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Keywords = disinfection by-products (DBPs)

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17 pages, 1295 KiB  
Article
Optimization of Ozonation in Drinking Water Production at Lake Butoniga
by Marija Gregov, Jasenka Gajdoš Kljusurić, Davor Valinger, Maja Benković, Tamara Jurina, Ana Jurinjak Tušek, Vlado Crnek, Marin Matošić, Magdalena Ujević Bošnjak and Josip Ćurko
Water 2025, 17(1), 97; https://doi.org/10.3390/w17010097 - 1 Jan 2025
Viewed by 505
Abstract
This study focuses on optimizing the ozonation process in drinking water production from Lake Butoniga to ensure safe water quality while minimizing disinfection by-products (DBPs). Laboratory simulations were conducted using the Box–Behnken design to model the effects of ozone dose and treatment duration [...] Read more.
This study focuses on optimizing the ozonation process in drinking water production from Lake Butoniga to ensure safe water quality while minimizing disinfection by-products (DBPs). Laboratory simulations were conducted using the Box–Behnken design to model the effects of ozone dose and treatment duration on bromate formation, trihalomethanes (THMs), haloacetic acids (HAAs) and specific UV absorption (SUVA). Two ozonation strategies were tested: Strategy 1 aimed to minimize all DBPs, while Strategy 2 focused on controlling bromate levels while keeping THMs, HAAs and SUVA below 80% of maximum contaminant levels. Results showed that Strategy 2 reduced ozone consumption while maintaining water quality within regulatory standards, providing a cost-effective and environmentally sustainable treatment approach. Seasonal and depth-dependent variations in water quality had a significant impact on treatment efficiency and required adjustments to operational settings. The study also addressed discrepancies between laboratory and real plant results and suggested recalibration methods that improved the accuracy of model predictions. These results highlight the potential for integrating predictive modelling and dynamic treatment strategies into large-scale water treatment processes. Full article
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<p>Flowchart of strategies used for the modelling of ozonation optimization.</p>
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<p>Input parameters (ozone dose in PT (pretreatment) and MO (main ozonation), ozonation duration in MO) for Strategy 1 (<b>A</b>,<b>B</b>) and Strategy 2 (<b>C</b>,<b>D</b>) for different raw waters extracted at 6.7 m above the lake bottom (<b>A</b>,<b>C</b>) and 4 m above the lake bottom (<b>B</b>,<b>D</b>).</p>
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<p>Qualitative differences of the input and output parameters for different raw water extracted at 6.7 m above the lake bottom and 4 m above the lake bottom. Input parameters are optimal ozone dosing in pretreatment (PT) and main ozonation (MO) with output duration.</p>
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12 pages, 2690 KiB  
Article
Perborate Activated Peroxymonosulfate Process for Improving the Coagulation Efficiency of Microcystis aeruginosa by Polymeric Aluminum Chloride
by Fan Chen, Lu Li, Shunfan Qiu, Shiyang Chen, Lingfang Yang, Lin Deng and Zhou Shi
Molecules 2024, 29(22), 5352; https://doi.org/10.3390/molecules29225352 - 14 Nov 2024
Viewed by 570
Abstract
In this study, the sodium perborate (SP)-activated peroxymonosulfate (PMS) process was used to enhance the coagulation efficiency of cyanobacteria with polymeric aluminum chloride (PAC), aiming to efficiently mitigate the impact of algal blooms on the safety of drinking water production. The optimal concentrations [...] Read more.
In this study, the sodium perborate (SP)-activated peroxymonosulfate (PMS) process was used to enhance the coagulation efficiency of cyanobacteria with polymeric aluminum chloride (PAC), aiming to efficiently mitigate the impact of algal blooms on the safety of drinking water production. The optimal concentrations of SP, PMS, and PAC were determined by evaluating the removal rate of OD680 and zeta potential of the algae. Experimental results demonstrated that the proposed ternary PMS/SP/PAC process achieved a remarkable OD680 removal efficiency of 95.2%, significantly surpassing those obtained from individual treatments with PMS (19.5%), SP (5.2%), and PAC (42.1%), as well as combined treatments with PMS/PAC (55.7%) and PMS/SP (28%). The synergistic effect of PMS/SP/PAC led to the enhanced aggregation of cyanobacteria cells due to a substantial reduction in their zeta potential. Flow cytometry was performed to investigate cell integrity before and after treatment with PMS/SP/PAC. Disinfection by-products (DBPs) (sodium hypochlorite disinfection) of the algae-laden water subsequent to PMS/SP/PAC treatment declined by 57.1%. Moreover, microcystin-LR was completely degraded by PMS/SP/PAC. Electron paramagnetic resonance (EPR) analysis evidenced the continuous production of SO4, •OH, 1O2, and O2, contributing to both cell destruction and organic matter degradation. This study highlighted the significant potential offered by the PMS/SP/PAC process for treating algae-laden water. Full article
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<p>Comparison of different processes on cyanobacteria removal (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM, PAC dosage: 10 mg/L).</p>
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<p>Effect of SP and PMS dosage on cyanobacteria removal using PMS/SP/PAC treatment (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, PAC dosage: 10 mg/L).</p>
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<p>Effect of PAC dosage on cyanobacteria removal using PMS/SP/PAC treatment (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM).</p>
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<p>Cell integrity of algae treated with (<b>a</b>) control, (<b>b</b>) PAC, (<b>c</b>) PMS/PAC, and (<b>d</b>) PMS/SP/PAC (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM, PAC dosage: 10 mg/L).</p>
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<p>DBP yield from different treatments of cyanobacteria under chlorination in DI water (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM, PAC dosage: 10 mg/L).</p>
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<p>Microcystin-LR elimination using different treatment processes in the removal of cyanobacteria (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM, PAC dosage: 10 mg/L).</p>
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<p>The EPR spectra of (<b>a</b>) DMPO−OH and DMPO−SO<sub>4</sub> adducts, (<b>b</b>) DMPO−<math display="inline"><semantics> <mrow> <msubsup> <mrow> <mi mathvariant="normal">O</mi> </mrow> <mrow> <mn>2</mn> </mrow> <mrow> <mo>•</mo> <mo>−</mo> </mrow> </msubsup> </mrow> </semantics></math> adducts, and (<b>c</b>) TEMP−<sup>1</sup>O<sub>2</sub> adducts (initial algal cell density: 5.0 × 10<sup>6</sup> cells/mL, SP dosage: 1 mM, PMS dosage: 3 mM, PAC dosage: 10 mg/L, [DMPO] = [TEMP] = 100 mM).</p>
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14 pages, 2493 KiB  
Article
Characterization of Disinfection By-Products Originating from Residual Chlorine-Based Disinfectants in Drinking Water Sources
by Dongmei Yang, Jiale Huang, Fenli Min, Huixian Zhong, Jialu Ling, Qun Kang, Zhaohua Li and Lilian Wen
Toxics 2024, 12(11), 808; https://doi.org/10.3390/toxics12110808 - 9 Nov 2024
Viewed by 955
Abstract
In this study, samples from the Yangtze River, Han River, and Liangzi Lake in Wuhan City were utilized to characterize the formation of disinfection by-products (DBPs) from chlorine-based disinfection residues in drinking water sources. The results indicated that the main DBPs in drinking [...] Read more.
In this study, samples from the Yangtze River, Han River, and Liangzi Lake in Wuhan City were utilized to characterize the formation of disinfection by-products (DBPs) from chlorine-based disinfection residues in drinking water sources. The results indicated that the main DBPs in drinking water sources were trichloromethane (TCM) and trichloroacetic acid (TCAA). The generation of DBPs was significantly positively correlated with oxidative substances, aromatic compounds, pH, and ammonia nitrogen (NH3-N) content in the water. The concentration of TCAA increased from 0 to 2.45 ± 0.31 mg/L when the reaction time increased to 72 h. As the NaClO concentration increased from 5 mg/L to 15 mg/L, the concentrations of TCAA, TBM, and DCAN increased from 2.03 ± 0.04 mg/L, 0 mg/L, and 0 mg/L to 2.49 ± 0.34 mg/L, 0.21 ± 0.07 mg/L, and 0.10 ± 0.04 mg/L before decreasing to 1.75 ± 0.19 mg/L, 0.17 ± 0.07 mg/L, and 0.04 ± 0.05 mg/L, respectively. The orthogonal experimental results showed that Br, NH3-N, and pH all had significant influences on the TCM generation, whereas temperature affected the formation of TCAA in the Han River. This work reveals the factors influencing the generation of DBPs from chlorine-based disinfection residues, offering a prevention and control method for DBPs in drinking water sources from a theoretical perspective. Full article
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<p>Distribution map of drinking water sources in Wuhan.</p>
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<p>Correlation analysis (<b>a</b>) and principal component analysis (<b>b</b>) of disinfection by-products (DBPs) with water quality parameters. In Figure (<b>a</b>), blue and orange indicate positive and negative correlations between the two factors, respectively. The larger the circle, the stronger the correlation, while the smaller the circle, the weaker the correlation. TOCl is total organic chlorine, TCAA is trichloroacetic acid, and SUV<sub>254</sub> is spectral UV absorption at 254 nm. In Figure (<b>b</b>), CG, HG, and LG mean samples in glass bottles from the Yangtze River, Han River, and the Liangzi Lake, respectively, while CP, HP, and LP mean samples in polyethylene bottles from the Yangtze River, Han River, and the Liangzi Lake, respectively. Variables with arrows pointing in the same direction have a positive correlation on principal components, while variables pointing in the opposite direction have a negative correlation. The length of the arrow represents the variance contribution of the variable, and the longer the length, the greater the explanatory power of the variable on the principal component.</p>
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<p>The time course of concentrations of DBPs under the condition of 10 mg/L chlorine and 10 μmol/L Br<sup>−</sup> at 20 °C. TCM-L, TCM-H, and TCM-C mean trichloromethane (TCM) in Liangzi Lake, Han River, and Yangtze River, respectively, while TCAA-L, TCAA-H, and TCAA-C mean trichloroacetic acid (TCAA) in Liangzi Lake, Han River, and Yangtze River, respectively.</p>
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<p>Effect of chlorine concentrations and water sources on the formation of disinfection by-products (DBPs) under the dark condition of 10 μmol/L Br<sup>−</sup> at 20 °C for 24 h. 5-TCM, 10-TCM, and 15-TCM mean that the concentrations of trichloromethane (TCM) are 5 mg/L, 10 mg/L, and 15 mg/L respectively, while 5-TCAA, 10-TCAA, and 15-TCAA mean that the concentrations of trichloroacetic acid (TCAA) are 5 mg/L, 10 mg/L, and 15 mg/L respectively. 5-TBM, 10-TBM, and 15-TBM mean that the concentrations of tribromomethane (TBM) are 5 mg/L, 10 mg/L, and 15 mg/L respectively, while 5-DCAN, 10-DCAN, and 15-DCAN mean that the concentrations of dichloroacetonitrile (DCAN) are 5 mg/L, 10 mg/L, and 15 mg/L respectively.</p>
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22 pages, 7889 KiB  
Article
Magnesium Bicarbonate–Walnut Shell Dual-Template Synthesis of Multifunctional Layered Porous Carbon for Enhanced Adsorption of Aqueous Chlorinated Organic Compounds
by Juanxue Kang, Xiaoli Bai, Junyang Leng, Yaxuan Lou, Daomei Chen, Liang Jiang and Jiaqiang Wang
Int. J. Mol. Sci. 2024, 25(21), 11761; https://doi.org/10.3390/ijms252111761 - 1 Nov 2024
Viewed by 649
Abstract
Chloride ions readily react with organic matter and other ions, resulting in the formation of disinfection by-products (DBPs) that exhibit heightened levels of toxicity, carcinogenicity, and mutagenicity. This study creatively employed waste walnut shells as self-templates and low-cost magnesium bicarbonate as a rigid [...] Read more.
Chloride ions readily react with organic matter and other ions, resulting in the formation of disinfection by-products (DBPs) that exhibit heightened levels of toxicity, carcinogenicity, and mutagenicity. This study creatively employed waste walnut shells as self-templates and low-cost magnesium bicarbonate as a rigid template to successfully synthesize multifunctional porous carbon derived from walnut shells. Employing a series of characterization techniques, it was ascertained that the porous carbon material (WSC/Mg) synthesized via the dual-template method exhibited a distinct layered microscopic surface structure, with a predominance of C and O elements on the surface. The material displayed a high degree of graphitization, significant specific surface area, and abundant oxygen-containing surface functional groups. The incorporation of magnesium bicarbonate as a hard template improved the structure of the walnut shell porous carbon, resulting in a significant enhancement in mass transfer efficiency for the target product on the adsorbent and a substantial improvement in removal efficiency. In comparison with walnut shell-derived carbon using only self-templating, WSC/Mg exhibited a 17.26-fold increase in adsorption capacity for 2,4-dichlorophenol. Furthermore, even after four adsorption–desorption cycles, WSC/Mg-12 maintained an adsorption efficiency above 90%. It is remarkable that WSC/Mg-12 demonstrated exceptional resistance to interference from natural organic matter and pH variations. Moreover, the adsorbed saturated WSC/Mg-12 effectively treated real coke wastewater, resulting in an 80% color removal rate, 20% COD removal rate, and 15% ammonia nitrogen removal rate. In conclusion, this study presents an innovative approach for cost-effective and versatile porous carbon materials with extensive applications in water environment purification and biomass utilization. Full article
(This article belongs to the Section Materials Science)
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<p>SEM images of (<b>a</b>) WSC; (<b>b</b>) WSC/Mg-21; (<b>c</b>) WSC/Mg-11; (<b>d</b>,<b>e</b>) WSC/Mg-12; and (<b>f</b>) WSC/Mg-13. (<b>g</b>) Element mapping of WSC/Mg-12.</p>
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<p>(<b>a</b>) FT-IR and (<b>b</b>) Raman spectra of WSC, WSC/Mg-21, WSC/Mg-11, WSC/Mg-12, and WSC/Mg-13.</p>
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<p>(<b>a</b>) N<sub>2</sub> adsorption–desorption curves; (<b>b</b>) pore size distribution of WSC, WSC/Mg-21, WSC/Mg-11, WSC/Mg-12, and WSC/Mg-13.</p>
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<p>(<b>a</b>) XPS; (<b>b</b>) C1s of WSC; (<b>c</b>) C1s of WSC/Mg-21; (<b>d</b>) C1s of WSC/Mg-11; (<b>e</b>) C1s of WSC/Mg-12; (<b>f</b>) C1s of WSC/Mg-13.</p>
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<p>(<b>a</b>) The effect of different materials; (<b>b</b>) the effect of dosage in 2,4-DCP on WSC/Mg-12.</p>
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<p>(<b>a</b>) The relationship between the duration of adsorption and the amount of adsorption; (<b>b</b>) pseudo-first order model; (<b>c</b>) pseudo-second order model; (<b>d</b>) intra-particle diffusion model of WSC/Mg-12.</p>
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<p>Adsorption isothermal models of WSC/Mg-12: (<b>a</b>) Langmuir; (<b>b</b>) Freundlich; (<b>c</b>) Temkin; (<b>d</b>) Sips.</p>
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<p>(<b>a</b>) Raman spectra, (<b>b</b>) FT-IR spectra, and (<b>c</b>) XPS of WSC-12 (used); (<b>d</b>) C1s, (<b>e</b>) O1s, and (<b>f</b>) Cl2p of WSC-12 (used).</p>
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<p>(<b>a</b>) 10,000× and (<b>b</b>) 100,000× SEM images of WSC-12 (used); (<b>c</b>) mapping of WSC-12 (used).</p>
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<p>Schematic illustration of possible adsorption mechanism.</p>
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<p>Adsorption of 2,4-DCP in different water samples.</p>
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<p>Recyclability of WSC/Mg-12.</p>
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<p>Comparison of coking wastewater pre-adsorption and post-adsorption.</p>
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<p>Schematic representation of WSC/Mg preparation procedure.</p>
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16 pages, 1554 KiB  
Article
Trihalomethane Formation Potential at the Barekese Water Treatment Plant and the Related Cancer Risk to Consumers in the Kumasi Metropolis of Ghana
by Nathaniel Kabral Wezenamo Fellalaga, Lawson Mensah, Bright Kwaku Agbekey, Ethel Bentil, Lilian Waaley and Geophery Kwame Anornu
Water 2024, 16(21), 3089; https://doi.org/10.3390/w16213089 - 29 Oct 2024
Viewed by 832
Abstract
The prevalence of disinfection by-products in drinking water supplies is a global concern due to their carcinogenicity. However, the monitoring of DBPs such as trihalomethanes (THMs) and haloacetic acids (HAAs) in drinking water supplies is non-existent in many developing Asian, South American, and [...] Read more.
The prevalence of disinfection by-products in drinking water supplies is a global concern due to their carcinogenicity. However, the monitoring of DBPs such as trihalomethanes (THMs) and haloacetic acids (HAAs) in drinking water supplies is non-existent in many developing Asian, South American, and African countries. The formation of THMs during disinfection arises from a reaction between the disinfectant and natural organic matter in the water, particularly, dissolved organic carbon (DOC). This reaction is hastened by increases in temperature, high levels of disinfectant doses or residual, elevated water pH, long disinfection contact times, and high DOC concentrations. However, the inclusion of a granular activated carbon adsorption process in the water treatment process is the most effective method for the removal of the main precursor (DOC) for the formation of THMs in treated water. The Barekese WTP, which disinfects with chlorine, has no adsorption process for DOC removal, and supplies over 80% of pipe-borne water to the city of Kumasi in Ghana, was assessed for the THM formation potential (THMFP). A THM predictive model was used to determine the potential THM concentration in the final water. The THMFP at the Barekese WTP ranged between 22.42 and 38.94 µg/L, which was below the 100 µg/L threshold set by the WHO. The lifetime average daily doses were 3.9494 × 10−4 µg/Kg/d and 3.9294 × 10−4 µg/Kg/d for male and female consumers, respectively. The lifetime integrative cancer risks associated with consumption of the water were 1.817 × 10−5 and 1.808 × 10−5 for males and females, respectively. The cancer risk posed was acceptably low. However, direct measurement of DBPs is required to corroborate these findings and verify the cancer risk posed to the consumers of treated water from the Barekese WTP to inform policies, regulations, public health interventions, and investment. Full article
(This article belongs to the Section Water and One Health)
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<p>Map of the study area.</p>
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<p>Schematic of the Barekese water treatment plant.</p>
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<p>Linear regression of the relationships between water quality parameters and THM concentration.</p>
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15 pages, 7269 KiB  
Article
Combined Toxic Effects and Mechanisms of Chloroacetic Acid and N-Nitrosodimethylamine on Submerged Macrophytes
by Kaili Huang, Haiqing Huang, Xuhui Huang, An Lao, Zheng Zheng and Hanqi Wu
Water 2024, 16(18), 2689; https://doi.org/10.3390/w16182689 - 21 Sep 2024
Viewed by 985
Abstract
Disinfection by-products (DBPs) such as chloroacetic acids (CAAs) and N-Nitrosodimethylamine (NDMA) are prevalent pollutants in surface waters, particularly with the increasing use of chlorine-based disinfectants. The entry of these DBPs into water bodies may increase accordingly, posing ecological risks to aquatic life. To [...] Read more.
Disinfection by-products (DBPs) such as chloroacetic acids (CAAs) and N-Nitrosodimethylamine (NDMA) are prevalent pollutants in surface waters, particularly with the increasing use of chlorine-based disinfectants. The entry of these DBPs into water bodies may increase accordingly, posing ecological risks to aquatic life. To assess the toxic effects of CAAs and NDMA on submerged macrophytes, Vallisneria natans was exposed to different concentrations of CAAs (1.0, 10.0, and 100.0 μg L−1) and NDMA (0.1, 1.0, and 10.0 μg L−1). A RI value of <1 indicates that simultaneous exposure to CAAs and NDMA can produce an antagonistic effect. Both CAAs and NDMA adversely affect the photosynthetic system of plants. In the NDMA treatment group, chlorophyll a content decreases with increasing concentration, accounting for 96.03%, 60.80%, and 58.67% of the CT group, respectively. Additionally, it effectively triggers the plant’s antioxidant response, with significant increases in SOD, POD, and GSH levels. Among these, the combined treatment group AN2 (10 + 1 μg L−1) showed the most significant change in SOD activity, reaching 3.57 times that of the CT group. Ultrastructural changes also revealed stress responses in leaf cells and damage to organelles. Furthermore, metabolomics provided insights into the metabolic responses induced by CAAs or NDMA in V. natans leaves, where the composition and metabolism of lipids, fatty acids, cofactors and vitamins, amino acids, nucleotides, and some antioxidants were regulated, affecting plant growth. This study provides preliminary information for the ecological risk assessment of submerged plants by complex contamination with the disinfection by-products CAA and NDMA. Full article
(This article belongs to the Section Biodiversity and Functionality of Aquatic Ecosystems)
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<p>Variations in growth and photosynthetic characteristics of <span class="html-italic">V. natans</span> when exposed to CAA, NDMA, and their combination. Increased root length (<b>a</b>); Increased leaf length (<b>b</b>); Increased biomass (<b>c</b>); Contents of Chl a (<b>d</b>); Chl b (<b>e</b>); Chl (a + b) (<b>f</b>). Different lowercase letters such as a, b, c, and d indicate statistically significant differences between treatments (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Variations in the <span class="html-italic">V. natans</span> leaf antioxidant system when exposed to CAA, NDMA, and their combination. SOD (<b>a</b>), POD (<b>b</b>), CAT (<b>c</b>), GSH (<b>d</b>), MDA (<b>e</b>), TP (<b>f</b>). Different lowercase letters such as a, b, c, and d indicate statistically significant differences between treatments (<span class="html-italic">p</span> &lt; 0.05).</p>
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<p>Variations in the ultrastructure of <span class="html-italic">V. natans</span> subjected to CAA and NDMA. Chloroplast (CH), nucleolus (N), plasmolysis (PL), cell wall (CW), osmiophilic granules (OG), starch (ST), and lysosomes (LY).</p>
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<p>(<b>a</b>) Metabolite identification from all samples were analyzed. (<b>b</b>) Volcano plots illustrating differentially expressed metabolites (DEMs). FC: fold change. Positive values of log2 fold change represent upregulated DEMs, indicated by red dots, while negative values represent downregulated DEMs, indicated by blue dots. (<b>c</b>) OPLS-DA score plots. Score [PC1] and other score [OC2] correspond to principal components 1 and 2, respectively. The distribution of samples in the plot indicates the extent of metabolite differences between groups.</p>
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<p>(<b>a</b>) Alterations in the essential antioxidant composition within <span class="html-italic">V. natans</span> leaves were observed. Between groups * indicates the significance of the difference between the four groups, <span class="html-italic">p</span> &lt; 0.05. (<b>b</b>–<b>e</b>) Enrichment analysis of altered metabolites in <span class="html-italic">V. natans</span> leaves subjected to CAA and NDMA exposure. The X-axis denotes the rich factor, while the Y-axis signifies the pathway names. The size of the bubbles corresponds to the quantity of DEGs involved, and the closer the bubbles are to brown, the higher the degree of enrichment in metabolic pathways.</p>
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29 pages, 2161 KiB  
Review
Innovative Approaches for Minimizing Disinfection Byproducts (DBPs) in Water Treatment: Challenges and Trends
by Spyridon K. Golfinopoulos, Anastasia D. Nikolaou and Dimitrios E. Alexakis
Appl. Sci. 2024, 14(18), 8153; https://doi.org/10.3390/app14188153 - 11 Sep 2024
Viewed by 2954
Abstract
Growing concerns over public health and environmental safety have intensified the focus on minimizing harmful disinfection byproducts (DBPs) in water treatment. Traditional methods like chlorination, while effective against pathogens, often lead to the formation of DBPs, which pose significant risks. This paper explores [...] Read more.
Growing concerns over public health and environmental safety have intensified the focus on minimizing harmful disinfection byproducts (DBPs) in water treatment. Traditional methods like chlorination, while effective against pathogens, often lead to the formation of DBPs, which pose significant risks. This paper explores alternative strategies to reducing DBP formation while ensuring effective disinfection. The methodology involved a bibliographic study conducted through the Scopus platform, using appropriate keywords. The initial search yielded 9576 articles from the period 2020 to 2024. The key approaches identified include advanced oxidation processes (AOPs) such as UV/H2O2 and ozone, which mineralize natural organic matter (NOM) and minimize chemical use and sludge production; membrane-based filtration systems, like reverse osmosis, effectively removing contaminants without chemical disinfectants, reducing DBP risks. Furthermore, conventional processes, such as coagulation and filtration, serve as crucial pretreatment steps to lower NOM levels before disinfection. Additionally, optimizing chlorine dosing, using non-chlorine disinfectants, and employing post-disinfection methods like adsorption and biological filtration further mitigate DBP formation. Finally, the integration of artificial intelligence in process optimization is emerging as a promising tool for enhancing treatment efficiency and safety. This research contributes to the development of safer, more sustainable water treatment solutions, addressing regulatory demands and public health objectives. Full article
(This article belongs to the Special Issue New Approaches to Water Treatment: Challenges and Trends)
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<p>Number of articles covering the years 2020–2024 returned for each searched keyword.</p>
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<p>Sedimentation tank.</p>
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<p>Sand filtration beds.</p>
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<p>GAC filter adsorber.</p>
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<p>Sedimentation tank effluent.</p>
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5 pages, 2122 KiB  
Proceeding Paper
A Comprehensive Virtual Testbed for Modeling Disinfection Byproduct Formation in Water Distribution Networks
by Pavlos Pavlou, Marios Kyriakou, Stelios G. Vrachimis and Demetrios G. Eliades
Eng. Proc. 2024, 69(1), 33; https://doi.org/10.3390/engproc2024069033 - 2 Sep 2024
Viewed by 379
Abstract
Drinking water disinfection by water utilities aims to ensure the safety and high quality of the provided water; however, it can pose a threat to human health due to the formation of disinfection byproducts (DBPs). The prediction and modeling of DBPs are challenging [...] Read more.
Drinking water disinfection by water utilities aims to ensure the safety and high quality of the provided water; however, it can pose a threat to human health due to the formation of disinfection byproducts (DBPs). The prediction and modeling of DBPs are challenging tasks due to the complex reactions within water distribution networks (WDN). To address this challenge, we introduce a virtual testbed based on a realistic WDN in Cyprus that utilizes the EPANET and EPANET-MSX engines to model multi-species reactions for the execution of simulation experiments under various conditions regarding the formation and fate of two families of DBPs within WDNs. Full article
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<p>Diagram illustrating the architecture of the CY-DBP virtual testbed.</p>
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<p>Simulated THM concentration bounds (red lines) at three locations, indicating the range in which this parameter may vary (blue area).</p>
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<p>Simulated HAA concentration bounds (red lines) at three locations, indicating the range in which this parameter may vary (blue area).</p>
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<p>Maximum THM (<b>left</b>) and HAA (<b>right</b>) concentration per node in μg/L. Sensors exist at numbered points: (1) re-chlorination tank; (2) DMA entrance; (3) DMA point.</p>
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11 pages, 1350 KiB  
Article
The Selectively Nontargeted Analysis of Halogenated Disinfection Byproducts in Tap Water by Micro-LC QTOFMS
by Jing Wu, Yulin Zhang, Qiwei Zhang, Fang Tan, Qiongyu Liu and Xiaoqiu Yang
Toxics 2024, 12(9), 630; https://doi.org/10.3390/toxics12090630 - 26 Aug 2024
Viewed by 733
Abstract
With the rapid development of society, more and more unknown halogenated disinfection byproducts (DBPs) enter into drinking water and pose potential risks to humans. To explore the unknown halogenated DBPs in tap water, a selectively nontargeted analysis (SNTA) method was developed by conducting [...] Read more.
With the rapid development of society, more and more unknown halogenated disinfection byproducts (DBPs) enter into drinking water and pose potential risks to humans. To explore the unknown halogenated DBPs in tap water, a selectively nontargeted analysis (SNTA) method was developed by conducting micro-liquid chromatography coupled with quadrupole time-of-flight mass spectrometry (micro-LC-QTOFMS). In this method, two runs were employed: in the first run, the modes of TOFMS and precursor ion (the fragments were set as Cl35/Cl37, Br79/Br81, and I126.9) were performed, and the molecular ions or precursor ions of the halogenated organics could be obtained; in the second run, the product ion mode was conducted by setting the molecular ion screened above, and the MS/MS spectrums could be acquired to speculate concerning the structure. Two kinds of model DBPs (one kind had an aliphatic structure and the other was an aromatic compound) were used to optimize the parameters of the MS, and their MS characteristics were summarized. With this SNTA method, 15 halogenated DBPs were screened in two tap water samples and their structures were proposed. Of them, six DBPs had not been reported before and were assumed to be new DBPs. Overall, the detected halogenated DBPs were mostly acidic substances. Full article
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<p>Optimization of delustering potential (DP) in <span class="html-italic">TOFMS</span> mode: (<b>A</b>) haloacetic acids—CAA: monochloroacetic acid; TCAA: trichloroacetic acid; DCAA: dichloroacetic acid; BAA: monobromoacetic acid; DBAA: dibromoacetic acid; IAA: monodiodoacetic acid; and BIAA: bromodiodoacetic acid; DIAA: diiodoacetic acid; and (<b>B</b>) halophenols and halobenzoquinones—2-MIBQ: 2-monoiodobenzoquinone; 2,3-DB-5,6-DMBQ: 2,3-dibromo-5,6-dimethylbenzoquinoen; Tetra C-1,2-BQ: tetrachloro-1,2-benzoquinone; 2-MCBQ: 2-monochlorobenzoquinone; 2,4-DCP: 2,4-dichlorophenol; and 2,4,6-TCP: 2,4,6-trichlorophenol.</p>
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<p>Optimization of collision energy (CE) in <span class="html-italic">product ion</span> mode: (<b>A</b>) haloacetic acids, and (<b>B</b>) halophenols and halobenzoquinones.</p>
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<p>Proposed structure and fragmentation scheme for ion cluster 300.8473/302.8407.</p>
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24 pages, 30669 KiB  
Article
Maximizing N-Nitrosamine Rejection via RO Membrane Plugging with Hexylamine and Hexamethylenediamine
by Silvia Morović, Katarina Marija Drmić, Sandra Babić and Krešimir Košutić
Nanomaterials 2024, 14(13), 1117; https://doi.org/10.3390/nano14131117 - 28 Jun 2024
Viewed by 1212
Abstract
The rapid expansion of urban areas and the increasing demand for water resources necessitate substantial investments in technologies that enable the reuse of municipal wastewater for various purposes. Nonetheless, numerous challenges remain, particularly regarding disinfection by-products (DBPs), especially carcinogenic compounds such as N [...] Read more.
The rapid expansion of urban areas and the increasing demand for water resources necessitate substantial investments in technologies that enable the reuse of municipal wastewater for various purposes. Nonetheless, numerous challenges remain, particularly regarding disinfection by-products (DBPs), especially carcinogenic compounds such as N-nitrosamines (NTRs). To tackle the ongoing issues associated with reverse osmosis (RO) membranes, this study investigated the rejection of NTRs across a range of commercially available RO membranes. In addition, the research aimed to improve rejection rates by integrating molecular plugs into the nanopores of the polyamide (PA) layer. Hexylamine (HEX) and hexamethylenediamine (HDMA), both linear chain amines, have proven to be effective as molecular plugs for enhancing the removal of NTRs. Given the environmental and human health concerns associated with linear amines, the study also aimed to assess the feasibility of diamine molecules as potential alternatives. The application of molecular plugs led to changes in pore size distribution (PSD) and effective pore number, resulting in a decrease in membrane permeability (from 5 to 33%), while maintaining levels suitable for RO processes. HEX and HDMA exhibited a positive effect on NTR rejection with ACM1, ACM5 and BW30LE membranes. In particular, NDMA rejection, the smallest molecule of the tested NTRs, with ACM1 was improved by 65.5% and 70.6% after treatment with HEX and HDMA, respectively. Full article
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<p>Schematic representation of the RO set up. H: hold-up tank, VP: high pressure pump, M: manometer, BPR: back pressure regulator, C: membrane cells. F, P and R stand for feed, permeate and retentate streams, respectively. The blue arrows represent the permeate stream.</p>
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<p>Pure water permeability of selected pristine and modified RO membranes. The error bars indicate the average values and the range of duplicated results.</p>
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<p>NaCl rejection rates for specific RO membranes. The error bars show the mean values and the variation range of the duplicated results.</p>
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<p>Rejection rates of (<b>a</b>) NDMA, (<b>b</b>) NDEA, (<b>c</b>) NMOR and (<b>d</b>) NPIP for pristine and modified RO membranes.</p>
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<p>Water contact angle for pristine and modified RO membranes. The error bars show the mean values and the variation range of at least 10 measurements.</p>
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<p>Infrared spectra of pristine and modified RO membranes; (<b>a</b>) ACM1, (<b>b</b>) ACM5, (<b>c</b>) BW30LE, (<b>d</b>) UTC73AC and (<b>e</b>) XLE.</p>
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<p>SEM micrographs of pristine (<b>a</b>) ACM1, (<b>d</b>) ACM5, (<b>g</b>) BW30LE, (<b>j</b>) UTC73AC, and (<b>m</b>) XLE; HEX-treated (<b>b</b>) ACM1, (<b>e</b>) ACM5, (<b>h</b>) BW30LE, (<b>k</b>) UTC73AC, and (<b>n</b>) XLE; and HDMA-treated (<b>c</b>) ACM1, (<b>f</b>) ACM5, (<b>i</b>) BW30LE, (<b>l</b>) UTC73AC, and (<b>o</b>) XLE membrane surfaces.</p>
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<p>SEM micrographs of pristine (<b>a</b>) ACM1, (<b>d</b>) ACM5, (<b>g</b>) BW30LE, (<b>j</b>) UTC73AC, and (<b>m</b>) XLE; HEX-treated (<b>b</b>) ACM1, (<b>e</b>) ACM5, (<b>h</b>) BW30LE, (<b>k</b>) UTC73AC, and (<b>n</b>) XLE; and HDMA-treated (<b>c</b>) ACM1, (<b>f</b>) ACM5, (<b>i</b>) BW30LE, (<b>l</b>) UTC73AC, and (<b>o</b>) XLE membrane surfaces.</p>
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<p>Pore size distribution of pristine and modified RO membranes: (<b>a</b>) ACM1, (<b>b</b>) ACM5, (<b>c</b>) BW30LE, (<b>d</b>) UTC73AC, and (<b>e</b>) XLE.</p>
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<p>Rejection of NTRs by the selected pristine RO membrane as a function of MPA.</p>
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<p>The rejection of NDMA and 1,3-dioxolane for selected pristine RO membranes.</p>
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<p>Schematic representation of molecular plugging in PA-RO membranes.</p>
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<p>Relative change in water permeability and rejection of NDMA and 1,3-dioxolane after treatment with (<b>A</b>) HEX and (<b>B</b>) HDMA.</p>
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<p>The rejection of 1,3-dioxolane and the pure water permeability of the (<b>A</b>) HEX- and (<b>B</b>) HDMA-plugged RO membranes over a 100-h period. The error bars indicate the mean values and ranges of the duplicated separation results.</p>
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19 pages, 5177 KiB  
Article
UV/Advanced Oxidation Process for Removing Humic Acid from Natural Water: Comparison of Different Methods and Effect of External Factors
by Qingchao Shen, Xiaosan Song, Jishuo Fan, Cheng Chen and Zhuohao Li
Water 2024, 16(13), 1815; https://doi.org/10.3390/w16131815 - 26 Jun 2024
Viewed by 1432
Abstract
Humic acid (HA) is an organic compound naturally present in aquatic environments. It has been found to have detrimental effects on water color, the transport of heavy metals, and the elimination of disinfection by-products (DBPs), thereby exerting an impact on human health. This [...] Read more.
Humic acid (HA) is an organic compound naturally present in aquatic environments. It has been found to have detrimental effects on water color, the transport of heavy metals, and the elimination of disinfection by-products (DBPs), thereby exerting an impact on human health. This study introduced four synergistic ultraviolet/advanced oxidation processes (UV/AOPs) systems aimed at eliminating HA from water. The research explored the effect of solution pH, duration of illumination, initial reactant concentration, and oxidant concentration on the degradation of HA. The results indicated that the mineralization rate achieved by individual UV or oxidant systems was less than 15%, which is significantly lower compared to UV/AOPs systems. Among these methods, the UV/peroxymonosulfate (UV/PMS) process demonstrated the highest effectiveness, achieving a mineralization rate of 94.15%. UV/peroxydisulfate (UV/PDS) and UV/sodium percarbonate (SPC) were subsequently implemented, with UV/sulfite (S(IV)) demonstrating the lowest effectiveness at 19.8%. Optimal degradation efficiency was achieved when the initial concentration of HA was 10 mg/L, the concentration of PMS was 3 mmol/L, and the initial pH was set at 5, with an illumination time of 180 min. This experimental setup resulted in high degradation efficiencies for chemical oxygen demand (COD), UV254, and HA, reaching 96.32%, 97.34%, and 92.09%, respectively. The energy efficiency of this process (EE/O) was measured at 0.0149 (kWh)/m3, indicating the capability of the UV/PMS system to efficiently degrade and mineralize HA in water. This offers theoretical guidance for the engineered implementation of a UV/PAM process in the treatment of HA. Full article
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<p>Structure of the advanced oxidation reaction device.</p>
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<p>Diagram of the experimental setup: (<b>a</b>) advanced oxidation reaction setup; (<b>b</b>) UV lamp.</p>
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<p>Degradation of HA by isolated UV, isolated PMS, and UV/PMS.</p>
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<p>Activation of PMS through electron and energy transfer processes [<a href="#B29-water-16-01815" class="html-bibr">29</a>].</p>
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<p>Degradation of HA by isolated UV, isolated PDS, and UV/PDS.</p>
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<p>Activation of PDS through electron and energy transfer processes [<a href="#B29-water-16-01815" class="html-bibr">29</a>].</p>
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<p>Degradation of organic matter by isolated UV, isolated SPC, and UV/SPC.</p>
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<p>Degradation of organic matter by isolated UV, isolated S(IV), and UV/S(IV).</p>
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<p>Mineralization effects of different processes on HA.</p>
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<p>Degradation effects of organic matter by different synergistic processes.</p>
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<p>Effect of initial solution pH on degradation of HA in UV/PMS.</p>
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<p>Effect of illumination time on degradation efficiency of organic matter.</p>
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<p>Actual images of HA degradation process solutions from 0 min to 120 min.</p>
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<p>Effect of PMS concentration on degradation efficiency of organic matter.</p>
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<p>Effect of substrate concentration on degradation efficiency of organic matter.</p>
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16 pages, 2129 KiB  
Article
Adsorption Behavior and Mechanisms of Trihalomethanes onto Virgin and Weathered Polyvinyl Chloride Microplastics
by Yi Li, Paragi Neema and Susan Andrews
Toxics 2024, 12(7), 450; https://doi.org/10.3390/toxics12070450 - 22 Jun 2024
Cited by 1 | Viewed by 890
Abstract
Microplastics that adsorb various toxic contaminants in water may be transported into cells and organs, possibly posing toxicological risks in the aquatic environment. Disinfection byproducts (DBPs), which are ubiquitous in chlorinated drinking water and wastewater, may have some potential to sorb onto microplastics [...] Read more.
Microplastics that adsorb various toxic contaminants in water may be transported into cells and organs, possibly posing toxicological risks in the aquatic environment. Disinfection byproducts (DBPs), which are ubiquitous in chlorinated drinking water and wastewater, may have some potential to sorb onto microplastics (MPs) through hydrophobic or electrostatic interactions. However, DBP adsorption on microplastics has not yet been closely examined. This work investigated the adsorption behavior of trihalomethanes (THMs)—a regulated and ubiquitous DBP class in chlorinated water—onto virgin and weathered polyvinyl chloride (PVC) microplastics, the most widely used plastic material in drinking water distribution and sewer systems. A comparative analysis of kinetic and isotherm test results indicated that the adsorption mechanisms mainly involved hydrophobic interactions from a combination of weak and strong physisorption behavior and possibly chemisorption. The adsorption coefficients from all the models examined suggested that the adsorption of THMs, and perhaps chemically similar DBPs, onto virgin PVC microplastics can be 10–20 µg g−1. However, the weathered PVC microplastics contained more polar functional groups, which led to a decreased hydrophobicity and reduced THM adsorption capacity by approximately 10%. These findings offer novel insights into the possible adsorption characteristics of disinfection byproducts (DBPs) onto microplastics and will assist in targeting more toxic DBPs for future investigations. Full article
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<p>SEM images of virgin (<b>a</b>) and weathered (<b>b</b>) PVC microplastics.</p>
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<p>Experimental data and fitted curves for adsorption of THMs onto PVC with pseudo-first-order (PFO) and pseudo-second-order (PSO) kinetic models. Error bars represent experimental errors for duplicate analyses of duplicate samples.</p>
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<p>Experimental data and fitted curves for the adsorption of THMs onto PVC with (<b>a</b>) intraparticle diffusion model and (<b>b</b>) Boyd kinetic model. Error bars represent experimental errors for duplicate analyses of duplicate samples.</p>
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<p>Experimental data and fitted curves for adsorption of THMs onto PVC with (<b>a</b>) Freundlich and (<b>b</b>) modified Freundlich isotherm models. Error bars represent experimental errors for duplicate analyses of duplicate samples.</p>
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<p>Experimental data and modified Freundlich model fitted curves for THM adsorption onto virgin and weathered PVC: (<b>a</b>) TCM, (<b>b</b>) BDCM, (<b>c</b>) CDBM, and (<b>d</b>) TBM.</p>
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12 pages, 1741 KiB  
Article
Photocatalytic Degradation of Algal Organic Matter Using TiO2/UV and Persulfate/UV
by Luan de Souza Leite, Maria Teresa Hoffmann, Danilo Vitorino dos Santos and Luiz Antonio Daniel
Water 2024, 16(11), 1626; https://doi.org/10.3390/w16111626 - 6 Jun 2024
Cited by 1 | Viewed by 1075
Abstract
Eutrophication in water reservoirs releases algal organic matter (AOM), a key precursor to the formation of disinfection by-products (DBPs) during the disinfection process. Typical drinking water treatment is not efficient for AOM removal, and advanced treatments are necessary for the removal of residual [...] Read more.
Eutrophication in water reservoirs releases algal organic matter (AOM), a key precursor to the formation of disinfection by-products (DBPs) during the disinfection process. Typical drinking water treatment is not efficient for AOM removal, and advanced treatments are necessary for the removal of residual AOM before chlorination. UV-based technology with PS and TiO2 is widely used as a pre-oxidation step in water treatment; however, no publications have focused on them for AOM degradation. In this context, this work investigated the effect of oxidant concentration (0.1 to 0.5 g∙L−1) and pH (6 to 10) on AOM degradation with TiO2/UV and persulfate (PS)/UV using response surface methodology. In general, PS/UV was more effective in removing protein, while TiO2/UV was more effective in carbohydrate degradation. TiO2/UV removals varied from 27 to 57% for protein and from 48 to 86% for carbohydrates. The optimal condition (57% for protein and 86% for carbohydrates) was obtained using 0.5 g∙L−1 TiO2 at pH 10. PS/UV removals varied from 33 to 81% for protein and from 24 to 53% for carbohydrates. The optimal condition (81% for protein and 53% for carbohydrates) was obtained using 0.5 g∙L−1 PS concentration at pH 8. Degradation kinetics showed a good fit to the pseudo-first-order model (R2 > 95%) for both processes. The DBP formation reductions observed with TiO2/UV—trihalomethane (THM) (85 to 86%) and chloral hydrate (CH) (94 to 96%)—were similar to the efficiencies observed for PS/UV—THM (87 to 89%) and CH (83 to 88%). These results show the efficiency of UV-based technology for AOM degradation and the control of DBP formation. Full article
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<p>Removal (RE) of (<b>a</b>) protein and (<b>b</b>) carbohydrates from AOM with TiO<sub>2</sub>/UV using different values of pH (6 to 10) and TiO<sub>2</sub> concentration (0.1 to 0.5 g∙L<sup>−1</sup>). The experiments were carried out for 2 h.</p>
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<p>Removal (RE) of (<b>a</b>) protein and (<b>b</b>) carbohydrates from AOM with TiO<sub>2</sub>/UV using different values of pH (6 to 10) and TiO<sub>2</sub> concentration (0.1 to 0.5 g∙L<sup>−1</sup>). The experiments were carried out for 2 h.</p>
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<p>(<b>a</b>) AOM adsorption with TiO<sub>2</sub> measured in terms of protein, carbohydrate, and DOC removal. The experiments were completed under continuous agitation at 80 rpm for 2 h with 0.5 g∙L<sup>−1</sup> TiO<sub>2</sub> without UV light. (<b>b</b>) Zeta potential measurements of AOM and TiO<sub>2</sub> over pH range.</p>
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<p>Removal (RE) of (<b>a</b>) protein and (<b>b</b>) carbohydrates from AOM with PS/UV using different values of pH (6 to 10) and PS concentration (0.1 to 0.5 g∙L<sup>−1</sup>). The experiments were carried out for 2 h.</p>
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<p>Kinetics of AOM degradation with TiO<sub>2</sub>/UV and PS/UV measured by (<b>a</b>) protein and (<b>b</b>) carbohydrate analysis. The experiments were performed using 0.5 g∙L<sup>−1</sup> TiO<sub>2</sub>/PS at different pH values. Predicted values using a pseudo-first-order model are shown in the continuous line.</p>
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<p>Reduction in disinfection by-product (DBP) formation after the application of TiO<sub>2</sub>/UV and PS/UV. The experiments were carried out using 0.5 g∙L<sup>−1</sup> TiO<sub>2</sub>/PS at different pH values for 2.5 h.</p>
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11 pages, 1271 KiB  
Review
The Role of Ferrate (VI) in the Pretreatment of Algal Cells and Algal Organic Matters: A Review
by Saige Wang, Shuyi Yang, Huan Chen and Qiufeng Lin
Water 2024, 16(10), 1361; https://doi.org/10.3390/w16101361 - 11 May 2024
Cited by 1 | Viewed by 1607
Abstract
Algal blooms are caused by excessive levels of nitrogen, phosphorus, and other plant nutrients in water. Algae and algal organic matter (AOM) pose a great threat to the quality of drinking water. This manuscript offers a systematic review of algal removal by ferrate [...] Read more.
Algal blooms are caused by excessive levels of nitrogen, phosphorus, and other plant nutrients in water. Algae and algal organic matter (AOM) pose a great threat to the quality of drinking water. This manuscript offers a systematic review of algal removal by ferrate (Fe(VI)) oxidation, including the conditions for the removal of different algae by Fe(VI) and the factors affecting the removal efficiency. On this basis, the oxidation and coagulation mechanisms of algae removal by Fe(VI) are discussed. Then, the review introduces the process combining Fe(VI) pre-oxidation with aluminum sulfate action. The addition of aluminum sulfate can further enhance the coagulation effect and reduce the formation of disinfection byproducts (DBPs) in the subsequent chlorination process by effectively removing AOM, which is recognized as a precursor of DBPs. In addition, recent studies on the combined application of Fe(VI) and Fe(II) are also reviewed. In a reasonable dose range, the synergistic effect of Fe(VI) and Fe(II) can significantly improve the removal of algae and algal toxins. Finally, this review provides a comprehensive evaluation of the applicability of Fe(VI) in removing algal material, offers guidance for the harmless treatment of algae with Fe(VI), and identifies future research questions. Full article
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<p>Scheme of multistage algal removal using Fe(VI) treatment.</p>
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<p>Digital photos of algae-laden water (<b>A</b>) and water pre-oxidized with 0.01 mM (<b>C</b>), 0.02 mM (<b>E</b>), and 0.03 mM (<b>G</b>) Fe(VI) and coagulated with 0.5 mM FeCl<sub>3</sub>. Corresponding scanning electron microscope (SEM) photos of algae in beakers (<b>B</b>,<b>D</b>,<b>F</b>,<b>H</b>). (Adapted from He et al. [<a href="#B21-water-16-01361" class="html-bibr">21</a>]).</p>
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<p>Possible reaction steps of ferrate oxidation of AOM(x). (Adapted from Yu et al. [<a href="#B20-water-16-01361" class="html-bibr">20</a>]).</p>
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14 pages, 2026 KiB  
Article
Mucolytic Drugs Ambroxol and Bromhexine: Transformation under Aqueous Chlorination Conditions
by Sergey A. Sypalov, Ilya S. Varsegov, Nikolay V. Ulyanovskii, Albert T. Lebedev and Dmitry S. Kosyakov
Int. J. Mol. Sci. 2024, 25(10), 5214; https://doi.org/10.3390/ijms25105214 - 10 May 2024
Cited by 1 | Viewed by 1179
Abstract
Bromhexine and ambroxol are among the mucolytic drugs most widely used to treat acute and chronic respiratory diseases. Entering the municipal wastewater and undergoing transformations during disinfection with active chlorine, these compounds can produce nitrogen- and bromine-containing disinfection by-products (DBPs) that are dangerous [...] Read more.
Bromhexine and ambroxol are among the mucolytic drugs most widely used to treat acute and chronic respiratory diseases. Entering the municipal wastewater and undergoing transformations during disinfection with active chlorine, these compounds can produce nitrogen- and bromine-containing disinfection by-products (DBPs) that are dangerous for aquatic ecosystems. In the present study, primary and deep degradation products of ambroxol and bromhexine obtained in model aquatic chlorination experiments were studied via the combination of high-performance liquid and gas chromatography with high-resolution mass spectrometry. It was shown that at the initial stages, the reactions of cyclization, hydroxylation, chlorination, electrophilic ipso-substitution of bromine atoms with chlorine, and oxidative N-dealkylation occur. Along with known metabolites, a number of novel primary DBPs were tentatively identified based on their elemental compositions and tandem mass spectra. Deep degradation of bromhexine and ambroxol gives twenty-four identified volatile and semi-volatile compounds of six classes, among which trihalomethanes account for more than 50%. The specific class of bromhexine- and ambroxol-related DBPs are bromine-containing haloanilines. Seven of them, including methoxy derivatives, were first discovered in the present study. One more novel class of DBPs associated with bromhexine and ambroxol is represented by halogenated indazoles formed through dealkylation of the primary transformation products containing pyrazoline or tetrahydropyrimidine cycle in their structure. Full article
(This article belongs to the Section Molecular Pharmacology)
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<p>The structural formulas of ambroxol (<b>a</b>) and bromhexine (<b>b</b>).</p>
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<p>Bromhexine degradation pathways and primary transformation products formed during the aqueous chlorination.</p>
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<p>Scheme of the formation of detected DBPs during the interaction of ambroxol with active chlorine.</p>
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<p>Chromatographic peak areas of parent compounds and primary transformation products of bromhexine (<b>a</b>,<b>b</b>) and ambroxol (<b>c</b>,<b>d</b>) at active chlorine concentrations of 4 (<b>a</b>,<b>c</b>) and 7 (<b>b</b>,<b>d</b>) mg L<sup>−1</sup> depending on the reaction time.</p>
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