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Search Results (1,988)

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13 pages, 1775 KiB  
Article
Influence of Organic Loading Rates on the Treatment Performance of Membrane Bioreactors Treating Saline Industrial Wastewater
by Majeb Alotaibi, Ashraf Refaat, Faris Munshi, Mohamed Ali El-Said and Saber A. El-Shafai
Water 2024, 16(18), 2629; https://doi.org/10.3390/w16182629 - 16 Sep 2024
Abstract
This study investigated the efficacy of membrane bioreactor (MBR) technology in treating saline industrial wastewater, focusing on the impact of the organic loading rate (OLR) and the food-to-microorganism (F/M) ratio on treatment performance. This research utilized saline industrial wastewater from Al-Hasa, which had [...] Read more.
This study investigated the efficacy of membrane bioreactor (MBR) technology in treating saline industrial wastewater, focusing on the impact of the organic loading rate (OLR) and the food-to-microorganism (F/M) ratio on treatment performance. This research utilized saline industrial wastewater from Al-Hasa, which had salinity levels ranging from 5000 to 6900 mg/L. It explored treatment processes at varying Chemical Oxygen Demand (COD) concentrations of 800, 1400, and 2000 mg/L, corresponding to an OLR of 0.80 ± 0.05, 1.41 ± 0.07, and 1.98 ± 0.12 g COD/L, respectively. The average F/M ratios used were 0.20, 0.36, and 0.50 g COD/g MLSS·d, maintaining a constant Sludge Residence Time (SRT) of 12 days, a hydraulic retention time (HRT) of 24 h (hrs.), and a flux of 10 L/m2·h. The MBR system demonstrated high COD removal efficiencies, averaging 95.7 ± 1.6%, 95.5 ± 0.4%, and 96.1 ± 0.3%, alongside Biochemical Oxygen Demand (BOD) removal rates of 98.3 ± 0.2%, 99.8 ± 0.1%, and 98.5 ± 0.1%, respectively. However, an increased OLR led to elevated residual COD and BOD levels in the treated effluent, with COD concentrations reaching 34.2 ± 12.8, 63.3 ± 5.9, and 76.5 ± 5.4 mg/L, respectively. This study also reveals a significant decline in ammonia and Total Kjeldahl Nitrogen (TKN) removal efficiencies as OLR increases, dropping from 96.1 ± 0.5% to 80.2 ± 0.9% for ammonia and from 83.8 ± 3.4% to 65.8 ± 2.3% for TKN. Furthermore, higher OLRs significantly contribute to membrane fouling and elevate the transmembrane pressure (TMP), indicating a direct correlation between OLRs and operational challenges in MBR systems. The findings suggest that for optimal performance within the Saudi disposal limits for industrial wastewater, the MBR system should operate at an F/M ratio of ≤0.33 g COD/g of Mixed Liquor Suspended Solid (MLSS)·d. This study underscores the critical role of the OLR and F/M ratio in treating saline industrial wastewater using MBR technology, providing valuable insights for enhancing treatment efficiency and compliance with environmental standards. Full article
(This article belongs to the Section Wastewater Treatment and Reuse)
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<p>A schematic diagram of the treatment unit.</p>
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<p>The COD and BOD loading rates during the experiment.</p>
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<p>Salinity, TDS, and EC during the COD 800, COD 1400, and COD 2000 experiments.</p>
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<p>The flux rate and TMP during the COD 800, COD 1400, and COD 2000 experiments.</p>
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<p>SEM images showing the formation of the cake layer ((<b>A</b>): start-up; (<b>B</b>,<b>C</b>): samples with low and medium OLRs; and (<b>D</b>) samples with high OLRs).</p>
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13 pages, 3229 KiB  
Article
Characterization of Silica Sand-Based Pervious Bricks and Their Performance under Stormwater Treatment
by Meijuan Chen, Weiying Li, Zhiqiang Dong and Dawei Zhang
Water 2024, 16(18), 2625; https://doi.org/10.3390/w16182625 - 16 Sep 2024
Abstract
The acceleration of urbanization has disrupted natural water cycles, resulting in increased impervious urban surfaces and non-point source pollution from stormwater runoff. Addressing urban stormwater recharge has become crucial. This study introduces a novel silica sand-based permeable filtration material, investigating its surface characteristics, [...] Read more.
The acceleration of urbanization has disrupted natural water cycles, resulting in increased impervious urban surfaces and non-point source pollution from stormwater runoff. Addressing urban stormwater recharge has become crucial. This study introduces a novel silica sand-based permeable filtration material, investigating its surface characteristics, pore structure, permeability, and pollutant interception capabilities. The results demonstrate that hydrophilic binder coating modification of the permeable surface sand aggregate, combined with hydrophilic inorganic additives, having a porous structure with an average pore size of less than 50 μm and a porosity between 15% and 35%, significantly enhances surface hydrophilicity, achieving a permeation rate of up to 6.8 mL/(min·cm²). Moreover, it shows exceptional filtration and anti-clogging properties, achieving over 98% suspended solids interception and strong resistance to fouling. Dynamic biofilm formation experiments using simulated rain and domestic wastewater explore biofilm morphology and function on silica sand filtration well surfaces. Mature biofilms sustain COD removal efficiency exceeding 70%, with levels consistently below 50 mg/L, NH4+ decreasing to 2 mg N/L, and total nitrogen maintained below 10 mg N/L. The system features anoxic, anoxic, and aerobic zones, fostering synergistic organic matter and nitrogen removal by diverse microorganisms, enhancing pollutant mitigation. Silica sand-based permeable filtration material effectively mitigates urban stormwater runoff pollutants—suspended solids, organic matter, and nitrogen—offering an innovative solution for sponge city development and rainwater resource management. Full article
(This article belongs to the Special Issue Urban Stormwater Harvesting, and Wastewater Treatment and Reuse)
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<p>(<b>A</b>) Original silica sand photo; (<b>B</b>) schematic diagram of sand grain coating modification; (<b>C</b>) photo of modified sand grains; (<b>D</b>) silica sand permeable and filter brick; (<b>E</b>) water purification filter wall structure made from silica sand permeable and filter bricks; (<b>F</b>) structure of silica sand filter well.</p>
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<p>(<b>A</b>) SEM image of the surface layer of the permeable and filterable brick; and (<b>B</b>) schematic diagram of the structure of the permeable and filterable brick.</p>
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<p>XPS spectra of the permeable surface of the water-permeable filter brick for Si2p (<b>A</b>) and C1s (<b>B</b>). The observed different colors refer to different elements or its chemical states for the easily distinguish and identify, as indicated by the arrow.</p>
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<p>(<b>A</b>) Schematic diagram of the water permeation mechanism of the permeable and filterable brick, (<b>B</b>) variation of water flux (<span class="html-italic">J</span>), porosity (<span class="html-italic">ε</span>), pore diameter (<span class="html-italic">r<sub>p</sub></span>), and membrane resistance (<span class="html-italic">R</span>) along the direction of water flow in the permeable and filterable brick.</p>
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<p>(<b>A</b>) The underwater oil contact angle of the water-permeable and filterable brick; (<b>B</b>) the oil-blocking effect of the water-permeable and filterable brick when wetted by water; (<b>C</b>) schematic diagram of the oil-blocking mechanism of the water-permeable and filterable brick when wetted by water.</p>
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<p>SEM observation of the biofilm on the surface of silicon sand filter bricks with different magnification. (<b>A</b>) ×5.00k; (<b>B</b>) ×20.0k; (<b>C</b>) ×5.00k; (<b>D</b>) ×30.0k.</p>
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<p>Schematic diagram of the biofilm in the silicon sand filter well: (<b>A</b>) Schematic diagram of denitrification mechanism, (<b>B</b>) Variation of the concentrations of COD, ammonia nitrogen, and nitrate nitrogen in each layer.</p>
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13 pages, 4242 KiB  
Article
Alkylated MXene–Carbon Nanotube/Microfiber Composite Material with Flexible, Superhydrophobic, and Sensing Properties
by Siyu Wang, Dawei Xia, Xinyu Xu, Haoyang Song and Yongquan Qing
Materials 2024, 17(18), 4499; https://doi.org/10.3390/ma17184499 - 13 Sep 2024
Viewed by 329
Abstract
Superhydrophobic strain sensors are highly promising for human motion and health monitoring in wet environments. However, the introduction of superhydrophobicity inevitably alters the mechanical and conductive properties of these sensors, affecting sensing performance and limiting behavior monitoring. Here, we developed an alkylated MXene–carbon [...] Read more.
Superhydrophobic strain sensors are highly promising for human motion and health monitoring in wet environments. However, the introduction of superhydrophobicity inevitably alters the mechanical and conductive properties of these sensors, affecting sensing performance and limiting behavior monitoring. Here, we developed an alkylated MXene–carbon nanotube/microfiber composite material (AMNCM) that is simultaneously flexible, superhydrophobic, and senses properties. Comprising a commercially available fabric substrate that is coated with a functional network of alkylated MXene/multi-walled carbon nanotubes and epoxy–silicone oligomers, the AMNCM offers high mechanical and chemical robustness, maintaining high conductivity and strain sensing properties. Furthermore, the AMNCM strain sensor achieves a gauge factor of up to 51.68 within a strain range of 80–100%, and exhibits rapid response times (125 ms) and long-term stability under cyclic stretching, while also displaying superior direct/indirect anti-fouling capabilities. These properties position the AMNCM as a promising candidate for next-generation wearable devices designed for advanced environmental interactions and human activity monitoring. Full article
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<p>(<b>a</b>) Design strategies for AMNCM. (<b>b</b>) Reaction mechanism illustration for the formation of the AMNCM.</p>
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<p>SEM images of (<b>a</b>) original fabric and (<b>b</b>–<b>d</b>) AMNCM surface at different magnifications. (<b>e</b>) Elemental mappings of main elements C, O, Si, and Cl on the AMNCM surface.</p>
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<p>LSCM topographical images of (<b>a</b>) original fabric and (<b>b</b>) AMNCM surface.</p>
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<p>(<b>a</b>) FTIR spectra of OTS–MXene and MXene. (<b>b</b>) XPS survey spectra, (<b>c</b>) C1s, (<b>d</b>) O1s, and (<b>e</b>) Si2p high-resolution XPS spectra of the AMNCM surface.</p>
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<p>(<b>a</b>) Schematic illustration of sandpaper abrasion test experimental setup. (<b>b</b>) Change in the contact angle and sliding angle with mechanical abrasion lengths for AMNCM. (<b>c</b>) Image of AMNCM wettability before and after sewage washing. (<b>d</b>) Image of the AMNCM wettability after finger wiping, tape peeling, and knife scratching. Image of wettability of the AMNCM after (<b>e</b>) water impact, (<b>f</b>) stretching, and (<b>g</b>) bending kink. (<b>h</b>) Effect of outdoor exposure time on the stability of the AMNCM. (<b>i</b>) The wetting state of water, acid, alkali, and salt on the AMNCM surface. (<b>j</b>) CA and SA of droplets with different pH values on the AMNCM surface.</p>
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<p>(<b>a</b>) Different types of liquid droplets with spherical shapes on coating surface, namely red-dyed water, Coca-Cola, orange juice, peanut dew, coffee, and mango juice. (<b>b</b>) The CAs and SAs of different droplets on the AMNCM surface. (<b>c</b>) Photo of acid, Coca-Cola, and milk being poured onto the AMNCM surface. Self-cleaning ability of the AMNCM against (<b>d</b>) soil and (<b>e</b>) white contaminants.</p>
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<p>(<b>a</b>) Resistance response of the AMNCM strain sensor at different strain regions. (<b>b</b>) Relative resistance variation of the AMNCM strain sensor under various stretching/releasing conditions. (<b>c</b>) Periodic strain sensing behavior of the AMNCM strain sensor with different frequencies. (<b>d</b>) Response time of the AMNCM strain sensor. (<b>e</b>) Long-term strain sensing performance of the AMNCM strain sensor under 3000 stretching and releasing cycles (20% strain). Human behavior monitoring map of the AMNCM strain sensor for (<b>f</b>) finger bending changes and (<b>g</b>) resistance changes at different bending angles.</p>
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18 pages, 4821 KiB  
Article
Fabrication of Corrosion-Resistant Superhydrophobic Coatings and Impermeable Porous Structures Using Fluorinated Microemulsions Containing Thermally Decomposable Surfactants
by Bin Zhang, Hongen Zhang, Qiang Ren, Bei He, Yi Zhang and Zhengwu Jiang
Coatings 2024, 14(9), 1176; https://doi.org/10.3390/coatings14091176 - 11 Sep 2024
Viewed by 334
Abstract
In this work, a series of fluorinated microemulsions were synthesized using thermally decomposable N-dodecyl-N,N-dimethylamine N-oxide (LDAO) as surfactant. Then, polybutylene terephthalate nonwoven fabrics (PBT) were coated with microemulsion and heat-treated. Superhydrophobic and oil-repellent modified PBT with WCA (water contact angle) of about 152°, [...] Read more.
In this work, a series of fluorinated microemulsions were synthesized using thermally decomposable N-dodecyl-N,N-dimethylamine N-oxide (LDAO) as surfactant. Then, polybutylene terephthalate nonwoven fabrics (PBT) were coated with microemulsion and heat-treated. Superhydrophobic and oil-repellent modified PBT with WCA (water contact angle) of about 152°, a sliding angle of about 2.1°, and oil repellency grade of 8 were prepared. The effect of surfactants on the surface wettability of hydrophobic materials was analyzed by TG-DTA, XPS, and WCA tests. The results show that surfactants decrease the WCA of hydrophobic materials, but LDAO can eliminate this effect by heat treatment. The anti-corrosion and permeability of LDAO coatings were compared with those of conventional fluorinated coatings through degradation and anti-permeability tests. It was shown that the LDAO fluorinated superhydrophobic coating is more resistant to corrosion by chemical solutions and significantly improves the impermeability of porous materials. Anti-fouling and self-cleaning tests showed excellent anti-fouling and self-cleaning properties on several common substrate surfaces modified with LDAO fluorinated microemulsions. It is expected that these new LDAO fluorinated microemulsions have promising applications in the preparation of corrosion-resistant surfaces and impermeable structures. Full article
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<p>Thermal decomposition of N-Dodecyl-N,N-dimethylamine N-oxide.</p>
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<p>The fabrication process of the superhydrophobic PBT fabrics.</p>
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<p>The schematic diagram for measuring ΔP value (<b>a</b>) and air flux (<b>b</b>).</p>
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<p>FTIR (<b>a</b>) and <sup>1</sup>H-NMR (<b>b</b>) spectra of fluorinated emulsions after dehydration. (<b>c</b>) The laser particle size graphs of fluorinated emulsions. (<b>d</b>) XPS spectra of PBT, PBT-E4a, and PBT-E4.</p>
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<p>FTIR (<b>a</b>) and <sup>1</sup>H-NMR (<b>b</b>) spectra of fluorinated emulsions after dehydration. (<b>c</b>) The laser particle size graphs of fluorinated emulsions. (<b>d</b>) XPS spectra of PBT, PBT-E4a, and PBT-E4.</p>
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<p>SEM of PBT (<b>a</b>) and PBT-E4 (<b>b</b>).</p>
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<p>Wettability test for fabrics. (<b>a</b>–<b>e</b>) Static contact angle of PBT (<b>a</b>), PBT-E4 (<b>b</b>), PBT-AO-1 (<b>c</b>), PBT-AO-2 (<b>d</b>), and PBT-SDBS (<b>e</b>). (<b>f</b>) Static photo of stained water droplets on the PBT-E4. (<b>g</b>,<b>h</b>) The droplets of mineral oil (<b>g</b>) and n-heptane (<b>h</b>) on the surface of PBT and PBT-E4. (<b>i</b>) From (1) to (4) are motion pictures of PBT-E4 slide angle test.</p>
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<p>TGA (<b>a</b>) and DTG (<b>b</b>) curves of N-dodecyl-N,N-dimethylamine N-oxide (LDAO).</p>
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<p>FTIR spectra of N-dodecyl-N,N-dimethylamine N-oxide (LDAO) before and after thermal treatment.</p>
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<p>(<b>a</b>) The wetting process of superhydrophobic coatings in immersion experiments. (<b>b</b>–<b>f</b>) The water absorption curves of fabrics in deionized water, physiological saline, 10% glucose solution, 1% acetic acid solution, and 1% diethylamine solution immersion experiments.</p>
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<p>(<b>a</b>) Comparison between the pristine and modified PBT fabrics (1), wool nonwoven mats (2), wood panels (3), and glass fiber paper (4) after 48 h immersion in methyl blue stained water. (<b>b</b>) Photographs of the diverse liquid droplets on the pristine and modified PBT fabrics, wool nonwoven mats, wood panels, and glass fiber paper. Liquids on each substrate were (A) vinegar, (B) stained water, (C) coffee, (D) milk, (E) soy sauce, (F) stained oil. (<b>c</b>) Self-cleaning test of the pristine and modified PBT fabrics, wool nonwoven mats, wood panels, and glass fiber paper.</p>
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<p>(<b>a</b>) The schematic diagram of the permeation mechanism. (<b>b</b>–<b>d</b>) The ΔP value testing of PBT (<b>b</b>), PBT-ES (<b>c</b>), and PBT-E4 (<b>d</b>).</p>
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17 pages, 3855 KiB  
Article
Compressible Diagnosis of Membrane Fouling Based on Transfer Entropy
by Xiaolong Wu, Dongyang Hou, Hongyan Yang and Honggui Han
Appl. Sci. 2024, 14(18), 8176; https://doi.org/10.3390/app14188176 - 11 Sep 2024
Viewed by 267
Abstract
Membrane fouling caused by many direct and indirect triggering factors has become an obstacle to the application of membrane bioreactors (MBRs). The nonlinear relationship between those factors is subject to complex causality or affiliation, which is difficult to clarify for the diagnosis of [...] Read more.
Membrane fouling caused by many direct and indirect triggering factors has become an obstacle to the application of membrane bioreactors (MBRs). The nonlinear relationship between those factors is subject to complex causality or affiliation, which is difficult to clarify for the diagnosis of membrane fouling. To solve this problem, this paper proposes a compressible diagnosis model (CDM) based on transfer entropy to facilitate the fault diagnosis of the root cause for membrane fouling. The novelty of this model includes the following points: Firstly, a framework of a CDM between membrane fouling and causal variables is built based on a feature extraction algorithm and mechanism analysis. The framework can identify fault transfer scenarios following the changes in operating conditions. Secondly, the fault transfer topology of a CDM based on transfer entropy is constructed to describe the causal relationship between variables dynamically. Thirdly, an information compressible strategy is designed to simplify the fault transfer topology. This strategy can eliminate the repetitious affiliation relationship, which contributes to diagnosing the root causal variables speedily and accurately. Finally, the effectiveness of the proposed CDM is verified by the measured data from an actual MBR. The results of experiments demonstrate that the proposed CDM fulfills the diagnosis of membrane fouling. Full article
(This article belongs to the Special Issue Application of Neural Computation in Artificial Intelligence)
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<p>Membrane fouling diagnosis system.</p>
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<p>Autoencoder structure.</p>
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<p>Fault transfer topology.</p>
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<p>Indirect connection.</p>
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<p>Characteristic variable selection.</p>
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<p>The RMSE during the training process.</p>
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<p>The RMSE during the detection process.</p>
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<p>Initial fault transfer topology.</p>
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<p>Fault transfer topology after setting the threshold.</p>
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<p>Fault transfer topology based on information compressible strategy.</p>
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25 pages, 7108 KiB  
Article
Coupling Low-Frequency Ultrasound to a Crossflow Microfiltration Pilot: Effect of Ultrasonic Pulse Application on Sono-Microfiltration of Jackfruit Juice
by Herenia Adilene Miramontes-Escobar, Nicolas Hengl, Manuel Dornier, Efigenia Montalvo-González, Martina Alejandra Chacón-López, Nawel Achir, Fabrice Vaillant and Rosa Isela Ortiz-Basurto
Membranes 2024, 14(9), 192; https://doi.org/10.3390/membranes14090192 - 11 Sep 2024
Viewed by 277
Abstract
To reduce membrane fouling during the processing of highly pulpy fruit juices into clarified beverages, a crossflow Sono-Microfiltration (SMF) system was employed, strategically equipped with an ultrasonic probe for the direct application of low-frequency ultrasound (LFUS) to the juice just before the entrance [...] Read more.
To reduce membrane fouling during the processing of highly pulpy fruit juices into clarified beverages, a crossflow Sono-Microfiltration (SMF) system was employed, strategically equipped with an ultrasonic probe for the direct application of low-frequency ultrasound (LFUS) to the juice just before the entrance to the ceramic membrane. Operating conditions were standardized, and the application of LFUS pulses in both corrective and preventive modes was investigated. The effect of SMF on the physicochemical properties and the total soluble phenol (TSP) content of the clarified juice was also evaluated. The distance of ultrasonic energy irradiation guided the selection of the LFUS probe. Amplitude conditions and ultrasonic pulses were more effective in the preventive mode and did not cause membrane damage, reducing the operation time of jackfruit juice by up to 50% and increasing permeability by up to 81%. The SMF did not alter the physicochemical parameters of the clarified juice, and the measured LFUS energy ranges did not affect the TSP concentration during the process. This study is the first to apply LFUS directly to the feed stream in a pilot-scale crossflow microfiltration system to reduce the fouling of ceramic membranes and maintain bioactive compounds in jackfruit juice. Full article
(This article belongs to the Special Issue Membrane Technologies in Food Industry and Bioprocessing)
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Figure 1
<p>Options for using the pumping system that allow different operating modes to be applied in the Sono-Microfiltration pilot. The solid line indicates the use of the SMF pilot with a centrifugal pump; the dashed line indicates the use of the SMF pilot with a positive displacement pump; the solid and dotted lines indicate the use of both pumps. (1) Recirculating bath; (2) Feed tank (30 L); (3) Positive displacement pump; (4) Centrifugal pump; (5) Flowmeter; (6) Ultrasound probe; (7) Filtration membrane housing; (8) Permeate flow outlet; (9) Tubular heat exchanger.</p>
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<p>Thermal imaging of ultrasonic energy irradiation from two probes at different amplitudes of low-frequency ultrasound (LFUS) (without membrane filtration, U = 6 m·s<sup>−1</sup>).</p>
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<p>Thermal imaging of ultrasonic energy irradiation from two probes at different amplitudes of low-frequency ultrasound (LFUS) (without membrane filtration, U = 6 m·s<sup>−1</sup>).</p>
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<p>Effect of LFUS application in corrective mode during the processing of jackfruit juice. Pulp/water ratio of 1:1 at VRR = 1 (ultrasonic diameter probe 2.54 cm, membrane Tami, dpore = 0.2 μm, TMP = 2.7 bar, T<sub>feed</sub> = 30 °C, and U = 6 m·s<sup>−1</sup>). ON: application of LFUS, OFF: without LFUS, A: LFUS amplitude, MF: Microfiltration.</p>
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<p>Multichannel ceramic membrane (0.2 μm) with damage caused by applying a 50% LFUS amplitude, an ultrasonic intensity of 21.2–31.2 W·cm<sup>2</sup>, and 104–153 W power.</p>
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<p>Effect of LFUS application on (<b>A</b>) the volumetric reduction ratio (VRR) during the SMF process of jackfruit juicing on process time and (<b>B</b>) total membrane resistance to the VRR (ultrasonic diameter probe 2.54 cm, membrane Tami, dpore = 0.2 μm, TMP = 2.7 bar, T<sub>feed</sub> = 30 °C, and U = 6 m·s<sup>−1</sup>). ON: LFUS application; OFF: without LFUS application; A: LFUS amplitude.</p>
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<p>Effect of LFUS application on (<b>A</b>) the volumetric reduction ratio (VRR) during the SMF process of jackfruit juicing on process time and (<b>B</b>) total membrane resistance to the VRR (ultrasonic diameter probe 2.54 cm, membrane Tami, dpore = 0.2 μm, TMP = 2.7 bar, T<sub>feed</sub> = 30 °C, and U = 6 m·s<sup>−1</sup>). ON: LFUS application; OFF: without LFUS application; A: LFUS amplitude.</p>
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<p>Effect of low-frequency ultrasound application on the decrease in membrane permeability during Sono-Microfiltration processes of clarified jackfruit juice at VRR = 1.85 (ultrasonic diameter probe 2.54 cm, membrane Tami, dpore = 0.2 μm, TMP = 2.7 bar, T<sub>feed</sub> = 30 °C, and U = 6 m·s<sup>−1</sup>). ON: LFUS application; OFF: no LFUS application; A: LFUS amplitude.</p>
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<p>Contour plots of 2<sup>3−1</sup> fractional factorial design in SMF pilot in jackfruit juice 1:2. (<b>A</b>) Pulse OFF vs. Pulse ON, (<b>B</b>) amplitude vs. pulse ON, (<b>C</b>) amplitude vs. pulse OFF.</p>
Full article ">Figure 7 Cont.
<p>Contour plots of 2<sup>3−1</sup> fractional factorial design in SMF pilot in jackfruit juice 1:2. (<b>A</b>) Pulse OFF vs. Pulse ON, (<b>B</b>) amplitude vs. pulse ON, (<b>C</b>) amplitude vs. pulse OFF.</p>
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<p>Effect of Sono-Microfiltration (SMF) on the turbidity of (<b>A</b>) clarified jackfruit juice (CJJ) and (<b>B</b>) retained jackfruit juice (RJJ). Different letters show statistically significant differences.</p>
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<p>Effect of Sono-Microfiltration (SMF) on (<b>A</b>) total soluble solids (TSS) and (<b>B</b>) viscosity in jackfruit juice. IJJA: fed initial jackfruit juice, CJJ: clarified jackfruit juice, RJJ: retained jackfruit juice. Different letters show statistically significant differences.</p>
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<p>Effect of Sono-Microfiltration (SMF) on (<b>A</b>) total soluble solids (TSS) and (<b>B</b>) viscosity in jackfruit juice. IJJA: fed initial jackfruit juice, CJJ: clarified jackfruit juice, RJJ: retained jackfruit juice. Different letters show statistically significant differences.</p>
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<p>Total soluble phenols (TSP) in clarified jackfruit juice by Sono-Microfiltration (SMF) compared with the raw juice (IJJF). Different letters show statistically significant differences.</p>
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<p>Design of the Sono-Microfiltration pilot. (1) Recirculating bath; (2) Feed tank (30 L); (3) Positive displacement pump; (4) Centrifugal pump; (5) Flowmeter; (6) Ultrasonic probe; (7) Filtration membrane housing; (8) Permeate flow outlet; (9) Tubular heat exchanger.</p>
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<p>Volumetric reduction ratio (VRR) vs. permeate flux (Jp) during the clarification of jackfruit juice by Sono-Microfiltration.</p>
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15 pages, 1837 KiB  
Article
Mitigation of Membrane Fouling in Membrane Bioreactors Using Granular and Powdered Activated Carbon: An Experimental Study
by Nataly Morales, Camila Mery-Araya, Paula Guerra, Rodrigo Poblete and Jaime Chacana-Olivares
Water 2024, 16(17), 2556; https://doi.org/10.3390/w16172556 - 9 Sep 2024
Viewed by 616
Abstract
This experimental study explores the mitigation of membrane fouling in membrane bioreactors (MBRs) through the combined use of granular activated carbon (GAC) and powdered activated carbon (PAC). The research assesses the impact of these materials on the fouling resistance, critical flux, and permeate [...] Read more.
This experimental study explores the mitigation of membrane fouling in membrane bioreactors (MBRs) through the combined use of granular activated carbon (GAC) and powdered activated carbon (PAC). The research assesses the impact of these materials on the fouling resistance, critical flux, and permeate quality using various mixed liquor suspended solids concentrations and carbon dosages. The results indicate that the GAC-PAC combination significantly reduces the total filtration resistance, particularly the cake layer resistance, by 11.7% to 13.6% compared to setups without activated carbon or with the individual carbon types. The study also reveals that this combination decreased the fouling rate by 15% to 24% at critical flux steps, demonstrating substantial improvements in fouling mitigation and operational efficiency. Furthermore, the GAC-PAC combination, which produces an adsorption process, enhances the permeate quality, achieving the near-complete removal of organic matter, total nitrogen, and turbidity, with total phosphorus removal reaching 99%. These findings demonstrate that the combined use of GAC and PAC not only reduces membrane fouling but also improves the overall MBR performance, making it a viable strategy for enhancing the efficiency of wastewater treatment processes. Full article
(This article belongs to the Special Issue Membrane Technology for Desalination and Wastewater Treatment)
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<p>Schematic of the experimental setup.</p>
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<p>Evolution of TMP during F<sub>c</sub> measurement of MBRs with GAC and PAC at various doses and combinations in MBR M1 and MBR M2.</p>
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<p>The evolution of the fouling rate during F<sub>c</sub> measurement for MBR M1 and MBR M2.</p>
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<p>Permeability for the tests conducted in MBR M1 and MBR M2.</p>
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<p>Initial increase in TMP (ΔP<sub>0</sub>) in MBR M1 and MBR M2.</p>
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<p>Intrinsic membrane resistance, total resistance, and cake layer resistance for MBR M1 and MBR M2.</p>
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12 pages, 4585 KiB  
Article
Thin-Layer TiO2 Membrane Fabrication by Condensed Layer Deposition
by Mohammed M. Numaan, Ahmed M. Jasim, Yangchuan Xing and Maria M. Fidalgo
Materials 2024, 17(17), 4436; https://doi.org/10.3390/ma17174436 - 9 Sep 2024
Viewed by 248
Abstract
A novel approach to the fabrication of thin-film supported metal oxide membranes was investigated. Nanocoatings were obtained by the condensed layer deposition of TiO2 on tubular microporous supports, applying multiple consecutive layers of TiO2/polyaniline. The surface, cross-sectional structure, and morphology [...] Read more.
A novel approach to the fabrication of thin-film supported metal oxide membranes was investigated. Nanocoatings were obtained by the condensed layer deposition of TiO2 on tubular microporous supports, applying multiple consecutive layers of TiO2/polyaniline. The surface, cross-sectional structure, and morphology of the materials were investigated by electron microscopy. Their membrane-related properties were explored by permeability measurements, rejection, and fouling analysis, using polyethylene glycol (PEG) as test molecules. The SEM images showed that TiO2 was successfully deposited on the surface, creating a layer with partial coverage of the support after each layer was deposited; consequently, the permeability of the membranes decreased gradually. Overall, the results of the flux and permeability of the membranes confirmed the coating. The transmembrane pressure (TMP) increased with each coating layer, while the rejection of the membrane showed gradual improvement. Full article
(This article belongs to the Special Issue Advancements in Thin Film Deposition Technologies)
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<p>Schematic of the experimental setup and the membrane module.</p>
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<p>SEM images of uncoated membrane surfaces (<b>a</b>) and surfaces coated with (<b>b</b>) 1 TiO<sub>2</sub> layer, (<b>c</b>) 2 TiO<sub>2</sub> layers, (<b>d</b>) 3 TiO<sub>2</sub> layers, and (<b>e</b>) 4 TiO<sub>2</sub> layers.</p>
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<p>SEM images of membrane cross-sections of (<b>a</b>) uncoated support and support coated with (<b>b</b>) 1 TiO<sub>2</sub> layer, (<b>c</b>) 2 TiO<sub>2</sub> layers, (<b>d</b>) 3 TiO<sub>2</sub> layers, and (<b>e</b>) 4 TiO<sub>2</sub> layers.</p>
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<p>Water permeability of support and coated membranes with 1, 2, 3, and 4 layers; CLD coated clean membranes; after PEG filtration and hydraulic cleaning.</p>
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<p>Rejection evolution vs. time: (<b>left</b>) 25 ppm solution PEG (MW 20,000 Da); (<b>right</b>) 25 ppm solution PEG (MW 200,000 Da); Q<sub>feed</sub> = 33 mL/min; Q<sub>retent =</sub> 22.5 mL/L; T = 25 °C.</p>
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<p>Transmembrane pressure vs. time during filtration of (<b>left</b>) 25 ppm PEG solution (MW 20 kDa); (<b>right</b>) 25 ppm PEG solution (MW 200 kDa); Q<sub>feed</sub> = 33 mL/min; Q<sub>retent</sub> = 22.5 mL/L; T = 25 °C.</p>
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17 pages, 7534 KiB  
Article
Impact of PCLNPG Nanopolymeric Additive on the Surface and Structural Properties of PPSU Ultrafiltration Membranes for Enhanced Protein Rejection
by Younus Rashid Taha, Adel Zrelli, Nejib Hajji, Raed A. Al-Juboori and Qusay Alsalhy
Processes 2024, 12(9), 1930; https://doi.org/10.3390/pr12091930 - 8 Sep 2024
Viewed by 616
Abstract
This research explored the use of a partially cross-linked graft copolymer (PCLNPG) as an innovative nanopolymer pore-forming agent to enhance polyphenylsulfone (PPSU) membranes for protein separation applications. The study systematically examined the impact of incorporating PCLNPG at varying concentrations on the morphological and [...] Read more.
This research explored the use of a partially cross-linked graft copolymer (PCLNPG) as an innovative nanopolymer pore-forming agent to enhance polyphenylsulfone (PPSU) membranes for protein separation applications. The study systematically examined the impact of incorporating PCLNPG at varying concentrations on the morphological and surface properties of PPSU membranes. A thorough characterization of the resulting PPSU-PCLNPG membranes was performed, focusing on changes in morphology, water affinity, porosity, pore size, and pore size distribution. The experimental findings demonstrated that the use of PCLNPG led to a significantly more porous structure, as confirmed by SEM analysis, with notable increases in porosity and pore size (nearly double). Additionally, the hydrophilicity of the PPSU membrane was remarkably enhanced. Performance evaluations revealed a substantial improvement in pure water flux, with the flux nearly tripling. The BSA retention was directly correlated with the concentration of the PCLNPG pore former for a loading range of 0.25–0.75 wt.%. The incorporation of PCLNPG also reduced the membrane fouling propensity by reducing both cake layer resistance (Rc) and pore plugging resistance (Rp). These results underscore the potential of PCLNPG-PPSU membranes for wastewater reclamation and nutrient recovery applications. Full article
(This article belongs to the Section Materials Processes)
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<p>Top surface micrographs of PPSU membranes at different PCLNPG concentrations: (<b>A</b>) 0 wt.%, (<b>B</b>) 0.25 wt.%, (<b>C</b>) 0.5 wt.%, (<b>D</b>) 0.75 wt.%, (<b>E</b>) 1.0 wt.%, and (<b>F</b>) 1.25 wt.%.</p>
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<p>Top surface micrographs of PPSU membranes at different PCLNPG concentrations: (<b>A</b>) 0 wt.%, (<b>B</b>) 0.25 wt.%, (<b>C</b>) 0.5 wt.%, (<b>D</b>) 0.75 wt.%, (<b>E</b>) 1.0 wt.%, and (<b>F</b>) 1.25 wt.%.</p>
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<p>Cross-section SEM images of the prepared membranes at different PCLNPG concentrations: (<b>A</b>) 0 wt.%, (<b>B</b>) 0.25 wt.%, (<b>C</b>) 0.5 wt.%, (<b>D</b>) 0.75 wt.%, (<b>E</b>) 1.0 wt.%, and (<b>F</b>) 1.25 wt.%.</p>
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<p>FTIR for the PCLNPG nanopolymer and prepared membranes.</p>
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<p>The contact angle of the prepared membranes.</p>
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<p>Thickness and porosity of prepared membranes.</p>
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<p>Mean pore size of unmodified and PPSU modified membranes.</p>
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<p>Pore size distribution of membranes (<b>A</b>) 0 wt.% PCLNPG, (<b>B</b>) 0.25 wt.% PCLNPG, (<b>C</b>) 0.5 wt.% PCLNPG, (<b>D</b>) 0.75 wt.% PCLNPG, (<b>E</b>) 1.0 wt.% PCLNPG, and (<b>F</b>) 1.25 wt.% PCLNPG.</p>
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<p>(<b>A</b>) Pure water and BSA solution fluxes; (<b>B</b>) rejection of BSA.</p>
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<p>(<b>A</b>) Pure water and BSA solution fluxes; (<b>B</b>) rejection of BSA.</p>
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<p>Resistance of membranes Rm, Rp, Rc, and Rt.</p>
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<p>Flux recovery ratio (FRR) of membranes.</p>
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15 pages, 9452 KiB  
Article
Preparation of Robust Superhydrophobic Coatings Using Hydrophobic and Tough Micro/Nano Particles
by Tianyi Feng, Yifan Liu, Siyan Ye, Liping Sheng, Binrui Wu and Lingcai Huang
Coatings 2024, 14(9), 1156; https://doi.org/10.3390/coatings14091156 - 8 Sep 2024
Viewed by 489
Abstract
Superhydrophobic nanocomposite coatings, prepared using adhesive and fillers, offer advantages including ease of fabrication and suitability for large-scale applications, but compared with other types of artificial superhydrophobic surfaces, poor durability still limits these surfaces from practical applications. The utilization of micro/nanoscale particles with [...] Read more.
Superhydrophobic nanocomposite coatings, prepared using adhesive and fillers, offer advantages including ease of fabrication and suitability for large-scale applications, but compared with other types of artificial superhydrophobic surfaces, poor durability still limits these surfaces from practical applications. The utilization of micro/nanoscale particles with both intrinsic hydrophobicity and robust mechanical properties to prepare coatings should significantly contribute to enhanced durability. Herein, rough and hydrophobic particles with micro/nano hierarchical structures were prepared at first, and robust superhydrophobic surfaces were fabricated using the prepared particles and additional nanoparticles. The initially prepared particles formed a rough framework of the coating, while additional nanoparticles provided inevitable nanoscale structures. A series of mechanical tests were carried out to validate the durability, and the surface with 20 wt.% NPs exhibited the best performance, withstanding 30 tape peeling tests, a 2.47 m sandpaper rubbing test (at a pressure of 5 kPa), the impact of 200 g of grit dropped from a height of 20 cm, and a 2 h acidic immersion. These appealing materials may attract attention for self-cleaning, high-speed water impact resistance, anti-icing, and anti-fouling applications in the coatings industry. Full article
(This article belongs to the Special Issue Superhydrophobic Surfaces and Coatings)
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<p>Surface microscopic morphology of particle specimens with different Al<sub>2</sub>O<sub>3</sub> nanoparticle contents: (<b>a<sub>1</sub></b>,<b>a<sub>2</sub></b>) 20 wt.%; (<b>b<sub>1</sub></b>,<b>b<sub>2</sub></b>) 40 wt.%; (<b>c<sub>1</sub></b>,<b>c<sub>2</sub></b>) 50 wt.%; (<b>d<sub>1</sub></b>,<b>d<sub>2</sub></b>) 60 wt.%.</p>
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<p>The surface microstructure of samples prepared using different mechanical stirring speeds: (<b>a</b>) 100 r/min; (<b>b</b>) 200 r/min; (<b>c</b>) 400 r/min; (<b>d</b>) 600 r/min; (<b>e</b>) 800 r/min; (<b>f</b>) 1000 r/min.</p>
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<p>The variation in the surface hydrophobic properties with different nanoparticle contents.</p>
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<p>Surface microstructure of coated samples with different Al<sub>2</sub>O<sub>3</sub> nanoparticle contents: (<b>a</b>,<b>d</b>) 10 wt.%; (<b>b</b>,<b>e</b>) 20 wt.%; (<b>c</b>,<b>f</b>) 100 wt.%.</p>
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<p>Test results for the coating grid division method: (<b>a</b>) 10 wt.%; (<b>b</b>) 20 wt.%; (<b>c</b>) 100 wt.%; (<b>d</b>) damage area and corresponding classification after the test. The black area represents the detached portion after the test, while the white area represents the intact area.</p>
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<p>Tape peeling test results for the coating samples: (<b>a</b>,<b>b</b>) test results for C10 and C20, respectively; (<b>c</b>,<b>d</b>) surface morphology of the sample after the test.</p>
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<p>Sandpaper abrasion test results: (<b>a</b>,<b>b</b>) C10 sample test results for 600 grit and 800 grit sandpaper abrasion, respectively; (<b>c</b>,<b>d</b>) C20 sample test results for 600 grit and 800 grit sandpaper abrasion, respectively; (<b>e</b>) the surface microstructure of the sample after abrasion testing.</p>
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<p>Sand impact test results for the (<b>a</b>) C10 sample and (<b>b</b>) C20 sample; the microscopic morphology of the (<b>c</b>) C10 and (<b>d</b>) C20 samples, respectively.</p>
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<p>Results of chemical durability tests: (<b>a</b>) immersion in hydrochloric acid solution; (<b>b</b>) immersion in sodium hydroxide solution. Microscopic morphology of the coating surface after chemical durability testing via: (<b>c</b>) immersion in hydrochloric acid solution; (<b>d</b>) immersion in sodium hydroxide solution.</p>
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12 pages, 1769 KiB  
Review
Recent Progress on Atmospheric Corrosion of Field-Exposed Magnesium Alloys
by Mengqi Wang, Lihui Yang, Hao Liu, Xiutong Wang, Yantao Li and Yanliang Huang
Metals 2024, 14(9), 1000; https://doi.org/10.3390/met14091000 - 2 Sep 2024
Viewed by 365
Abstract
It is well known that the poor corrosion resistance of magnesium alloys is a key factor limiting their application. Field exposure is the most reliable means to evaluate the atmospheric corrosion performance of magnesium alloys. This article reviews the field exposure corrosion behavior [...] Read more.
It is well known that the poor corrosion resistance of magnesium alloys is a key factor limiting their application. Field exposure is the most reliable means to evaluate the atmospheric corrosion performance of magnesium alloys. This article reviews the field exposure corrosion behavior of magnesium alloys in typical atmospheric environments (including the marine atmosphere, industrial atmosphere, etc.) in recent years. According to the literature review, it was found that there are significant regional differences in the atmospheric corrosion behavior of magnesium alloys, which is the result of the coupling of multiple factors in the atmospheric environment. By investigating the corrosion rate and corrosion products of different types of magnesium alloys in different environments, the corrosion mechanism of magnesium alloys in different environments was summarized. Specifically, environmental parameters such as atmospheric temperature, relative humidity, CO2, and chloride ion deposition rates in the marine atmospheric environment can affect the corrosion behavior of magnesium alloys. The corrosion of magnesium alloys in different industrial atmospheric environments is mainly affected by atmospheric temperature and relative humidity, as well as atmospheric pollutants (such as SO2, CO2, NO2) and dust. This review provides assistance to the development of new corrosion-resistant magnesium alloys. Full article
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<p>Microstructure of magnesium and several common magnesium alloys [<a href="#B17-metals-14-01000" class="html-bibr">17</a>].</p>
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<p>Summary of the weight loss rates of the pure Mg and Mg alloys at the two exposure sites, and in the lab salt spray and sea wave impact tests [<a href="#B29-metals-14-01000" class="html-bibr">29</a>].</p>
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<p>Corrosion mechanism diagram of magnesium alloys in marine atmosphere.</p>
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<p>Hydrogen evolution curves of pure Mg immersed in basic Mg(OH)<sub>2</sub> saturated solution, haze constituent-contaminated solutions, and haze-contaminated solution for 72 h: (<b>a</b>) all the curves, and (<b>b</b>) details of some curves in (<b>a</b>) [<a href="#B58-metals-14-01000" class="html-bibr">58</a>].</p>
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17 pages, 2852 KiB  
Article
Flourishing in Darkness: Protist Communities of Water Sites in Shulgan-Tash Cave (Southern Urals, Russia)
by Natalia E. Gogoleva, Marina A. Nasyrova, Alexander S. Balkin, Olga Ya. Chervyatsova, Lyudmila Yu. Kuzmina, Elena I. Shagimardanova, Yuri V. Gogolev and Andrey O. Plotnikov
Diversity 2024, 16(9), 526; https://doi.org/10.3390/d16090526 - 1 Sep 2024
Viewed by 382
Abstract
Karst caves, formed by the erosion of soluble carbonate rocks, provide unique ecosystems characterized by stable temperatures and high humidity. These conditions support diverse microbial communities, including wall microbial fouling, aquatic biofilms, and planktonic communities. This study discloses the taxonomic diversity of protists [...] Read more.
Karst caves, formed by the erosion of soluble carbonate rocks, provide unique ecosystems characterized by stable temperatures and high humidity. These conditions support diverse microbial communities, including wall microbial fouling, aquatic biofilms, and planktonic communities. This study discloses the taxonomic diversity of protists in aquatic biotopes of Shulgan-Tash Cave, a culturally significant site and popular tourist destination, by 18S rRNA gene metabarcoding. Our findings reveal the rich protist communities in the cave’s aquatic biotopes, with the highest diversity observed in Blue Lake at the cave entrance. In contrast, Distant Lake in the depth of the cave was inhabited by specific communities of plankton, mats, and pool fingers, which exhibited lower richness and evenness, and were adapted to extreme conditions (cold, darkness, and limited nutrients). High-rank taxa including Opisthokonta, Stramenopiles, and Rhizaria dominated all biotopes, aligning with observations from other subterranean environments. Specific communities of biotopes inside the cave featured distinct dominant taxa: amoeboid stramenopile (Synchromophyceae) and flagellates (Choanoflagellatea and Sandona) in mats; flagellates (Choanoflagellatea, Bicoecaceae, Ancyromonadida) and amoeboid protists (Filasterea) in pool fingers; flagellates (Ochromonadales, Glissomonadida, Synchromophyceae), fungi-like protists (Peronosporomycetes), and fungi (Ustilaginomycotina) in plankton. The specificity of the communities was supported by LEfSe analysis, which revealed enriched or differentially abundant protist taxa in each type of biotope. The predominance of Choanoflagellatea in the communities of cave mats and pool fingers, as well as the predominance of Synchromophyceae in the cave mats, appears to be a unique feature of Shulgan-Tash Cave. The cold-tolerant yeast Malassezia recorded in other caves was present in both plankton and biofilm communities, suggesting its resilience to low temperatures. However, no potentially harmful fungi were detected, positioning this research as a baseline for future monitoring. Our results emphasize the need for ongoing surveillance and conservation efforts to protect the fragile ecosystems of Shulgan-Tash Cave from human-induced disturbances and microbial invasions. Full article
(This article belongs to the Special Issue Diversity in 2024)
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<p>Map of the research area and Shulgan-Tash Cave sampling sites: (<b>A</b>) Overview map showing the global position of the research area. (<b>B</b>) The position of the cave in relation to the Southern Urals. (<b>C</b>) Digital model of the cave combined with the relief of the Tirmentau massif. Visualization was created using Cloud Compare 2020 software with laser scanning point clouds [<a href="#B32-diversity-16-00526" class="html-bibr">32</a>]. The cavities of the phreatic zone are shown schematically (by Snetkov E., unpublished data). (<b>D</b>) Sampling scheme of Distant Lake and its watercourses. PF—pool finger biofilm; CEW—lake water at the point of inflow into Distant Lake; WPF—water surrounding pool fingers; WDL—water in the middle of Distant Lake; MDL—mats of Distant Lake; BL—water from Blue Lake.</p>
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<p>Distant Lake sampling sites: (<b>a</b>) Distant Lake; (<b>b</b>) the outflowing creek with filamentous microbial mats; (<b>c</b>) microbial mats; (<b>d</b>) pool fingers.</p>
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<p>Alpha diversity indices of the protist communities in the sites of Shulgan-Tash Cave and the outer Blue Lake: Chao 1, Shannon, Gini-Simpson, and Pielou’s evenness. The points on the plot correspond to the individual samples and are colored according to the different sites: PF—pool finger biofilm; CEW—lake water at the point of inflow into Distant Lake; WPF—water surrounding pool fingers; WDL—water in the middle of Distant Lake; MDL—mats of Distant Lake; BL—water from Blue Lake.</p>
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<p>2D plots based on the results of principal coordinate analysis (PCoA) of the protist communities using Bray–Curtis (left) and the weighted UniFrac (right) distances. PCo1 (Axis 1) and PCo2 (Axis 2) explained 33.65% and 25.8% of the protist community variance at the ASV level, respectively. PF—pool finger biofilms; CEW—lake water at the point of inflow into Distant Lake; WPF—water surrounding pool fingers; WDL—water in the middle of Distant Lake; MDL—mats of Distant Lake; BL—water from Blue Lake.</p>
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<p>The most abundant protist taxa in the communities of water sites in Shulgan-Tash Cave. Circle size indicates the inferred relative abundance based on amplicon numbers (in %). PF—pool finger biofilm; CEW—lake water at the point of inflow into Distant Lake; WPF—water surrounding pool fingers; WDL—water in the middle of Distant Lake; MDL—mats of Distant Lake; BL—water from Blue Lake.</p>
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<p>The relative abundances of the protist functional groups in communities of Blue Lake and Distant Lake (Shulgan-Tash Cave). The colors correspond to the supergroup names.</p>
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16 pages, 3727 KiB  
Article
A Carrier Phase Ultrafiltration and Backflow Recovery Technique for Purification of Biological Macromolecules
by Raja Ghosh
Membranes 2024, 14(9), 188; https://doi.org/10.3390/membranes14090188 - 30 Aug 2024
Viewed by 564
Abstract
A simple carrier phase based ultrafiltration technique that is akin to liquid chromatography and is suitable for medium-to-large volume sample preparation in the laboratory is discussed in this paper. A membrane module was integrated with a liquid chromatography system in a “plug and [...] Read more.
A simple carrier phase based ultrafiltration technique that is akin to liquid chromatography and is suitable for medium-to-large volume sample preparation in the laboratory is discussed in this paper. A membrane module was integrated with a liquid chromatography system in a “plug and play” mode for ease of sample handling, and recovery of species retained by the membrane. The sample injector and pump were used for feed injection and for driving ultrafiltration, while the sensors and detectors were used for real-time monitoring of the separation process. The concentration of retained species was enriched by utilizing controlled concentration polarization. The recovery of the retained and enriched species was enhanced by backflow of carrier phase through the membrane using appropriate combination of valves. The backflow of carrier phase also cleaned the membrane and limited the extent of membrane fouling. Proof-of-concept of the proposed technique was provided by conducting different types of protein ultrafiltration experiments. The technique was shown to be suitable for carrying out protein fractionation, desalting, buffer exchange and concentration enrichment. Adoption of this approach is likely to make ultrafiltration easier to use for non-specialized users in biological research laboratories. Other advantages include enhanced product recovery, significant reduction in the number of diavolumes of buffer needed for conducting desalting and buffer exchange, minimal membrane fouling and the potential for repeated use of the same module for multiple separation cycles. Full article
(This article belongs to the Section Membrane Applications for Other Areas)
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<p>(<b>A</b>) Flow channels, inlets/outlets and position of membrane in a laterally fed ultrafiltration device. (<b>B</b>) The different components used to assemble a laterally fed ultrafiltration device for the carrier phase ultrafiltration and backflow recovery technique.</p>
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<p>Comparison of the mechanisms involved in the recovery of retained species by crossflow and backflow.</p>
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<p>Set-ups used for monitoring the clearance of permeable species from the membrane module by S-flow ultrafiltration (<b>A</b>) and C-flow ultrafiltration (<b>B</b>).</p>
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<p>Set-up used for S-flow ultrafiltration crossflow recovery.</p>
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<p>Set-ups used for S-flow ultrafiltration S-backflow recovery (<b>A</b>) and S-flow ultrafiltration C-backflow recovery (<b>B</b>).</p>
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<p>Set-ups used for S-flow ultrafiltration flipped C-backflow recovery (<b>A</b>) and S-flow ultrafiltration flipped S-backflow recovery (<b>B</b>).</p>
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<p>(<b>A</b>) UV absorbance profiles of permeate obtained during the clearance of lysozyme from the membrane module using S-flow ultrafiltration (thin line) and C-flow ultrafiltration (thick line). (<b>B</b>) Close up on the start and tail sections of the lysozyme clearance profiles.</p>
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<p>UV absorbance profiles obtained during recovery of BSA using S-flow ultrafiltration crossflow recovery (<b>A</b>), S-flow ultrafiltration S-backflow recovery (<b>B</b>), S-flow ultrafiltration C-backflow recovery (<b>C</b>), S-flow ultrafiltration flipped C-backflow recovery (<b>D</b>) and S-flow ultrafiltration flipped S-flow recovery (<b>E</b>).</p>
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<p>UV absorbance profile obtained during the fractionation of lysozyme (permeable protein) and BSA (retained protein) by S-flow ultrafiltration C-backflow recovery.</p>
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<p>Desalting of 0.25 mg mL<sup>−1</sup> BSA solution (50 mL feed volume) by S-flow ultrafiltration C-backflow recovery at 4 mL min<sup>−1</sup> flow rate (<b>A</b>) and at 5 mL min<sup>−1</sup> flow rate (<b>B</b>) (F: feed injection, D: diafiltration, R: recovery, solid line: UV absorbance and dashed line: conductivity).</p>
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<p>Concentration of 0.25 mg mL<sup>−1</sup> BSA solution (70 mL feed volume) by S-flow ultrafiltration C-backflow recovery using 4 mL min<sup>−1</sup> flow rate during both feed injection and diafiltration (<b>A</b>) and using a combination of 4 mL min<sup>−1</sup> flow rate during feed injection and 5 mL min<sup>−1</sup> flow rate during diafiltration and recovery (<b>B</b>) (F: feed injection, D: diafiltration and R: recovery).</p>
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<p>Concentration of 2 mg mL<sup>−1</sup> BSA solution (50 mL feed volume) by S-flow ultrafiltration C-backflow recovery using 1 mL min<sup>−1</sup> flow rate during feed injection and 2 mL min<sup>−1</sup> flow rate during diafiltration and recovery (F: feed injection, D: diafiltration and R: recovery).</p>
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14 pages, 10170 KiB  
Article
AgNP Composite Silicone-Based Polymer Self-Healing Antifouling Coatings
by Xingda Liu, Jiawen Sun, Jizhou Duan, Kunyan Sui, Xiaofan Zhai and Xia Zhao
Materials 2024, 17(17), 4289; https://doi.org/10.3390/ma17174289 - 30 Aug 2024
Viewed by 335
Abstract
Biofouling poses a significant challenge to the marine industry, and silicone anti-biofouling coatings have garnered extensive attention owing to their environmental friendliness and low surface energy. However, their widespread application is hindered by their low substrate adhesion and weak static antifouling capabilities. In [...] Read more.
Biofouling poses a significant challenge to the marine industry, and silicone anti-biofouling coatings have garnered extensive attention owing to their environmental friendliness and low surface energy. However, their widespread application is hindered by their low substrate adhesion and weak static antifouling capabilities. In this study, a novel silicone polymer polydimethylsiloxane (PDMS)-based poly(urea-thiourea-imine) (PDMS-PUTI) was synthesized via stepwise reactions of aminopropyl-terminated polydimethylsiloxane (APT-PDMS) with isophorone diisocyanate (IPDI), isophthalaldehyde (IPAL), and carbon disulfide (CS2). Subsequently, a nanocomposite coating (AgNPs-x/PDMS-PUTI) was prepared by adding silver nanoparticles (AgNPs) to the polymer PDMS-PUTI. The dynamic multiple hydrogen bonds formed between urea and thiourea linkages, along with dynamic imine bonds in the polymer network, endowed the coating with outstanding self-healing properties, enabling complete scratch healing within 10 min at room temperature. Moreover, uniformly dispersed AgNPs not only reduced the surface energy of the coating but also significantly enhanced its antifouling performance. The antibacterial efficiency against common marine bacteria Pseudomonas aeruginosa (P.sp) and Staphylococcus aureus (S.sp) was reduced by 97.08% and 96.71%, respectively, whilst the diatom settlement density on the coating surface was as low as approximately 59 ± 3 diatom cells/mm2. This study presents a novel approach to developing high-performance silicone antifouling coatings. Full article
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<p>(<b>a</b>) Synthesis of AgNPs-X/PDMS-PUTI. (<b>b</b>) AgNPs-X/PDMS-PUTI design diagram.</p>
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<p>(<b>a</b>) Synthesis of AgNPs-X/PDMS-PUTI. (<b>b</b>) AgNPs-X/PDMS-PUTI design diagram.</p>
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<p><sup>1</sup>H NMR spectra of PDMS-PUTI.</p>
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<p>FTIR spectra of PDMS-PUTI.</p>
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<p>GPC curve of PDMS-PUTI.</p>
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<p>(<b>a</b>) Appearance of PDMS-PUTI and AgNPs-x/PDMS-PUTI. (<b>b</b>) The stress–strain curves at 25 °C of PDMS-PUTI and AgNPs-x/PDMS-PUTI.</p>
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<p>Self-healing properties of the AgNPs-x/PDMS-PUTI coatings. Micrographs images of the self-healing process of (<b>a</b>) PDMS-PUTI, (<b>b</b>) AgPNs-3/PDMS-PUTI, (<b>c</b>) AgPNs-6/PDMS-PUTI, and (<b>d</b>) AgPNs-9/PDMS-PUTI at 25 °C in the air (scratch thickness: ~120 μm, scratch width: ~7 μm, film thickness: ~0.7 mm).</p>
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<p>Adhesion strength of PDMS and AgNPs-x/PDMS-PUTI coatings adhered to the GFE and steel.</p>
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<p>SEM and EDS spectrum images (C, S, Cu, Si, Ag) of the surface of (<b>a</b>) PDMS-PUTI, (<b>b</b>) AgNPs-3/PDMS-PUTI, (<b>c</b>) AgNPs-6/PDMS-PUTI, (<b>d</b>) AgNPs-9/PDMS-PUTI.</p>
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<p>CLSM images of (<b>a</b>) PDMS-PUTI, (<b>b</b>) AgNPs-3/PDMS-PUTI, (<b>c</b>) AgNPs-3/PDMS-PUTI, and (<b>d</b>) AgNPs-3/PDMS-PUTI (image showing a 324 μm × 322 μm area).</p>
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<p>(<b>a</b>) Images of water and DIM contact angles for PDMS-PUTI, PDMS-PUTI/0.1, PDMS-PUTI/0.5, and PDMS-PUTI/1.0, (<b>b</b>) WCA of PDMS, PDMS-PUTI, PDMS-PUTI/0.1, PDMS-PUTI/0.5, and PDMS-PUTI/1.0, (<b>c</b>) SE of PDMS, PDMS-PUTI, PDMS-PUTI/0.1, PDMS-PUTI/0.5, and PDMS-PUTI/1.0.</p>
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<p>Removal strength of pseudobarnacles on each coating.</p>
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<p>Antibacterial and anti-diatom properties of AgNPs-X/PDMS-PUTI coatings. Fluorescence images of (<b>a</b>) <span class="html-italic">P.</span>sp. and (<b>b</b>) <span class="html-italic">S</span>.sp, (<b>c</b>) <span class="html-italic">N. incerta</span> adhering to PDMS, PDMS-PUTI, AgNPs-3/PDMS-PUTI, AgNPs-6/PDMS-PUTI, and AgNPs-9/PDMS-PUTI, (<b>d</b>) quantitative evaluation of <span class="html-italic">P.</span>sp. and <span class="html-italic">S.</span>sp. adhesion rates, (<b>e</b>) quantitative colonization density of <span class="html-italic">N. incerta</span> on coating surfaces.</p>
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9 pages, 3136 KiB  
Communication
Off-Stoichiometry Thiol-Ene (OSTE) Micro Mushroom Forest: A Superhydrophobic Substrate
by Haonan Li, Muyang Zhang, Yeqian Liu, Shangneng Yu, Xionghui Li, Zejingqiu Chen, Zitao Feng, Jie Zhou, Qinghao He, Xinyi Chen, Huiru Zhang, Jiaen Zhang, Xingwei Zhang and Weijin Guo
Micromachines 2024, 15(9), 1088; https://doi.org/10.3390/mi15091088 - 28 Aug 2024
Viewed by 404
Abstract
Superhydrophobic surfaces have been used in various fields of engineering due to their resistance to corrosion and fouling and their ability to control fluid movement. Traditionally, superhydrophobic surfaces are fabricated via chemical methods of changing the surface energy or mechanical methods of controlling [...] Read more.
Superhydrophobic surfaces have been used in various fields of engineering due to their resistance to corrosion and fouling and their ability to control fluid movement. Traditionally, superhydrophobic surfaces are fabricated via chemical methods of changing the surface energy or mechanical methods of controlling the surface topology. Many of the conventional mechanical methods use a top-to-bottom scheme to control the surface topolopy. Here, we develop a novel fabrication method of superhydrophobic substrates using a bottom-to-top scheme via polymer OSTE, which is a prototyping polymer material developed for the fabrication of microchips due to its superior photocuring ability, mechanical properties, and surface modification ability. We fabricate a superhydrophobic substrate by OSTE–OSTE micro mushroom forest via a two-step lithography process. At first, we fabricate an OSTE pillar forest as the mushroom stems; then, we fabricate the mushroom heads via backside lithography with diffused UV light. Such topology and surface properties of OSTE render these structures superhydrophobic, with water droplets reaching a contact angle of 152.9 ± 0.2°, a sliding angle of 4.1°, and a contact angle hysteresis of less than 0.5°. These characteristics indicate the promising potential of this substrate for superhydrophobic applications. Full article
(This article belongs to the Special Issue Recent Advances in Micro/Nano-Fabrication)
Show Figures

Figure 1

Figure 1
<p>Schematic diagram of the fabrication of OSTE micro mushroom forest. At first, we fabricate the OSTE pillar forest on a flat substrate. Then, we use black gelatin solution to fill the space between pillars under capillary action and solidify gelatin. After that, diffused UV light is reflected through pillars and cures the OSTE contacting the pillar top, thereafter forming the OSTE micro mushroom forest. This diagram is not to scale.</p>
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<p>(<b>a</b>) The fabrication procedures of OSTE pillar forest in cross-section view. The pillars are in an orthogonal arrangement. (<b>b</b>) The design of the chrome glass mask.</p>
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<p>(<b>a</b>) The cross-section view of the fabrication process of the OSTE micro mushroom forest. (<b>b</b>) The working principle of the light diffuser and the fabrication of the mushroom head: diffused UV light is reflected in the pillars and emitted from the pillar top, curing a spherical microstructure.</p>
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<p>(<b>a</b>,<b>b</b>) OSTE micro mushroom forest with a pillar diameter of 300 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 400 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m. (<b>c</b>) OSTE micro mushroom forest with a pillar diameter of 400 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 600 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m. (<b>d</b>) OSTE micro mushroom forest with a pillar diameter of 400 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 1000 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m. The difference in brightness of the images is due to different imaging angle, illumination intensity, and exposure time.</p>
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<p>(<b>a</b>) The contact angle of a water droplet on a flat OSTE substrate. (<b>b</b>) The contact angle of a water droplet on the OSTE micro mushroom forest (with a pillar diameter of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m), which is 152.9 ± 0.2°. The volume of the water droplet in both images is 5.0 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>L.</p>
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<p>The sliding angle of a water droplet with a volume of 5.0 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>L on OSTE micro mushroom forest (with a pillar diameter of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m) is evaluated, with a sliding angle of 4.1° and a contact angle hysteresis of 0.484°.</p>
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<p>A series of images that show the low adhesion of water droplets on OSTE micro mushroom forest (with a pillar diameter of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m). The volume of the water droplet is 5.0 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>L.</p>
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<p>(<b>a</b>–<b>c</b>) The images illustrate the water droplet contact angle tests conducted on OSTE micro mushroom forest (with a pillar diameter of 100 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m and a distance of 50 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>m) over a period of time after fabrication. The volume of the water droplet is 5.0 <math display="inline"><semantics> <mi mathvariant="sans-serif">μ</mi> </semantics></math>L.</p>
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