb, Cu, and Cd) from aqueous solutions. The functional groups of OFI were identified by employing DRIFT-FTIR and CP-MAS-NMR techniques before and [...] Read more.
The raw cladode of Opuntia ficus indica (OFI) was evaluated as a sustainable biosorbent for the removal of heavy metals (Ni, Pb, Cu, and Cd) from aqueous solutions. The functional groups of OFI were identified by employing DRIFT-FTIR and CP-MAS-NMR techniques before and after contact with the ions in an aqueous media, showing a rearrangement of the biomass structure due to the complexation between the metal and the functional groups. The adsorption process was studied in both single- and multi-component systems under batch conditions at different pHs (4.0, 5.0, and 6.0), different metal concentrations, and different biomass amounts. The results show that the raw OFI had a removal capacity at room temperature of over 80% for all metals studied after only 30 min of contact time, indicating a rapid adsorption process. Biosorption kinetics were successfully fitted by the pseudo-second-order equation, while Freundlich correctly modelled the biosorption data at equilibrium. The results of this work highlight the potential use of the untreated cladode of OFI as an economical and environmentally friendly biosorbent for the removal of heavy metals from the contaminated aqueous solution. Full article
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<p>DRIFT spectra of OFI biomass.</p>
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<p>DRIFT spectra of biomass before and after the contact with single- and multi-component ion solutions at pH 5. The violet line is the spectrum of the raw biomass; the blue line is the spectrum of the biomass in contact with the multi-component solution; and the pink, orange, red, and green lines are the spectra of the biomass in contact with solutions of Pb, Cu, Cd, and Ni, respectively.</p>
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<p>CP-NMR-MAS spectra of biomass before (blue line) and after contact with multi-elemental ion solution (red line).</p>
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<p>Sorption isotherm for a single-component system at 25 °C.</p>
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<p>The effect of contact time on OFI adsorption capacity in water solution at pHs 4.0, 5.0, and 6.0.</p>
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<p>Adsorption efficiency of biomass (0.1 mg) in single- (<bold>a</bold>,<bold>c</bold>) and multi-component (<bold>b</bold>,<bold>d</bold>) solutions as a function of metal concentrations after a contact time of 30 min. (<bold>a</bold>,<bold>b</bold>) are the results obtained at pH 4.0 and (<bold>c</bold>,<bold>d</bold>) at pH 5.0.</p>
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Review

Jump to: Research

24 pages, 2417 KiB  
Review
Application of Electrochemical Oxidation for Water and Wastewater Treatment: An Overview
by Mohammad Saleh Najafinejad, Simeone Chianese, Angelo Fenti, Pasquale Iovino and Dino Musmarra
Molecules 2023, 28(10), 4208; https://doi.org/10.3390/molecules28104208 - 20 May 2023
Cited by 21 | Viewed by 5152
Abstract
In recent years, the discharge of various emerging pollutants, chemicals, and dyes in water and wastewater has represented one of the prominent human problems. Since water pollution is directly related to human health, highly resistant and emerging compounds in aquatic environments will pose [...] Read more.
In recent years, the discharge of various emerging pollutants, chemicals, and dyes in water and wastewater has represented one of the prominent human problems. Since water pollution is directly related to human health, highly resistant and emerging compounds in aquatic environments will pose many potential risks to the health of all living beings. Therefore, water pollution is a very acute problem that has constantly increased in recent years with the expansion of various industries. Consequently, choosing efficient and innovative wastewater treatment methods to remove contaminants is crucial. Among advanced oxidation processes, electrochemical oxidation (EO) is the most common and effective method for removing persistent pollutants from municipal and industrial wastewater. However, despite the great progress in using EO to treat real wastewater, there are still many gaps. This is due to the lack of comprehensive information on the operating parameters which affect the process and its operating costs. In this paper, among various scientific articles, the impact of operational parameters on the EO performances, a comparison between different electrochemical reactor configurations, and a report on general mechanisms of electrochemical oxidation of organic pollutants have been reported. Moreover, an evaluation of cost analysis and energy consumption requirements have also been discussed. Finally, the combination process between EO and photocatalysis (PC), called photoelectrocatalysis (PEC), has been discussed and reviewed briefly. This article shows that there is a direct relationship between important operating parameters with the amount of costs and the final removal efficiency of emerging pollutants. Optimal operating conditions can be achieved by paying special attention to reactor design, which can lead to higher efficiency and more efficient treatment. The rapid development of EO for removing emerging pollutants from impacted water and its combination with other green methods can result in more efficient approaches to face the pressing water pollution challenge. PEC proved to be a promising pollutants degradation technology, in which renewable energy sources can be adopted as a primer to perform an environmentally friendly water treatment. Full article
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<p>(<b>a</b>) Classification and properties of active and non-active anodes (modified from Yang et al., 2020 [<a href="#B21-molecules-28-04208" class="html-bibr">21</a>]); (<b>b</b>) Type of electrode materials employed in different EO studies over the recent years.</p>
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<p>(<b>a</b>) Analysis of the effect of the electrolyte type on the EO process for removing pollutant, modified from Sanni et al. [<a href="#B34-molecules-28-04208" class="html-bibr">34</a>]); (<b>b</b>) Comparison of the performance of two electrolytes NaCl and Na<sub>2</sub>SO<sub>4</sub> on %COD removal with time, adapted from Ken et al. [<a href="#B35-molecules-28-04208" class="html-bibr">35</a>] with modification; (<b>c</b>) Effect of electrolyte concentration on COD removal efficiency, adapted from Ken et al. [<a href="#B35-molecules-28-04208" class="html-bibr">35</a>] with modification; (<b>d</b>) Effect of different electrolyte on %PNP removal with time, adapted from Wang et al. [<a href="#B36-molecules-28-04208" class="html-bibr">36</a>] with modification.</p>
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<p>The removal percentage of p-nitrophenol during electrochemical oxidation with different current densities, adapted from Wang et al. [<a href="#B36-molecules-28-04208" class="html-bibr">36</a>] with modification.</p>
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<p>(<b>a</b>) Effect of the temperature on removing COD/COD<sub>0</sub>, adapted from Panizza et al. [<a href="#B50-molecules-28-04208" class="html-bibr">50</a>] with modification; (<b>b</b>) Effect of the initial PFOS concentration on the decomposition ratios, adapted from Zhuo et al. [<a href="#B53-molecules-28-04208" class="html-bibr">53</a>] with modification; (<b>c</b>) Effect of gap distance between two plates and PFOA concentration, adapted from Ma et al. [<a href="#B54-molecules-28-04208" class="html-bibr">54</a>] with modification.</p>
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<p>Different AOPs and the ROS involved (modified from Rayaroth et al., 2022) [<a href="#B15-molecules-28-04208" class="html-bibr">15</a>].</p>
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<p>Electrochemical configurations: (<b>A</b>) Batch mode; (<b>B</b>) Flow-by mode; (<b>C</b>) Flow-through mode.</p>
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<p>Electrochemical configurations: (<b>A</b>) Batch mode; (<b>B</b>) Flow-by mode; (<b>C</b>) Flow-through mode.</p>
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