[go: up one dir, main page]
More Web Proxy on the site http://driver.im/
You seem to have javascript disabled. Please note that many of the page functionalities won't work as expected without javascript enabled.
 
 
Sign in to use this feature.

Years

Between: -

Subjects

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Journals

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Article Types

Countries / Regions

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Search Results (6,768)

Search Parameters:
Keywords = filtration

Order results
Result details
Results per page
Select all
Export citation of selected articles as:
20 pages, 1954 KiB  
Article
Inflammatory Biomarkers and Oral Health Disorders as Predictors of Head and Neck Cancer: A Retrospective Longitudinal Study
by Amr Sayed Ghanem, Kitti Sipos, Ágnes Tóth and Attila Csaba Nagy
Int. J. Mol. Sci. 2025, 26(5), 2279; https://doi.org/10.3390/ijms26052279 (registering DOI) - 4 Mar 2025
Abstract
Head and neck cancers (HNCs) are often diagnosed late, leading to poor prognosis. Chronic inflammation, particularly periodontitis, has been linked to carcinogenesis, but systemic inflammatory markers remain underexplored. This study was the first to examine whether elevated C-reactive protein (CRP) can serve as [...] Read more.
Head and neck cancers (HNCs) are often diagnosed late, leading to poor prognosis. Chronic inflammation, particularly periodontitis, has been linked to carcinogenesis, but systemic inflammatory markers remain underexplored. This study was the first to examine whether elevated C-reactive protein (CRP) can serve as a cost-effective adjunct in HNC risk assessment, alongside oral health indicators. A retrospective cohort study analysed 23,742 hospital records (4833 patients, 2015–2022) from the University Hospital of Debrecen. HNC cases were identified using ICD-10 codes, with CRP and periodontitis as key predictors. Kaplan–Meier survival analysis, log-rank tests, and Weibull regression were used to assess risk, with model performance evaluated via AIC/BIC and ROC curves. Periodontitis was significantly associated with HNC (HR 5.99 [1.96–18.30]), while elevated CRP (>15 mg/L) independently increased risk (HR 4.16 [1.45–12.00]). Females had a significantly lower risk than males (HR 0.06 [0.01–0.50]). CRP may serve as a cost-effective, easily accessible biomarker for early HNC detection when combined with oral health screening. Integrating systemic inflammation markers into HNC risk assessment models could potentially improve early diagnosis in high-risk populations. Full article
(This article belongs to the Special Issue Pathogenesis and Treatments of Head and Neck Cancer)
Show Figures

Figure 1

Figure 1
<p>Cumulative hazard plots by periodontitis, CRP levels, gender, and dental developmental disorders. Note: Cumulative hazard functions illustrating the relationships between time to head and neck cancer diagnosis and key variables: (<b>A</b>) periodontitis (yes vs. no), (<b>B</b>) C-reactive protein levels (&gt;15 mg/L vs. ≤15 mg/L), (<b>C</b>) gender (male vs. female), and (<b>D</b>) dental developmental (DD) disorders (present vs. absent). Hazard functions are stratified by categories with 95% confidence intervals (shaded areas), calculated using the Nelson–Aalen estimator. CRP, C-reactive protein; DD disorders, dental developmental disorders.</p>
Full article ">Figure 2
<p>Cumulative hazard plots by embedded and impacted teeth, dental caries, disease of hard tissue of teeth, and disorders of teeth and supporting structures. Note: Cumulative hazard functions depicting the association between time to head and neck cancer diagnosis and key dental conditions: (<b>A</b>) embedded and impacted teeth (present vs. absent), (<b>B</b>) dental caries (present vs. absent), (<b>C</b>) disease of hard tissue (DHT) of teeth (present vs. absent), and (<b>D</b>) disorders of teeth and supporting structures (DTSS) (present vs. absent). Hazard functions are stratified by condition categories with 95% confidence intervals (shaded areas), calculated using the Nelson–Aalen estimator. DHT, disease of hard tissue; DTSS, disorders of teeth and supporting structures.</p>
Full article ">Figure 3
<p>Receiver operating characteristic (ROC) curve of the Weibull regression model for predicting head and neck cancer. Note: The ROC curve shows an AUC of 0.8646, demonstrating excellent model discrimination.</p>
Full article ">Figure 4
<p>Kaplan–Meier survival curves stratified by significant predictors. Kaplan–Meier survival curves depicting observed and Weibull model-predicted probabilities over time. Stratification is based on significant covariates: (<b>A</b>) impacted teeth, (<b>B</b>) periodontitis, (<b>C</b>) C-reactive protein (CRP) levels, and (<b>D</b>) gender.</p>
Full article ">
12 pages, 1269 KiB  
Article
Efficacy of Acid-Treated HEPA Filters for Dual Sequestration of Nicotine and Particulate Matter
by Toluwanimi M. Oni, Changjie Cai and Evan L. Floyd
Air 2025, 3(1), 8; https://doi.org/10.3390/air3010008 (registering DOI) - 4 Mar 2025
Abstract
Tobacco smoking and electronic cigarette (EC) use are associated with elevated levels of particulate matter (PM) and nicotine in indoor environments. This study assessed filtration and nicotine capture efficiency of untreated and citric acid-treated high efficiency particulate air (HEPA) filters from two manufacturers, [...] Read more.
Tobacco smoking and electronic cigarette (EC) use are associated with elevated levels of particulate matter (PM) and nicotine in indoor environments. This study assessed filtration and nicotine capture efficiency of untreated and citric acid-treated high efficiency particulate air (HEPA) filters from two manufacturers, “on-brand” (original) and “off-brand” (replacement). When challenged with salt aerosol, the filtration efficiency (FE) (Mean ± RSD) of original HEPA filters (99.9% ± 0.1) was significantly higher than replacements (94.4% ± 1.7), but both were significantly below the HEPA designation of 99.97%. No significant differences in FE were observed between treated and untreated HEPA filters. All filters had lower FE for EC aerosol compared to salt aerosol, especially among replacement filters. Nicotine capture efficiency was significantly higher in citric acid-treated HEPA filters for originals (99.4% ± 0.22) and replacements (99.0% ± 1.07) compared to untreated originals (57.4% ± 2.33) and replacements (42.0% ± 14.20). This study demonstrated that our citric acid treatment of HEPA filters was effective and efficient at capturing airborne nicotine and did not affect the FE for PM. Use of citric acid-treated HEPA filters would be an effective exposure reduction strategy for both nicotine and PM in indoor settings. Full article
Show Figures

Figure 1

Figure 1
<p>HEPA filter types used in this study left panel shows original filter and right panel shows replacement filter. Filter components; (<b>a</b>) Pre-filter screen and pleated filter (<b>b</b>) Gasket (<b>c</b>) Activated carbon filter.</p>
Full article ">Figure 2
<p>Environmental chamber set-up for treating filters with citric acid, testing their filtration efficiency, and nicotine capture efficiency.</p>
Full article ">Figure 3
<p>Filtration Efficiency (%) between Untreated Original and Replacement HEPA Filters with Salt Aerosol.</p>
Full article ">
15 pages, 2902 KiB  
Article
Development of a Concept for Closing the Water Cycle in the Surface Treatment of Ferrous and Non-Ferrous Metals
by Jolanta Janiszewska and Paulina Rajewska
Sustainability 2025, 17(5), 2212; https://doi.org/10.3390/su17052212 (registering DOI) - 4 Mar 2025
Abstract
This study examines the treatment of industrial wastewater generated during vibro-abrasive steel and Zn-Al alloy parts machining in a Polish metal-processing plant. The machining process uses grinding fluids, which are sent for disposal after becoming saturated with contaminants, incurring high costs. A two-stage [...] Read more.
This study examines the treatment of industrial wastewater generated during vibro-abrasive steel and Zn-Al alloy parts machining in a Polish metal-processing plant. The machining process uses grinding fluids, which are sent for disposal after becoming saturated with contaminants, incurring high costs. A two-stage filtration process was investigated: an initial bag filtration (pore size 5 µm) followed by a low-pressure (4 bar) ultrafiltration with polyacrylonitrile membranes (30 kDa cut-off). The studies were carried out on a laboratory scale in a cross-flow system using a batch configuration. The initial filtrate flux was 0.116 mL min−1 cm−2 and 0.050 mL min−1 cm−2 for Zn-Al alloy and the steel wastewater, respectively. Key physicochemical parameters, including turbidity, COD, and TOC, were analysed for raw wastewater, feed, retentate, and permeate. Significant reductions in contaminant concentrations were achieved, with comparable total efficiencies for both the wastewaters tested. The reductions in turbidity, COD, TOC, anionic surfactants, total phosphorus and non-ionic surfactants ranged from 80% to almost 100%. A complete removal of total suspended solids was achieved. The novelty of this research lies in applying polyacrylonitrile flat-sheet membranes to treat wastewater from vibratory machining of ferrous and non-ferrous materials and recycle reclaimed water, which has not been systematically explored in previous studies. The study demonstrates the potential of low-pressure membrane filtration for wastewater recycling, offering insights into environmentally friendly and energy-efficient management of industrial wastewater. Full article
(This article belongs to the Section Waste and Recycling)
Show Figures

Figure 1

Figure 1
<p>The installation diagram for vibro-abrasive machining of steel and Zn-Al alloy parts.</p>
Full article ">Figure 2
<p>A schematic diagram of the laboratory membrane filtration system used.</p>
Full article ">Figure 3
<p>The characteristics of the membrane used for the treatment of tested wastewater.</p>
Full article ">Figure 4
<p>A photo of samples (Zn-Al alloy; wastewater after filtration through a 5 µm filter bag is the feed).</p>
Full article ">Figure 5
<p>The reduction (%) of the tested physicochemical parameters after filtration on a bag filter (pore diameter 5 µm).</p>
Full article ">Figure 6
<p>Changes in the permeate flux during the membrane filtration process of (<b>a</b>) Zn-Al alloy wastewater and (<b>b</b>) steel wastewater.</p>
Full article ">Figure 7
<p>A comparison of rejection coefficients for the determined physicochemical parameters of (<b>a</b>,<b>b</b>) Zn-Al wastewater and (<b>c</b>,<b>d</b>) steel wastewater obtained in the UF process (relative to the feed).</p>
Full article ">Figure 8
<p>Schematic diagram of the concept of closing the water circuit in the vibro-abrasive treatment of Zn-Al alloy and steel.</p>
Full article ">
8 pages, 725 KiB  
Article
A Single-Center Experience of En Bloc vs. Single Renal Transplantation on Adult Recipients
by Yoon-Jung Chang, Samuel Simpson, Megan Charette and Obi Ekwenna
Transplantology 2025, 6(1), 7; https://doi.org/10.3390/transplantology6010007 (registering DOI) - 4 Mar 2025
Abstract
Background/Objectives: While there are several debates on en bloc renal transplants and pediatric donors regarding the efficacy and concern for renal mass, multiple studies have supported the notion that transplanting pediatric en bloc kidneys produces comparable results in contrast to single kidneys [...] Read more.
Background/Objectives: While there are several debates on en bloc renal transplants and pediatric donors regarding the efficacy and concern for renal mass, multiple studies have supported the notion that transplanting pediatric en bloc kidneys produces comparable results in contrast to single kidneys from living or deceased donors. Methods: This case series included a retrospective analysis of a university medical center, primarily focused on comparing the post-operative outcomes between recipients of pediatric and adult en bloc kidneys, which are horseshoe kidneys, from deceased donors and recipients of single adult kidneys from living or deceased donors. Results: This study demonstrated that the post-operative results in recipients of pediatric en bloc kidneys consisting of serum creatinine and estimated glomerular filtration rate (eGFR) values were lower and higher, respectively, and had a comparable improvement in kidney function at post-transplant, 1-week, 1-month, 3-months, and 1-year post-op marks. Conclusions: Our center data and outcomes indicate that en bloc kidney transplantation from pediatric donors yields comparable results to that of single kidney transplantations from living and deceased donors. Full article
(This article belongs to the Section Solid Organ Transplantation)
Show Figures

Figure 1

Figure 1
<p>(<b>a</b>) Primary renal diseases of pediatric en bloc kidney recipients at this center; (<b>b</b>) primary renal diseases of adult kidney recipients at this center.</p>
Full article ">Figure 2
<p>(<b>a</b>) Serum creatinine levels of pediatric en bloc vs. single kidney transplantation on adult recipients at the post-transplant, 1-week, 1-month, 3-months, and 1-year marks; (<b>b</b>) eGFR levels of pediatric en bloc vs. single kidney transplantation on adult recipients at the post-transplant, 1-week, 1-month, 3-months, and 1-year marks.</p>
Full article ">
17 pages, 2695 KiB  
Article
Enhancing the Performance of Tangential Flow Microfiltration for Bioreactor Clarification
by Amir Hossein Mostafavi, Liang-Kai Chu, Xianghong Qian, John Paul Smelko, Da Zhang, Andrew Zydney and Sumith Ranil Wickramasinghe
Membranes 2025, 15(3), 78; https://doi.org/10.3390/membranes15030078 - 3 Mar 2025
Abstract
Tangential flow microfiltration is easily adapted for batch and continuous bioreactor clarification. The permeate can be introduced directly to the subsequent capture step. However, the commercial use of tangential flow filtration (TFF) is limited by membrane fouling, leading to a compromised performance. Here, [...] Read more.
Tangential flow microfiltration is easily adapted for batch and continuous bioreactor clarification. The permeate can be introduced directly to the subsequent capture step. However, the commercial use of tangential flow filtration (TFF) is limited by membrane fouling, leading to a compromised performance. Here, we explored the possibility of reducing membrane fouling by integrating a hydrocyclone as the primary clarification operation. The overflow from the hydrocyclone was introduced directly as the feed to the microfiltration module. Chinese hamster ovary cells were used as the feed stream to investigate the feasibility of this integrated process. A range of cell viabilities from 0% (cell lysate) to 96% were investigated. The cell densities ranged from 0.9 to 10 million cells per mL. Two commercially available hollow fiber microfiltration membranes were used, an essentially symmetric membrane and a reverse asymmetric membrane where the more open support structure faced the feed stream. The reverse asymmetric membrane was more resistant to fouling in the absence of an integrated hydrocyclone. Integrating a hydrocyclone led to a reduction in the flux decline for the symmetric membrane, but did not affect the performance of the reverse asymmetric membrane. The careful choice of membrane morphology and pore size is important when designing an integrated process. Full article
Show Figures

Figure 1

Figure 1
<p>Schematic of a hydrocyclone; (<b>a</b>) flow pattern and (<b>b</b>) nomenclature for relevant components.</p>
Full article ">Figure 2
<p>CAD drawings of hydrocyclones in SolidWorks. (<b>a</b>) Design I and (<b>b</b>) design II.</p>
Full article ">Figure 3
<p>Experimental setups used here (<b>a</b>) TFF, (<b>b</b>) hydrocyclone, and (<b>c</b>) integrated hydrocyclone–TFF.</p>
Full article ">Figure 4
<p>SEM images of (<b>a</b>) UJP cross section, with inside diameter of 1.1 mm, courtesy of Asahi Kasei Corporation; (<b>b</b>–<b>e</b>) BioOptimal MF-SL, with inside diameter of 1.4 mm; and (<b>b</b>,<b>c</b>) cross section showing clear asymmetric structure, (<b>d</b>) outside surface, and (<b>e</b>) inside surface, courtesy of Asahi Kasei Bioprocess.</p>
Full article ">Figure 5
<p>Flux versus productivity for BioOptimal MF-SL and UJP filters under a range of feed conditions. Percentages in the legend represent different cell viabilities. All results are for BioOptimal unless noted in the legend.</p>
Full article ">Figure 6
<p>Variation in underflow split ratio and pressure drop with inlet feed velocity.</p>
Full article ">Figure 7
<p>Separation efficiency versus inlet velocity. (<b>a</b>) Comparison of efficiency of hydrocyclone design 1 with results of He et al. [<a href="#B18-membranes-15-00078" class="html-bibr">18</a>]; (<b>b</b>) comparison of efficiency of design II with results of Syed et al. [<a href="#B17-membranes-15-00078" class="html-bibr">17</a>].</p>
Full article ">Figure 8
<p>Variation in viable cell density and cell viability over a 14-day perfusion experiment. A BioOptimal MF SL microfilter was run in ATF mode as the cell retention device.</p>
Full article ">Figure 9
<p>Variation in permeate flux with time: (<b>a</b>) BioOptimal and hydrocyclone–BioOptimal system and (<b>b</b>) UJP and hydrocylone–UJP system. Data for the integrated systems were obtained with the same module used for the TFF alone, but after cleaning/regeneration.</p>
Full article ">
13 pages, 3743 KiB  
Article
Inserting an Additional Vortex Finder to Improve the Performance of Cyclones in Series
by Weihong He, Jingxuan Yang and Guogang Sun
Separations 2025, 12(3), 60; https://doi.org/10.3390/separations12030060 - 3 Mar 2025
Abstract
Multiple cyclones working in series are sufficient for heavy separation tasks at the cost of significant energy consumption. The majority of researchers conducting optimization studies on multiple cyclones have attempted to find the best possible compromise between pressure drop and collection efficiency by [...] Read more.
Multiple cyclones working in series are sufficient for heavy separation tasks at the cost of significant energy consumption. The majority of researchers conducting optimization studies on multiple cyclones have attempted to find the best possible compromise between pressure drop and collection efficiency by optimizing the geometry of the cyclones. In a departure from this approach, we report a novel design. Using the proposed method, exit gas is divided into dirty and clean gas by inserting a secondary vortex finder (SVF) into the primary vortex finder (PVF) of the previous cyclone. The dirty gas flows into the succeeding cyclone, whereas the clean gas passes over the succeeding cyclone and directly flows into the device farther behind. Methodologically, the separation performance was tested experimentally, and computational fluid dynamics (CFD) simulations were employed. The Reynolds Stress Model (RSM) for turbulence and the Discrete Phase Model (DPM) were used to simulate the turbulent two-phase flow within the gas–solid separator, capturing the three-dimensional, transient, and turbulent characteristics of the flow. Our performance test results showed that the new series configuration clearly reduces energy consumption while not hindering overall efficiency. The CFD simulation was used to optimize the SVF’s diameter and length. The results indicated that having an SVF with optimal dimensions significantly enhances the vortex flow in the separation space and thus improves the efficiency of the previous cyclone. In addition, an equation was established that describes the volume of gas flowing into a succeeding cyclone. Full article
Show Figures

Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>Schematic illustration of the experimental equipment: (<b>a</b>) the experimental apparatus and (<b>b</b>) the geometries of two-stage cyclones [<a href="#B28-separations-12-00060" class="html-bibr">28</a>].</p>
Full article ">Figure 2
<p>(<b>a</b>) Mesh independence verification; (<b>b</b>) mesh model; (<b>c</b>) validation of the CFD simulation method.</p>
Full article ">Figure 2 Cont.
<p>(<b>a</b>) Mesh independence verification; (<b>b</b>) mesh model; (<b>c</b>) validation of the CFD simulation method.</p>
Full article ">Figure 3
<p>The experimental performance of normal and new series configurations: (<b>a</b>) separation efficiencies of the primary cyclone in both configurations; (<b>b</b>) separation efficiencies of the secondary cyclone in both configurations; (<b>c</b>) overall separation efficiency in both configurations; (<b>d</b>) overall pressure drop in both configurations.</p>
Full article ">Figure 4
<p>The effect of the secondary vortex finder dimensions on tangential velocity: (<b>a</b>) length and (<b>b</b>) diameter.</p>
Full article ">Figure 5
<p>The effect of secondary vortex finder dimensions on the gas volume flowed into the secondary cyclone: (<b>a</b>) length and (<b>b</b>) diameter.</p>
Full article ">
16 pages, 4460 KiB  
Article
Tailoring the Performance of a Composite PEI Nanofiltration Membrane via Incorporating Activated PDA for Efficient Dye Sieving and Salt Separation
by Wanting Li, Jiaye Liu, Weifu Wang, Shichun Chen, Fengwei Jia, Xiang Li, Ying Zhao, Wenjuan Zhang, Dan Song and Jun Ma
Membranes 2025, 15(3), 75; https://doi.org/10.3390/membranes15030075 - 2 Mar 2025
Viewed by 100
Abstract
Efficient dye sieving and salt separation can facilitate the recycling of valuable resources in textile wastewater treatment. This study focuses on developing a high-performance nanofiltration membrane (NF) by co-depositing activated polydopamine (O-PDA), oxidized with KMnO4, and polyethyleneimine (PEI) onto a polysulfone [...] Read more.
Efficient dye sieving and salt separation can facilitate the recycling of valuable resources in textile wastewater treatment. This study focuses on developing a high-performance nanofiltration membrane (NF) by co-depositing activated polydopamine (O-PDA), oxidized with KMnO4, and polyethyleneimine (PEI) onto a polysulfone support membrane (PSF), thereby enabling effective dye sieving and salt separation. Due to the high hydrophilicity of PDA and the formation of high molecular polymers after oxidation, it was anticipated that O-PDA would crosslink the PEI layer, providing rapid permeating channels. Filtration experiments demonstrated that the formation of O-PDA significantly enhanced the salt retention rate of nanofiltration membranes, achieving a nearly threefold increase in NaCl retention from 15% to 45.7%. It was observed that the retention performance of O-PDA could be adjusted by controlling its loading or oxidation level. Furthermore, despite a notable reduction in permeability, the dye removal efficiency of the O-PDA/PEI membrane increased substantially to 99.5%. Long-term filtration experiments also confirmed both the stability and anti-fouling properties of this membrane design. Clearly, owing to its excellent operational stability and anti-fouling characteristics, the O-PDA/PEI membrane exhibits great potential for applications in dye sieving and salt separation. Full article
Show Figures

Figure 1

Figure 1
<p>Schematic diagram of the membrane preparation process.</p>
Full article ">Figure 2
<p>Schematic diagram of the cross-flow membrane filtration test setup.</p>
Full article ">Figure 3
<p>UV-vis absorbance at 357 nm and 420 nm for KMnO<sub>4</sub>-activated DA solutions with varying molar ratios.</p>
Full article ">Figure 4
<p>Surface images of the (<b>a</b>) PSf, DE, KD, and KDE8 membranes; (<b>b</b>) surface roughness of the PSf, DE, KD, and KDE8 membranes; and (<b>c</b>) roughness parameters (<span class="html-italic">R<sub>q</sub></span>, <span class="html-italic">R<sub>a</sub></span> and <span class="html-italic">R<sub>p</sub></span>) of the membranes.</p>
Full article ">Figure 5
<p>ATR-FTIR spectra of the PSf, KD, and KDE8 membranes.</p>
Full article ">Figure 6
<p>(<b>a</b>) XPS spectra overview for the PSf, KD, KDE2, and KDE8 membranes. (<b>b</b>) Elemental distribution on the membrane surfaces pre- and post-modification. High-resolution XPS N1s spectra of the (<b>c</b>) KDE8-C1s and (<b>d</b>) KDE8-N1s.</p>
Full article ">Figure 7
<p>The changes in (<b>a</b>) CA and (<b>b</b>) zeta potential on the membrane surface pre- and post-modification.</p>
Full article ">Figure 8
<p>(<b>a</b>) Membrane permeability, (<b>b</b>) rejection of salts, and (<b>c</b>) dyes of pre- and post-modification.</p>
Full article ">Figure 9
<p>(<b>a</b>) Membrane permeability in two cycles of filtration and (<b>b</b>) the flux recovery of these membranes after BSA fouling cleaning processes.</p>
Full article ">
28 pages, 8440 KiB  
Article
Feasibility Study of Biodegradable Vegetable Peels as Sustainable Fluid Loss Additives in Water-Based Drilling Fluids
by Olajide Ibrahim Oladipo, Foad Faraji, Hossein Habibi, Mardin Abdalqadir, Jagar A. Ali and Perk Lin Chong
J 2025, 8(1), 10; https://doi.org/10.3390/j8010010 - 1 Mar 2025
Viewed by 231
Abstract
Drilling fluids are vital in oil and gas well operations, ensuring borehole stability, cutting removal, and pressure control. However, fluid loss into formations during drilling can compromise formation integrity, alter permeability, and risk groundwater contamination. Water-based drilling fluids (WBDFs) are favored for their [...] Read more.
Drilling fluids are vital in oil and gas well operations, ensuring borehole stability, cutting removal, and pressure control. However, fluid loss into formations during drilling can compromise formation integrity, alter permeability, and risk groundwater contamination. Water-based drilling fluids (WBDFs) are favored for their environmental and cost-effective benefits but often require additives to address filtration and rheological limitations. This study explored the feasibility of using vegetable waste, including pumpkin peel (PP), courgette peel (CP), and butternut squash peel (BSP) in fine (75 μm) and very fine (10 μm) particle sizes as biodegradable WBDF additives. Waste vegetable peels were processed using ball milling and characterized via FTIR, TGA, and EDX. WBDFs, prepared per API SPEC 13A with 3 wt% of added additives, were tested for rheological and filtration properties. Results highlighted that very fine pumpkin peel powder (PP_10) was the most effective additive, reducing fluid loss and filter cake thickness by 43.5% and 50%, respectively. PP_10 WBDF maintained mud density, achieved a pH of 10.52 (preventing corrosion), and enhanced rheological properties, including a 50% rise in plastic viscosity and a 44.2% increase in gel strength. These findings demonstrate the remarkable potential of biodegradable vegetable peels as sustainable WBDF additives. Full article
Show Figures

Figure 1

Figure 1
<p>Flowchart of procedural steps.</p>
Full article ">Figure 2
<p>Process flow diagram for the synthesis and characterization of biodegradable drilling fluid additives from vegetable peels.</p>
Full article ">Figure 3
<p>EDX analysis for (<b>a</b>) butternut squash peel, (<b>b</b>) courgette peel, (<b>c</b>) pumpkin peel, and FESEM analysis for (<b>d</b>) butternut squash peel, (<b>e</b>) courgette peel, and (<b>f</b>) pumpkin peel.</p>
Full article ">Figure 4
<p>FTIR analysis for (<b>a</b>) butternut squash peel, (<b>b</b>) courgette peel, and (<b>c</b>) pumpkin peel.</p>
Full article ">Figure 5
<p>TGA analysis for (<b>a</b>) butternut squash peel, (<b>b</b>) courgette peel, and (<b>c</b>) pumpkin peel.</p>
Full article ">Figure 5 Cont.
<p>TGA analysis for (<b>a</b>) butternut squash peel, (<b>b</b>) courgette peel, and (<b>c</b>) pumpkin peel.</p>
Full article ">Figure 6
<p>Yield point, plastic viscosity, and apparent viscosity of base mud (BM) and biodegradable drilling fluids with vegetable peel additives at particle sizes (<b>a</b>) below 75 µm and (<b>b</b>) below 10 µm.</p>
Full article ">Figure 7
<p>Initial and final gel strength of BM and biodegradable drilling fluids with vegetable peel additives at particle sizes (<b>a</b>) below 75 µm and (<b>b</b>) below 10 µm.</p>
Full article ">Figure 8
<p>The relationship between shear strain rate and shear stress of (<b>a</b>) biodegradable pumpkin peel at 75 µm particle size, (<b>b</b>) biodegradable pumpkin peel at 10 µm particle size, (<b>c</b>) biodegradable butternut squash peel at 75 µm particle size, (<b>d</b>) biodegradable at butternut squash peel 10 µm at particle size, (<b>e</b>) biodegradable courgette peel at 75 µm particle size, and (<b>f</b>) biodegradable courgette peel at 10 µm particle size.</p>
Full article ">Figure 8 Cont.
<p>The relationship between shear strain rate and shear stress of (<b>a</b>) biodegradable pumpkin peel at 75 µm particle size, (<b>b</b>) biodegradable pumpkin peel at 10 µm particle size, (<b>c</b>) biodegradable butternut squash peel at 75 µm particle size, (<b>d</b>) biodegradable at butternut squash peel 10 µm at particle size, (<b>e</b>) biodegradable courgette peel at 75 µm particle size, and (<b>f</b>) biodegradable courgette peel at 10 µm particle size.</p>
Full article ">Figure 8 Cont.
<p>The relationship between shear strain rate and shear stress of (<b>a</b>) biodegradable pumpkin peel at 75 µm particle size, (<b>b</b>) biodegradable pumpkin peel at 10 µm particle size, (<b>c</b>) biodegradable butternut squash peel at 75 µm particle size, (<b>d</b>) biodegradable at butternut squash peel 10 µm at particle size, (<b>e</b>) biodegradable courgette peel at 75 µm particle size, and (<b>f</b>) biodegradable courgette peel at 10 µm particle size.</p>
Full article ">Figure 9
<p>(<b>a</b>) Viscosity and (<b>b</b>) shear stress as functions of shear rates of BM and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm.</p>
Full article ">Figure 10
<p>(<b>a</b>) Mud balance test, (<b>b</b>) pH analysis of BM, and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm.</p>
Full article ">Figure 10 Cont.
<p>(<b>a</b>) Mud balance test, (<b>b</b>) pH analysis of BM, and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm.</p>
Full article ">Figure 11
<p>(<b>a</b>) Filtration rate over time, (<b>b</b>) filtration rate at 30 min of BM, and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm.</p>
Full article ">Figure 12
<p>Filter cakes thickness of BM and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm.</p>
Full article ">Figure 13
<p>Mechanism of filter cake formation on the borehole wall using BM and biodegradable drilling fluids with vegetable peel additives at particle sizes below 75 µm and 10 µm. The direction of the drilling mud during the operation is shown by the arrows.</p>
Full article ">
34 pages, 7443 KiB  
Review
Metal–Organic Frameworks (MOFs) for Adsorption and Degradation of Microplastics
by Thayna Campeol Marinho, Almudena Gomez-Aviles and Pilar Herrasti
Microplastics 2025, 4(1), 11; https://doi.org/10.3390/microplastics4010011 - 1 Mar 2025
Viewed by 72
Abstract
Microplastics (MPs) are currently a serious environmental problem, primarily due to their persistence in the environment, low concentration, and difficulty in detection and disposal. MPs have also been detected in humans and have been shown to be harmful. Although there are methodologies for [...] Read more.
Microplastics (MPs) are currently a serious environmental problem, primarily due to their persistence in the environment, low concentration, and difficulty in detection and disposal. MPs have also been detected in humans and have been shown to be harmful. Although there are methodologies for their recovery or elimination in most water treatment plants, a significant portion still bypasses these elimination systems. It is this percentage that we must try to eliminate. In addition to finding new methodologies for the treatment of MPs, it is important to find new materials adapted to this process. In this context, metal–organic frameworks (MOFs) are high-versatility compounds that can be synthesized using different techniques to obtain materials with different properties, such as porosity, morphology, conductivity, etc. These materials can adsorb MPs in different ways, such as electrostatic interaction, bond formation, etc., or they can be obtained by containing metals that catalyze reactions for the formation of highly reactive species that can oxidize the MPs. This review examines how MOF materials have gained attention for the adsorption-based recovery and removal of MPs and discusses the problems associated with these materials and possible solutions. Full article
Show Figures

Figure 1

Figure 1
<p>Scheme of methodologies to separate MPs from the environment.</p>
Full article ">Figure 2
<p>Scheme of employment methods for MP degradation.</p>
Full article ">Figure 3
<p>Number of MOF structures in the Cambridge Structural Database (CSD) and MOF reports found in the Web of Science, from 1976 to 2019. Reprinted with permission from [<a href="#B74-microplastics-04-00011" class="html-bibr">74</a>]. Copyright 2020. Royal Society of Chemistry.</p>
Full article ">Figure 4
<p>Commonly methods employed to synthesize MOFs.</p>
Full article ">Figure 5
<p>Illustration showing the mechanisms between MOFs and adsorbates (microplastic). Reprinted with permission from [<a href="#B153-microplastics-04-00011" class="html-bibr">153</a>]. Copyright 2022. Elsevier.</p>
Full article ">Figure 6
<p>(<b>a</b>) The removal efficiency of UiO-66-X@MF (X = H, NH<sub>2</sub>, OH, Br, and NO<sub>2</sub>) and (<b>b</b>) the efficiency performance of UiO-66-OH@MF-3 after 10 cycles. Reprinted with permission from [<a href="#B154-microplastics-04-00011" class="html-bibr">154</a>]. Copyright 2020. Royal Society of Chemistry.</p>
Full article ">Figure 7
<p>(<b>a</b>) Photographs of the device for large-quantity filtration testing (flow rate: ~0.25 L/h). (<b>b</b>) The photo of the automatic filtration system on the lab-scale. (<b>c</b>) Schematic representation of the possible interactions between MPs and foam materials. Reprinted with permission from [<a href="#B154-microplastics-04-00011" class="html-bibr">154</a>]. Copyright 2020. Royal Society of Chemistry.</p>
Full article ">Figure 8
<p>Effects of MP concentration and adsorption capacity and removal rate of MOF-545 and MOF-545-oxime. Reprinted with permission from [<a href="#B155-microplastics-04-00011" class="html-bibr">155</a>]. Copyright 2023. Elsevier.</p>
Full article ">Figure 9
<p>Molecular structure of (a) Cr-MOF and (b) polystyrene nanoplastics. Three main mechanisms of electrostatic, acid–base, and π–π interaction are dominant adsorption mechanisms of PSNPs on Cr-MOF. Reprinted with permission from [<a href="#B157-microplastics-04-00011" class="html-bibr">157</a>]. Copyright 2023. American Chemical Society.</p>
Full article ">Figure 10
<p>Four-cycle regeneration of Cr-MOF using NaOH for removing 5 ppm PSNPs using 100 ppm of regenerated Cr-MOF. Reprinted with permission from [<a href="#B157-microplastics-04-00011" class="html-bibr">157</a>]. Copyright 2023. American Chemical Society.</p>
Full article ">Figure 11
<p>The efficiency of the simultaneous removal of bisphenol A and 4-tert-butylphenol and MPs in Milli-Q water and tap water. Figure reprinted with permission from [<a href="#B158-microplastics-04-00011" class="html-bibr">158</a>]. Copyright 2023 Elsevier.</p>
Full article ">Figure 12
<p>Schematic representation of the fabrication process of PSF/MIL-100 (Fe) membranes. Reprinted with permission from [<a href="#B169-microplastics-04-00011" class="html-bibr">169</a>]. Copyright 2021. Elsevier.</p>
Full article ">Figure 13
<p>Proposed mechanism of catalytic degradation of PE by M/B-40% under simulated solar light. Reprinted with permission from [<a href="#B175-microplastics-04-00011" class="html-bibr">175</a>]. Copyright 2024. Elsevier.</p>
Full article ">Figure 14
<p>Scheme of photoelectrocatalytic (PEC) oxidation. Reprinted with permission [<a href="#B183-microplastics-04-00011" class="html-bibr">183</a>]. Copyright 2021. Elsevier.</p>
Full article ">
17 pages, 5147 KiB  
Article
Bacterial Contamination of Ultrafiltration Installation Applied to Carwash Wastewater Treatment
by Piotr Woźniak and Marek Gryta
Membranes 2025, 15(3), 71; https://doi.org/10.3390/membranes15030071 - 1 Mar 2025
Viewed by 106
Abstract
An ultrafiltration (UF) installation was used to separate the actual wastewater from a car wash. Following these studies, the plant was washed several times; however, severe membrane fouling was observed during the filtration of sterile deionised (DI) water. As a result, the permeate [...] Read more.
An ultrafiltration (UF) installation was used to separate the actual wastewater from a car wash. Following these studies, the plant was washed several times; however, severe membrane fouling was observed during the filtration of sterile deionised (DI) water. As a result, the permeate flux decreased by more than 50% after 5 h of the UF process. The source of the fouling was the release of deposits, particularly bacteria, from the surfaces of plant elements such as pipes and pumps. The paper presents the effectiveness of biofilm removal from the surface of the equipment during a cyclically repeated washing process. Chemical washing was carried out using acid solutions and alkaline cleaning solutions containing NaOH (pH = 11.5–12). After installation cleaning, the filtration tests were carried out using DI water as a feed. It was determined how biofouling, which develops under these conditions, reduces permeate flux. Despite 3 h of installation washing, there was a 50% reduction in flux after 10 h of UF. Repeating the installation wash (4 h) resulted in a similar decrease in flux after 4 days of UF. Stabilisation of the flux at a level of 500 LMH was achieved after an additional 5 h of washing, including application of hot (323–333 K) alkaline cleaning solutions. The number of bacteria in the biofilm collected from the surface of the membranes, the pump inlet and the surface of the polyvinyl chloride (PVC) hoses forming the pipeline was also investigated. Despite repeated chemical cleaning, the number of bacteria on the pump and hose surfaces was 50–100 CFU/cm2. Studies were carried out to determine which bacterial species survived the chemical cleaning of the installation. Gram-positive and Gram-negative bacteria were determined, and taxonomic characteristics of the isolated bacteria were identified. Full article
(This article belongs to the Special Issue Membrane Fouling during Water/Wastewater Treatment Processes)
Show Figures

Figure 1

Figure 1
<p>Experimental set-up of the UF installation with two plate-and-frame membrane modules (A and B). 1—module, 2—pump, 3—feed tank, 4—thermostat, 5—valve and P—manometer.</p>
Full article ">Figure 2
<p>PVC hose disconnected from a 3CP Stainless Steel Plunger Pump to take a sample of the biofilm from the inside of the hose and the inlet port to the pump. Arrows—biofilm collection point.</p>
Full article ">Figure 3
<p>SEM images of UE50 membranes (module A): (<b>a</b>) yellow line—seal location in UF module, to its left side active membrane area with deposit; (<b>b</b>) enlarged image of deposit.</p>
Full article ">Figure 4
<p>Permeate flux changes during 2 days of DI water filtration tests. Point N–overnight shutdown.</p>
Full article ">Figure 5
<p>SEM images of deposits on the PES membranes surface after 2 days filtration of DI water. (<b>a</b>) Membrane UE10 (module A), (<b>b</b>) membrane UE50 (module B).</p>
Full article ">Figure 6
<p>Permeate flux changes during 3 days of DI water filtration tests. Point N–overnight shutdown, W–membrane washing with P3 Ultrasil 11 solution (pH = 12, T = 313–323 K).</p>
Full article ">Figure 7
<p>SEM images of deposits on the UE50 membranes surface (<b>a</b>) after 3 days filtration of distilled water (module A); (<b>b</b>) after membrane washing (module B).</p>
Full article ">Figure 8
<p>Changes in the permeate flux during filtration of DI water. TMP = 0.3 MPa. Point N—overnight shutdown.</p>
Full article ">Figure 9
<p>SEM images of UE50 membrane after 5 days filtration of DI water (<a href="#membranes-15-00071-f008" class="html-fig">Figure 8</a>). (<b>a</b>) Deposits on the membrane surface; (<b>b</b>) Bacteria inside deposits. Sample taken from module A.</p>
Full article ">Figure 10
<p>The phylogenetic tree of the bacteria identified on the membrane surface. Groups ♦ <span class="html-italic">Alphaproteobacteria</span>, ■ <span class="html-italic">Betaproteobacteria</span>, ● <span class="html-italic">Gammaproteobacteria</span>, ▲ <span class="html-italic">Enterobacteria</span>, □ <span class="html-italic">Bacillota</span>, ○ FCB group.</p>
Full article ">Figure 11
<p>Effect of washing process application on the number of bacteria in the biofilm. UF–biofilm sample taken after the UF process (<a href="#membranes-15-00071-f008" class="html-fig">Figure 8</a>).</p>
Full article ">Figure 12
<p>Effect of feed flow rate (rpm pump speed) on the permeate flux and changes in feed and permeate turbidity. Feed—DI water, point ‘F’—fresh portion of DI water. The dash lines−rpm values (division into periods).</p>
Full article ">Figure 13
<p>SEM images of seal surface: (<b>a</b>) deposits on seal, (<b>b</b>) rod-shaped bacteria in the deposits.</p>
Full article ">
17 pages, 2091 KiB  
Article
The Purification and Characterization of a Novel Neutral Protease from Volvariella volvacea Fruiting Bodies and the Enzymatic Digestion of Soybean Isolates
by Baoting Xu, Zhiping Li, Qian Guo, Lei Zha, Chuanhua Li, Panling Yu, Mingjie Chen and Yan Zhao
J. Fungi 2025, 11(3), 190; https://doi.org/10.3390/jof11030190 - 1 Mar 2025
Viewed by 105
Abstract
A novel protease was isolated from the fruiting bodies of the straw mushroom Volvariella volvacea. The protease was purified 13.48-fold using a series of techniques, including ammonium sulfate precipitation, ultrafiltration, diethylaminoethyl fast-flow (DEAE FF) ion-exchange chromatography, and Superdex 75 gel filtration chromatography, [...] Read more.
A novel protease was isolated from the fruiting bodies of the straw mushroom Volvariella volvacea. The protease was purified 13.48-fold using a series of techniques, including ammonium sulfate precipitation, ultrafiltration, diethylaminoethyl fast-flow (DEAE FF) ion-exchange chromatography, and Superdex 75 gel filtration chromatography, resulting in a specific enzyme activity of 286.82 U/mg toward casein as a substrate. Sodium dodecyl sulfate–polyacrylamide gel electrophoresis (SDS-PAGE) analysis revealed that the purified protease had a molecular weight of 24 kDa. The enzyme exhibited optimal activity at pH 7 and 50 °C, showing sensitivity to alkaline conditions and instability at elevated temperatures. The presence of Ca2+ significantly enhanced enzyme activity, whereas Ni2+ and Cu2+ exerted strong inhibitory effects, with other metal ions showing weak inhibition. β-mercaptoethanol, Tween-80, and Triton X-100 had more pronounced inhibitory effects, whereas PMSF, EDTA, and CTAB had weaker inhibitory effects. The Michaelis constant (Km) and maximum velocity (Vm) of the protease were determined to be 1.34 g/L and 3.45 μg/(mL·min), respectively. The protease exhibited a greater degree of enzymatic degradation of soybean-isolate protein (7.58%) compared to trypsin (5.24%), with the enzyme product containing a high percentage of medicinal amino acids (73.54%), particularly phenylalanine (Phe) and arginine (Arg), suggesting their presence at the enzyme’s active site. These findings suggest that the protease from V. volvacea holds promising potential for applications in the food industry, particularly in protein hydrolysate production and flavor enhancement. Full article
Show Figures

Figure 1

Figure 1
<p>(<b>A</b>) Elution profile from DEAE-Sepharose FF. Numbers 1, 2, and 3 indicate distinct protein peaks; (<b>B</b>) Sephadex G-75 gel column chromatography profile. The protein content was expressed as the absorbance at 280 nm, and protease activity was expressed as the absorbance at 680 nm. (<b>C</b>) SDS-PAGE diagram of <span class="html-italic">V. volvacea</span> proteases. Lane 1, molecular weight marker; Lane 2, ammonium sulfate precipitation; Lane 3, DEAE FF ion-exchange chromatography; Lane 4, Sephadex G-75.</p>
Full article ">Figure 2
<p>(<b>A</b>) Effects of pH on protease activity and stability; (<b>B</b>) effects of temperature on protease activity; (<b>C</b>) effects of temperature on protease stability.</p>
Full article ">Figure 3
<p>Kinetic parameters of <span class="html-italic">V. volvacea</span> protease using casein as the substrate. (<b>A</b>) Reaction rate (V) as a function of casein concentration (S). (<b>B</b>) Lineweaver–Burk plot (1/V vs. 1/S) for determining Km and Vm.</p>
Full article ">Figure 4
<p>Enzymatic hydrolysis of soybean-isolate proteins by proteases. (<b>A</b>) Influence of pH on the degree of hydrolysis mediated by <span class="html-italic">V. volvacea</span> protease. (<b>B</b>) Impact of temperature on the degree of hydrolysis facilitated by <span class="html-italic">V. volvacea</span> protease. (<b>C</b>) Effects of reaction time on the degree of hydrolysis achieved with both proteases.</p>
Full article ">Figure 5
<p>High-performance liquid chromatographic profile of the product following enzymatic digestion. (<b>A</b>) <span class="html-italic">V. volvacea</span> protease; (<b>B</b>) Trypsin.</p>
Full article ">
18 pages, 272 KiB  
Article
Quality Parameters of Wort Produced with Lentil Malt with the Use of Some Enzymatic Preparations
by Katarzyna Fulara, Aneta Ciosek, Olga Hrabia, Monika Cioch-Skoneczny, Krystian Klimczak and Aleksander Poreda
Foods 2025, 14(5), 848; https://doi.org/10.3390/foods14050848 - 1 Mar 2025
Viewed by 226
Abstract
Lentils represent a promising alternative for beer production, potentially offering unique benefits and challenges. This study investigates the physicochemical properties of brewer’s wort derived from both barley and lentil grains. Specifically, it compares worts produced from raw and malted lentils, with and without [...] Read more.
Lentils represent a promising alternative for beer production, potentially offering unique benefits and challenges. This study investigates the physicochemical properties of brewer’s wort derived from both barley and lentil grains. Specifically, it compares worts produced from raw and malted lentils, with and without the addition of amylase and protease enzymes. Key parameters such as filtration and saccharification times, pH, extract content, color, turbidity, polyphenol content, free amino nitrogen (FAN), nitrogen content, and metal ion and sugar composition were meticulously measured. Results indicate that both raw and malted lentils can be utilized to produce brewer’s wort, with the malting process enhancing extract levels. Notably, the addition of amylolytic enzymes resulted in the highest extract levels for both lentil types. Lentil-based worts exhibited significantly higher FAN levels and lower turbidity compared to barley malt worts. Despite barley malt’s established advantages in saccharification efficiency, filtration, and extract yield, lentils offer distinct benefits such as elevated FAN levels and unique color profiles. Enzyme treatments play a crucial role in optimizing lentil-based wort production, highlighting the potential for lentils in brewing applications. Full article
(This article belongs to the Section Food Biotechnology)
11 pages, 1032 KiB  
Article
The Patient and Treatment Characteristics of Kidney Transplant Recipients with a Clinically Relevant Jaffe/Enzymatic Serum Creatinine Difference
by Kristina Boss, Susanne Stolpe, André Müller, Justa Friebus-Kardash, Bernd Wagner, Marc Wichert, Roland Assert, Lothar Volbracht, Andreas Stang, Bernd Kowall and Andreas Kribben
J. Clin. Med. 2025, 14(5), 1668; https://doi.org/10.3390/jcm14051668 - 28 Feb 2025
Viewed by 210
Abstract
Background: Differences in serum creatinine (SCr) between the Jaffe and enzymatic methods affect the detection and staging of chronic kidney disease in kidney transplant recipients (KTRs). However, there are very limited data on the extent to which the detection of acute kidney injury [...] Read more.
Background: Differences in serum creatinine (SCr) between the Jaffe and enzymatic methods affect the detection and staging of chronic kidney disease in kidney transplant recipients (KTRs). However, there are very limited data on the extent to which the detection of acute kidney injury (AKI) is affected, what impact immunosuppression can have and whether a KTR-specific estimated glomerular filtration rate (eGFR) formula is beneficial. Methods: A total of 12,081 parallel Jaffe/enzymatic SCr (eSCr) measurements of adult outpatient KTRs (61% male, median age 53 years) in the same serum sample at the University Hospital Essen (Germany) between January 2020 and October 2023 were evaluated. AKI and CKD were defined according to current KDIGO guidelines. The GFR was estimated using CKD-EPI and KTR-specific formulas. Results: In about 1% of all measurements and 5% of the KTR patients, the SCr difference between the two methods was ≥ 0.3 mg/dl. A total of 81% of these patients were male; the median age was 52 years. High levels of immunosuppression, including when Belatacept was used, did not seem to have a clinically relevant impact on the difference between Jaffe and eSCr. The KTR-specific eGFR formula generally showed a greater agreement between Jaffe and eSCr than the CKD-EPI eGFR formula, but they showed differences in the classification of CKD stages, especially in less severe stages. Conclusions: Clinically relevant SCr differences between Jaffe and SCr are rare and depend on the type of immunosuppression. A KTR-specific eGFR formula could be beneficial in some cases, but there are limitations in less severe CKD stages. Full article
(This article belongs to the Section Nephrology & Urology)
20 pages, 5438 KiB  
Article
Separation of Simultaneous Speakers with Acoustic Vector Sensor
by Józef Kotus and Grzegorz Szwoch
Sensors 2025, 25(5), 1509; https://doi.org/10.3390/s25051509 - 28 Feb 2025
Viewed by 81
Abstract
This paper presents a method of sound source separation in live audio signals, based on sound intensity analysis. Sound pressure signals recorded with an acoustic vector sensor are analyzed, and the spectral distribution of sound intensity in two dimensions is calculated. Spectral components [...] Read more.
This paper presents a method of sound source separation in live audio signals, based on sound intensity analysis. Sound pressure signals recorded with an acoustic vector sensor are analyzed, and the spectral distribution of sound intensity in two dimensions is calculated. Spectral components of the analyzed signal are selected based on the calculated source direction, which leads to a spatial filtration of the sound. The experiments were performed with test signals convolved with impulse responses of a real sensor, recorded for a varying sound source position. The experiments evaluated the proposed method’s ability to separate sound sources, depending on their position, spectral content, and signal-to-noise ratio, especially when multiple sources are active at the same time. The obtained results are presented and discussed. The proposed algorithm provided signal-to-distortion ratio (SDR) values 10–12 dB, and Short-Time Objective Intelligibility Measure (STOI) values in the range 0.86–0.94, an increase by 0.15–0.30 compared with the unprocessed speech signal. The proposed method is intended for applications in automated speech recognition systems, speaker diarization, and separation in the concurrent speech scenarios, using a small acoustic sensor. Full article
Show Figures

Figure 1

Figure 1
<p>Block diagram of the proposed algorithm for the separation of the desired signal from the disturbance.</p>
Full article ">Figure 2
<p>Example spectrograms: (<b>a</b>) input signal to the algorithm—male speech <span class="html-italic">x<sub>s</sub></span> at 0° mixed with the disturbance <span class="html-italic">x<sub>n</sub></span> (female speech) at 30°, (<b>b</b>) the processing result <span class="html-italic">y<sub>s</sub></span>, and (<b>c</b>) the original signal <span class="html-italic">x<sub>s</sub></span>. Color represents the spectral magnitude level in dB.</p>
Full article ">Figure 3
<p>Example of the signal processing: a binary spectral mask. Black color denotes spectral components that are removed from the signal.</p>
Full article ">Figure 4
<p>SDR values calculated between the input <span class="html-italic">x<sub>s</sub></span> and the output <span class="html-italic">y<sub>s</sub></span> signals, for a varying angular distance between the sources. Three combinations of female (F) and male (M) voices are presented.</p>
Full article ">Figure 5
<p>SDR values calculated for a varying azimuth range of interest for the desired signal for the M-F case (M source at 0°, F source at 90°, equal SNR).</p>
Full article ">Figure 6
<p>STOI difference between the processed and the unprocessed signal, for a varying angular distance between the sources.</p>
Full article ">Figure 7
<p>PESQ values calculated for a varying angular distance between the sources.</p>
Full article ">Figure 8
<p>SDR values calculated for a varying input SNR (source distance = 45°).</p>
Full article ">Figure 9
<p>STOI results calculated for a varying input SNR (source distance = 45°): (<b>a</b>) STOI values, and (<b>b</b>) the difference between the STOI for the processed and the unprocessed signal.</p>
Full article ">
18 pages, 3888 KiB  
Article
New Viologen-Based Ionic Porous Organic Polymers for Efficient Removal of Anionic Dyes and Hexavalent Chromium (Cr (VI)) from Water
by Meihan Lu, Lijun Sun, Dongxin Yang, Zewen Nie and Weitao Gong
Molecules 2025, 30(5), 1123; https://doi.org/10.3390/molecules30051123 - 28 Feb 2025
Viewed by 76
Abstract
Water pollution is a critical environmental issue in modern society, and adsorption is recognized as a straightforward and efficient water purification technique. In this study, three new viologen-based ionic porous organic polymers were designed and successfully synthesized via a simple approach, and their [...] Read more.
Water pollution is a critical environmental issue in modern society, and adsorption is recognized as a straightforward and efficient water purification technique. In this study, three new viologen-based ionic porous organic polymers were designed and successfully synthesized via a simple approach, and their adsorption properties for water pollutants were evaluated. The cationic nature of these polymers, coupled with their large conjugated π-electron system, physicochemical stability, and aromatic backbone, contributes to their high adsorption capacity and rapid adsorption efficiency for anionic contaminants in water such as Methyl Orange, Congo Red, and Cr (VI). The polymers exhibited maximum adsorption capacities of 1617 mg/g for MO, 3734 mg/g for CR, and 530.22 mg/g for Cr (VI), surpassing most previously reported adsorbents. Furthermore, the polymers maintained a high removal rate even in the presence of competing anions. Effective separation of anionic dyes from mixed solutions could be achieved through simple filtration. These characteristics make them promising candidates for water purification applications. Full article
(This article belongs to the Special Issue Porous Organic Materials: Design and Applications: Volume II)
Show Figures

Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>(<b>a</b>) FT-IR, (<b>b</b>) PXRD, and (<b>c</b>) SEM results for TET-BIP, TET-BPB, and TET-DBP.</p>
Full article ">Figure 2
<p>Changes in the UV–Vis spectra of MO solution (300 mg/L) with the addition of (<b>a</b>) TET-BIP, (<b>b</b>) TET-BPB, and (<b>c</b>) TET-DBP (each at 0.4 mg/mL) at different time intervals. The first-order and second-order kinetic models fit the adsorption curves of the MO solution after the addition of (<b>d</b>) TET-BIP, (<b>e</b>) TET-BPB, and (<b>f</b>) TET-DBP.</p>
Full article ">Figure 3
<p>Changes in the UV–Vis spectra of CR solution (400 mg/L) with the addition of (<b>a</b>) TET-BIP, (<b>b</b>) TET-BPB, and (<b>c</b>) TET-DBP (each at 0.4 mg/mL) at different time intervals. The first-order and second-order kinetic models fit the adsorption curves of the CR solution after the addition of (<b>d</b>) TET-BIP, (<b>e</b>) TET-BPB, and (<b>f</b>) TET-DBP.</p>
Full article ">Figure 4
<p>UV–Visible spectral changes in MO and MB binary mixtures upon the addition of (<b>a</b>) TET-BIP, (<b>b</b>) TET-BPB, and (<b>c</b>) TET-DBP.</p>
Full article ">Figure 5
<p>Efficiency of MO (<b>a</b>) and CR (<b>b</b>) removal by TET-BIP, TET-BPB, and TET-DBP after 5 cycles.</p>
Full article ">Figure 6
<p>Changes in the UV–Vis spectra of Cr (VI) solution (150mg/L) with the addition of (<b>a</b>) TET-BIP, (<b>b</b>) TET-BPB, and (<b>c</b>) TET-DBP (each at 0.4 mg/mL) at different time intervals. The first-order and second-order kinetic models fit the adsorption curves of the CR solution after the addition of (<b>d</b>) TET-BIP, (<b>e</b>) TET-BPB, and (<b>f</b>) TET-DBP.</p>
Full article ">Figure 7
<p>(<b>a</b>) Impact of interfering ions on the adsorption capacity of TET-BIP, TET-BPB, and TET-DBP. (<b>b</b>) Efficiency of Cr (VI) removal by TET-BIP, TET-BPB, and TET-DBP after 5 cycles. (<b>c</b>) XPS spectra of TET-BPB before and after the adsorption of Cr (VI). (<b>d</b>) Cr2p XPS peaks of TET-BPB after Cr (VI) adsorption.</p>
Full article ">Scheme 1
<p>Synthesis routes of three viologen-based iPOPs.</p>
Full article ">
Back to TopTop