[go: up one dir, main page]

 
 
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

Journals

Article Types

Countries / Regions

Search Results (40)

Search Parameters:
Keywords = microfilter

Order results
Result details
Results per page
Select all
Export citation of selected articles as:
15 pages, 3626 KiB  
Article
Optical Fiber Probe with Integrated Micro-Optical Filter for Raman and Surface-Enhanced Raman Scattering Sensing
by Md Abdullah Al Mamun, Tomas Katkus, Anita Mahadevan-Jansen, Saulius Juodkazis and Paul R. Stoddart
Nanomaterials 2024, 14(16), 1345; https://doi.org/10.3390/nano14161345 - 14 Aug 2024
Viewed by 648
Abstract
Optical fiber Raman and surface-enhanced Raman scattering (SERS) probes hold great promise for in vivo biosensing and in situ monitoring of hostile environments. However, the silica Raman scattering background generated within the optical fiber increases in proportion to the length of the fiber, [...] Read more.
Optical fiber Raman and surface-enhanced Raman scattering (SERS) probes hold great promise for in vivo biosensing and in situ monitoring of hostile environments. However, the silica Raman scattering background generated within the optical fiber increases in proportion to the length of the fiber, and it can swamp the signal from the target analyte. While filtering can be applied at the distal end of the fiber, the use of bulk optical elements has limited probe miniaturization to a diameter of 600 µm, which in turn limits the potential applications. To overcome this limitation, femtosecond laser micromachining was used to fabricate a prototype micro-optical filter, which was directly integrated on the tip of a 125 µm diameter double-clad fiber (DCF) probe. The outer surface of the microfilter was further modified with a nanostructured, SERS-active, plasmonic film that was used to demonstrate proof-of-concept performance with thiophenol as a test analyte. With further optimization of the associated spectroscopic system, this ultra-compact microprobe shows great promise for Raman and SERS optical fiber sensing. Full article
Show Figures

Figure 1

Figure 1
<p>Schematic of the microfilter assembly on the DCF tip. Filter coatings are deposited onto both sides of a UV-grade fused silica substrate. A ring of the short-pass coating is ablated out to the diameter of the inner cladding, leaving an island at the center that blocks Raman-scattered light from the single/few-mode core. The LPF on the second side of the glass substrate has a hole drilled into the axis of the core to pass the clean laser excitation and reduce the intensity of Rayleigh-scattered light from the sample that returns to the inner cladding. Depending on the transmission characteristics of the sample, a second glass plate can be used to allow the Raman-scattered light from the sample to completely fill the aperture of the inner cladding. The SERS substrate is deposited onto the spacer plate as required.</p>
Full article ">Figure 2
<p>Schematic illustration of the sequence of fabrication steps used to form the double-sided microfilter assembly for use on a DCF fiber tip (figure not to scale). (<b>a</b>) A commercially available LPF was used as the starting point (see text for details). (<b>b</b>) The glass substrate was ground down and polished to reduce the thickness of the substrate to approximately 0.7 mm. (<b>c</b>) The SPF was deposited onto the opposing surface to the long-pass coating. (<b>d</b>) A ring of SPF was removed through femtosecond laser drilling, after which (<b>e</b>) the hole in the LPF was drilled as described in the text. (<b>f</b>) Finally, a further glass spacer was bonded to the LPF surface to provide a substrate for the SERS sensing surface. (<b>g</b>) Perspective view of the filter patterns. (<b>h</b>) Scanning electron microscope image of SERS-active, photochemically deposited silver nanoparticles on the surface of the outer glass substrate.</p>
Full article ">Figure 3
<p>Tool paths programmed for ablating (<b>a</b>) the short-pass coating and (<b>b</b>) the long-pass coating. For the SERS testing presented below, <span class="html-italic">R</span><sub>1</sub> = 5 µm and <span class="html-italic">R</span><sub>2</sub> = 55 µm were used. The spacing and number of paths in each case were determined by the laser spot size (4.5 μm), the track overlap (1.5 μm), and the depth to be ablated.</p>
Full article ">Figure 4
<p>Translation stages and UV curing system used for aligning and attaching the microfilter assembly to the DCF tip.</p>
Full article ">Figure 5
<p>The double-sided filter combines the transmission characteristics of both the long- and short-pass filters. The SPF (black line) passes the laser line (shown in green) while blocking the silica Raman-scattered signal in the Raman spectral range. To enter the inner cladding of the DCF, Raman-scattered light from the sample passes through the LPF (red line) and through the ablated region of the short-pass coating, while Rayleigh scattering from the sample is blocked.</p>
Full article ">Figure 6
<p>(<b>a</b>) Optical profilometer measurement of a typical short-pass island (<span class="html-italic">R</span><sub>1</sub> = 8 µm) and ablated ring after cleaning. (<b>b</b>) Magnified view of the short-pass island region from (<b>a</b>). (<b>c</b>) Microscopic image of another example with <span class="html-italic">R</span><sub>1</sub> = 5 µm, taken under white light epi-illumination (20× objective). Wavelengths above 520 nm are transmitted by the LPF on the far side of the plate, while the shorter, mainly blue wavelengths are reflected, resulting in the observed blue color of the ablated region. (<b>d</b>) SEM image of the short-pass island from (<b>c</b>), with the edges of the island showing some evidence of the discrete layers deposited to form the SPF. The ablated region is accurate to the design dimensions, and the boundaries between the ablated region and the remaining SPF are relatively narrow. While the circumferential tool path from <a href="#nanomaterials-14-01345-f003" class="html-fig">Figure 3</a>a can be discerned here in (<b>c</b>), and individual ablation sites can be seen on the glass surface in (<b>d</b>), there is no sign of any significant residual filter coating material on the ablated surface.</p>
Full article ">Figure 7
<p>(<b>a</b>) Spectrum acquired through a 25 cm DCF segment with integrated microfilter assembly. (<b>b</b>) The characteristic SERS peaks of thiophenol are clearly visible after subtracting the fiber Raman background, which is generated primarily by the transmitted laser excitation in this simplified setup. The thiophenol spectrum could not be detected in any of the DCF probes without filtering assembly. (<b>c</b>) As expected, the intensity of the fiber Raman background scales approximately proportionally with the probe length, whereas the SERS peak intensity is reasonably constant with relatively minor losses for longer probe lengths. Peak intensities have been normalized against the 12 cm DCF probe in each case.</p>
Full article ">
14 pages, 1163 KiB  
Article
Application of Low-Pressure Nanofiltration Membranes NF90 and NTR-729HF for Treating Diverse Wastewater Streams for Irrigation Use
by Charith Fonseka, Seongchul Ryu, Sukanyah Devaisy, Jaya Kandasamy, Lee McLod, Harsha Ratnaweera and Saravanamuthu Vigneswaran
Water 2024, 16(14), 1971; https://doi.org/10.3390/w16141971 - 11 Jul 2024
Viewed by 592
Abstract
The application of low-pressure nanofiltration (NF) was investigated for three different applications: water reuse from acid mine drainage (AMD), surface water containing natural organic matter (NOM) and agricultural reuse of microfiltered biologically treated sewage effluent (MF-BTSE). AMD contains many valuable rare earth elements [...] Read more.
The application of low-pressure nanofiltration (NF) was investigated for three different applications: water reuse from acid mine drainage (AMD), surface water containing natural organic matter (NOM) and agricultural reuse of microfiltered biologically treated sewage effluent (MF-BTSE). AMD contains many valuable rare earth elements (REEs) and copper (Cu) that can be recovered with fresh water. The NF90 membrane was investigated for recovery of fresh water from synthetic AMD. A steady permeate flux of 15.5 ± 0.2 L/m2h was achieved for pretreated AMD with over 98% solute rejection. NF90 achieved a high dissolved organic carbon (DOC) rejection of 95% from surface water containing NOM where 80% of the organic fraction was hydrophilic, mainly humics. The NF process maintained a high permeate flux of 52 LMH at 4 bars. The MF-BTSE was treated by NTR-729HF for agricultural reuse. NTR-729HF membranes were capable of rejecting DOC and inorganics such as sulfates and divalent ions (SO42−, Ca2+ and Mg2+) from MF-BTSE, with less than 20% rejection of monovalent (Na+ and Cl) ions. The sodium adsorption ratio (SAR) was significantly reduced from 39 to 14 after treatment through NTR-729HF at 4 bar. The resulting water was found to be suitable to irrigate salt-sensitive crops. Full article
Show Figures

Figure 1

Figure 1
<p>Schematic diagram of NF setup.</p>
Full article ">Figure 2
<p>Permeate flux of NF90 in treating synthetic AMD solution (steady-state flux 15.5 L/m<sup>2</sup>h; pressure = 3 bar).</p>
Full article ">Figure 3
<p>Schematic diagram of trajectory of NF membranes for water reuse applications and their future implications.</p>
Full article ">
13 pages, 1746 KiB  
Article
Pectinase Production from Cocoa Pod Husk in Submerged Fermentation and Its Application in the Clarification of Apple Juice
by Anderson Steyner Rozendo, Luciana Porto de Souza Vandenberghe, Patricia Beatriz Gruening de Mattos, Hervé Louis Ghislain Rogez and Carlos Ricardo Soccol
Fermentation 2024, 10(7), 337; https://doi.org/10.3390/fermentation10070337 - 28 Jun 2024
Viewed by 754
Abstract
The present work aimed to use cocoa pod husk (CPH) and its extracted pectin as a potential substrate for the production of pectinase and to test the enzyme produced in the clarification process of apple juice. CPH with a particle size of <0.84 [...] Read more.
The present work aimed to use cocoa pod husk (CPH) and its extracted pectin as a potential substrate for the production of pectinase and to test the enzyme produced in the clarification process of apple juice. CPH with a particle size of <0.84 mm was employed for pectinase production by a selected strain of Aspergillus niger NRRL 2270. The optimization of the physicochemical conditions of the production medium led to an enzymatic activity of 602.03 U/g dry CPH, which was obtained under the following conditions: 110.25 g/L of CPH, 5% w/v pectin extract, 0.05 g/L of yeast extract, incubation at 28 °C, and pH 4, representing a 176% increase in enzymatic activity under the evaluated conditions. The production kinetics of pectinase showed maximum enzymatic activity at 96 h. Subsequently, the enzymatic extract was precipitated, microfiltered, and ultrafiltrated, resulting in 4852.50 U/mg of specific activity. The enzymatic activity after recovery and purification processes corresponded to 819 U/g dry CPH. Finally, a clarification stage of apple juice was carried out, in which the produced pectinase (CauPec) showed turbidity of 448.89 NTU compared to 417.89 NTU for the commercial enzyme and a viscosity of 1.86 cP, CauPec, and 1.19 cP, commercial pectinase, as well as soluble solids of 8.0 for commercial pectinase and 8.73 for CauPec. Therefore, it can be concluded that CPH and its pectin extract were excellent substrates for the production of pectinases, whose formulation is highly stable and can be applied in the clarification of apple juice. Full article
(This article belongs to the Special Issue Fermentation: 10th Anniversary)
Show Figures

Figure 1

Figure 1
<p>Pareto chart—Step 2 optimization—the effect of CPH and pectin extract concentrations on pectinase activity (U/g dry CPH).</p>
Full article ">Figure 2
<p>Response surface—CCRD—Step 2 optimization—Influence of CPH and pectin extract on pectinase activity (U/g dry CPH).</p>
Full article ">Figure 3
<p>Kinetics of pectinase production using CPH and pectin extract.</p>
Full article ">Figure 4
<p>Steps of the apple juice enzymatic clarification process.</p>
Full article ">
14 pages, 1782 KiB  
Article
Long-Term Effects of Microfiltered Seawater and Resistance Training with Elastic Bands on Hepatic Parameters, Inflammation, Oxidative Stress, and Blood Pressure of Older Women: A 32-Week, Double-Blinded, Randomized, Placebo-Controlled Trial
by Carlos Babiloni-Lopez, Pedro Gargallo, Alvaro Juesas, Javier Gene-Morales, Angel Saez-Berlanga, Pablo Jiménez-Martínez, Jose Casaña, Josep C. Benitez-Martinez, Guillermo T. Sáez, Julio Fernández-Garrido, Carlos Alix-Fages and Juan C. Colado
Healthcare 2024, 12(2), 204; https://doi.org/10.3390/healthcare12020204 - 15 Jan 2024
Viewed by 1582
Abstract
The bulk of research on microfiltered seawater (SW) is based on its short-term effects. However, the long-term physiological adaptations to combining SW and resistance training (RT) are unknown. This study aimed to analyse the impact of an RT program using elastic bands combined [...] Read more.
The bulk of research on microfiltered seawater (SW) is based on its short-term effects. However, the long-term physiological adaptations to combining SW and resistance training (RT) are unknown. This study aimed to analyse the impact of an RT program using elastic bands combined with SW intake on hepatic biomarkers, inflammation, oxidative stress, and blood pressure in post-menopausal women. Ninety-three women voluntarily participated (age: 70 ± 6.26 years; body mass index: 22.05 ± 3.20 kg/m2; Up-and-Go Test: 6.66 ± 1.01 s). RT consisted of six exercises (32 weeks, 2 days/week). Nonsignificant differences were reported for hepatic biomarkers except for a reduction in glutamic-pyruvic transaminase (GPT) in both RT groups (RT + SW: p = 0.003, ES = 0.51; RT + Placebo: p = 0.012, ES = 0.36). Concerning oxidative stress, vitamin D increased significantly in RT + SW (p = 0.008, ES = 0.25). Regarding inflammation, interleukin 6 significantly decreased (p = 0.003, ES = 0.69) in RT + SW. Finally, systolic blood pressure significantly decreased in both RT groups (RT + placebo: p < 0.001, ES = 0.79; RT + SW: p < 0.001, ES = 0.71) as did diastolic blood pressure in both SW groups (RT + SW: p = 0.002, ES = 0.51; CON + SW: p = 0.028, ES = 0.50). Therefore, RT + SW or SW alone are safe strategies in the long term with no influences on hepatic and oxidative stress biomarkers. Additionally, SW in combination with RT positively influences vitamin D levels, inflammation, and blood pressure in older women. Full article
(This article belongs to the Special Issue Physical Fitness—Effects on Muscle Function and Sports Performance)
Show Figures

Figure 1

Figure 1
<p>Flow of participants throughout the study. RT: resistance training; PLA: placebo; SW: seawater supplement; CON: control group. Participants are presented according to previous studies of this same project [<a href="#B25-healthcare-12-00204" class="html-bibr">25</a>].</p>
Full article ">Figure 2
<p>Individual responses of participants from each of the study groups in terms of interleukin 6. Colored shorter lines indicate the change from pre- to post-intervention of each participant. The longer line (which presents error bars on its extremes) indicates the mean change of the group. The red lines indicate the mean pre-intervention value of the group (this value is standardized to zero on the green column of the right-hand side of each plot). The blue lines indicate the mean post-intervention value of the group, which is connected to a red point that indicates the mean change from pre- and post-intervention of each group. Blue points on the right-hand side represent the difference obtained by each participant. RT: resistance training; PLA: placebo; SW: seawater supplement; CON: control group.</p>
Full article ">Figure 3
<p>Individual responses of participants from each of the study groups in terms of systolic blood pressure. Colored shorter lines indicate the change from pre- to post-intervention of each participant. The longer line (which presents error bars on its extremes) indicates the mean change of the group. The red lines indicate the mean pre-intervention value of the group (this value is standardized to zero on the green column of the right-hand side of each plot). The blue lines indicate the mean post-intervention value of the group, which is connected to a red point that indicates the mean change from pre- and post-intervention of each group. Blue points on the right-hand side represent the difference obtained by each participant. RT: resistance training; PLA: placebo; SW: seawater supplement; CON: control group.</p>
Full article ">
16 pages, 2328 KiB  
Article
Multivariate Analysis of the Influence of Microfiltration and Pasteurisation on the Quality of Beer during Its Shelf Life
by Ana Carolina de Lima, Luciana R. Brandao, Bruno G. Botelho, Carlos A. Rosa, Laura Aceña, Montserrat Mestres and Ricard Boqué
Foods 2024, 13(1), 122; https://doi.org/10.3390/foods13010122 - 29 Dec 2023
Cited by 1 | Viewed by 1127
Abstract
Gas chromatography–mass spectrometry (GC–MS), physicochemical and microbiological analyses, sensory descriptive evaluation, and multivariate analyses were applied to evaluate the efficiencies of microfiltration and pasteurization processes during the shelf life of beer. Samples of microfiltered and pasteurised beer were divided into fresh and aged [...] Read more.
Gas chromatography–mass spectrometry (GC–MS), physicochemical and microbiological analyses, sensory descriptive evaluation, and multivariate analyses were applied to evaluate the efficiencies of microfiltration and pasteurization processes during the shelf life of beer. Samples of microfiltered and pasteurised beer were divided into fresh and aged groups. A forced ageing process, which consisted of storing fresh samples at 55° C for 6 days in an incubator and then keeping them under ambient conditions prior to analysis, was applied. Physicochemical analysis showed that both microfiltered and pasteurised samples had a slight variation in apparent extract, pH, and bitterness. The samples that underwent heat treatment had lower colour values compared with those that were microfiltered. Chromatographic peak areas of vicinal diketones increased in both fresh and aged samples. The results of the microbiological analysis revealed spoilage lactic acid bacteria (Lactobacillus) and yeasts (Saccharomyces and non-Saccharomyces) in fresh microfiltered samples. In the GC–MS analysis, furfural, considered by many authors as a heat indicator, was detected only in samples that underwent forced ageing and not in samples that were subjected to thermal pasteurisation. Finally, sensory analysis found differences in the organoleptic properties of fresh microfiltered samples compared with the rest of the samples. Full article
(This article belongs to the Section Drinks and Liquid Nutrition)
Show Figures

Figure 1

Figure 1
<p>FM: Fresh Microfiltered; AM: Aged Microfiltered; FP: Fresh Pasteurised; AP: Aged Pasteurised.</p>
Full article ">Figure 2
<p>Overall impression of sensory analysis. Visual description, mouth sensation and taste description (<b>A</b>); aroma and flavour description (<b>B</b>). FM, fresh microfiltered; FP, fresh pasteurised; AM, aged microfiltered; AP, aged pasteurised; MS, mouthfeel sensations.</p>
Full article ">Figure 3
<p>(<b>A</b>) Loading PCA plot of the chromatographic data and physicochemical results for both microfiltered and pasteurised samples; (<b>B</b>) PCA biplot of the chromatographic data and physicochemical results of samples and physicochemical results: Apparent extract, pH, Alcohol, Colour, IBU, VDK. FM: Fresh Microfiltered; AM: Aged Microfiltered; FP: Fresh Pasteurised; AP: Aged Pasteurised.</p>
Full article ">Figure 4
<p>Threshold /ROC plots for the classification model with three classes: Class 1: FM; Class 2: (AM); and Class 3 (FP + AP).</p>
Full article ">Figure 5
<p>Score plot (<b>A</b>) and loading plot (<b>B</b>) of the PLS-DA classification model with three classes: Class 1: FM; Class 2: (AM); and Class 3 (FP + AP).</p>
Full article ">
10 pages, 269 KiB  
Article
Influence of Somatic Cell Removal on Milk Quality and Yield
by Ruthele Moraes do Carmo, Luiz Eduardo Costa do Nascimento, Paulo Victor Toledo Leão, Guilherme Henrique de Paula, Mariana Borges de Castro Dias, Patrick Bezerra Fernandes, Abner Alves Mesquita, Edmar Soares Nicolau, Melina Maria Rodrigues Rezende, Weilla Araujo de Sousa, Esther Cristina Neves Medeiros da Silva and Marco Antônio Pereira da Silva
Beverages 2024, 10(1), 5; https://doi.org/10.3390/beverages10010005 - 27 Dec 2023
Viewed by 1904
Abstract
This investigation aimed to assess how the somatic cell count (SCC) impacts milk production and the physicochemical quality of milk, including the effects of centrifugation and microfiltration on SCCs and the yield of fresh cheese. Milk production was analysed at different somatic cell [...] Read more.
This investigation aimed to assess how the somatic cell count (SCC) impacts milk production and the physicochemical quality of milk, including the effects of centrifugation and microfiltration on SCCs and the yield of fresh cheese. Milk production was analysed at different somatic cell counts (SCCs) to observe how centrifugation and microfiltration affected the removal of SCs from the milk and the yield of fresh cheese. Tukey’s test was employed at a 5% significance level to compare the chemical composition of the milk, milk production, and fresh cheese yield when using microfiltered and/or centrifuged milk. Milk with an SCC of ≤200,000 somatic cells (SCs) per mL exhibited higher yields. Although centrifugation and microfiltration influenced milk fat content, total dry extract and SCC, they did not impact fresh cheese yield. It is important to note that these processes reduced the fat content and SCC, making skim milk a potential option for future research studies. Full article
(This article belongs to the Section Beverage Technology Fermentation and Microbiology)
21 pages, 3198 KiB  
Article
Solid–Liquid Separation and Its Environmental Impact on Manure Treatment in Scaled Pig Farms—Evidence Based on Life Cycle Assessment
by Yijia Zhang, Qinqing Bo, Xintian Ma, Yating Du, Xinyi Du, Liyang Xu and Yadong Yang
Agriculture 2023, 13(12), 2284; https://doi.org/10.3390/agriculture13122284 - 16 Dec 2023
Viewed by 2204
Abstract
Recently, there has been a significant focus on the issue of pollution caused by livestock and poultry rearing, which is recognized as a prominent contributor to nonpoint source pollution in the agricultural sector. This study employed the life cycle assessment (LCA) methodology to [...] Read more.
Recently, there has been a significant focus on the issue of pollution caused by livestock and poultry rearing, which is recognized as a prominent contributor to nonpoint source pollution in the agricultural sector. This study employed the life cycle assessment (LCA) methodology to evaluate the environmental impact of several pig manure processing scenarios with the aim of determining the appropriate solid–liquid separation tool for large-scale pig farms. The findings indicate that the utilization of a screw extruder for solid–liquid separation in Scenario 2 has a lower environmental impact. In contrast to Scenario 1, Scenario 2 exhibits reduced environmental potential in the areas of global warming, human toxicity, acidification, and eutrophication. Specifically, the global warming, human toxicity, acidification, and eutrophication impacts decreased by 56%, 81%, 83%, and 273%, respectively, due to the implementation of solid–liquid separation. The type of solid–liquid separation equipment used during the processing of swine manure, as well as the subsequent treatment, have a significant impact on environmental emissions. Compared to Scenario 2, Scenario 3, which utilizes a centrifugal microfilter for solid–liquid separation, exhibits a lower environmental impact in terms of human toxicity, resulting in a reduction of 0.736 kg DCB-eq. In general, solid–liquid separation is a viable and environmentally friendly method for the disposal of waste from large-scale pig farms. The adoption of this method is highly recommended. During its implementation, careful consideration should be given to factors such as separation efficiency and pollution emissions. It is crucial to select appropriate equipment for solid–liquid separation to effectively process the waste. Full article
(This article belongs to the Section Agricultural Technology)
Show Figures

Figure 1

Figure 1
<p>System boundaries for Scenario 1.</p>
Full article ">Figure 2
<p>System boundaries for Scenario 2.</p>
Full article ">Figure 3
<p>UASB—AO process handling process.</p>
Full article ">Figure 4
<p>System boundaries for Scenario 3.</p>
Full article ">Figure 5
<p>Life cycle assessment results of the (<b>a</b>) global warming potential in 3 scenarios, (<b>b</b>) eutrophication potential in 3 scenarios, (<b>c</b>) acidification potential in 3 scenarios, (<b>d</b>) abiotic depletion in 3 scenarios, and (<b>e</b>) human toxicity potential in 3 scenarios.</p>
Full article ">
17 pages, 2199 KiB  
Article
Effects of Different TiO2/CNT Coatings of PVDF Membranes on the Filtration of Oil-Contaminated Wastewaters
by Ákos Ferenc Fazekas, Tamás Gyulavári, Zsolt Pap, Attila Bodor, Krisztián Laczi, Katalin Perei, Erzsébet Illés, Zsuzsanna László and Gábor Veréb
Membranes 2023, 13(10), 812; https://doi.org/10.3390/membranes13100812 - 27 Sep 2023
Cited by 2 | Viewed by 1535
Abstract
Six different TiO2/CNT nanocomposite-coated polyvinylidene-fluoride (PVDF) microfilter membranes (including –OH or/and –COOH functionalized CNTs) were evaluated in terms of their performance in filtering oil-in-water emulsions. In the early stages of filtration, until reaching a volume reduction ratio (VRR) of ~1.5, the [...] Read more.
Six different TiO2/CNT nanocomposite-coated polyvinylidene-fluoride (PVDF) microfilter membranes (including –OH or/and –COOH functionalized CNTs) were evaluated in terms of their performance in filtering oil-in-water emulsions. In the early stages of filtration, until reaching a volume reduction ratio (VRR) of ~1.5, the membranes coated with functionalized CNT-containing composites provided significantly higher fluxes than the non-functionalized ones, proving the beneficial effect of the surface modifications of the CNTs. Additionally, until the end of the filtration experiments (VRR = 5), notable flux enhancements were achieved with both TiO2 (~50%) and TiO2/CNT-coated membranes (up to ~300%), compared to the uncoated membrane. The irreversible filtration resistances of the membranes indicated that both the hydrophilicity and surface charge (zeta potential) played a crucial role in membrane fouling. However, a sharp and significant flux decrease (~90% flux reduction ratio) was observed for all membranes until reaching a VRR of 1.1–1.8, which could be attributed to the chemical composition of the oil. Gas chromatography measurements revealed a lack of hydrocarbon derivatives with polar molecular fractions (which can act as natural emulsifiers), resulting in significant coalescent ability (and less stable emulsion). Therefore, this led to a more compact cake layer formation on the surface of the membranes (compared to a previous study). It was also demonstrated that all membranes had excellent purification efficiency (97–99.8%) regarding the turbidity, but the effectiveness of the chemical oxygen demand reduction was slightly lower, ranging from 93.7% to 98%. Full article
(This article belongs to the Section Membrane Applications)
Show Figures

Figure 1

Figure 1
<p>IR spectra of the CNT<sub>a</sub> sample and its corresponding functionalized derivatives.</p>
Full article ">Figure 2
<p>IR spectra of the CNT<sub>b</sub> sample and the oxidation products obtained after acidic treatment.</p>
Full article ">Figure 3
<p>Flux values measured during the filtration of the oil emulsions (as a function of volume reduction ratio).</p>
Full article ">Figure 4
<p>Chromatograms of crude oils: sample 1 (<b>a</b>) and sample 2 (<b>b</b>).</p>
Full article ">Figure 5
<p>Filtration resistance values of the different membranes.</p>
Full article ">Figure 6
<p>Purification efficiencies of the membranes (calculated from the turbidity and chemical oxygen demand values).</p>
Full article ">
15 pages, 3124 KiB  
Article
The Performance of Ultrafiltration Process to Further Refine Lactic Acid from the Pre-Microfiltered Broth of Kitchen Waste Fermentation
by Yan Guo, Chenglong Li, Hongjun Zhao, Xiaona Wang, Ming Gao, Xiaohong Sun and Qunhui Wang
Membranes 2023, 13(3), 330; https://doi.org/10.3390/membranes13030330 - 13 Mar 2023
Cited by 1 | Viewed by 1512
Abstract
Lactic acid (LA) is an important chemical material facing rapid demand in recent years. The oriented fermentation of kitchen waste is a promising route for economic LA production. However, the refinement of LA from fermentation broth is a spiny issue. In this study, [...] Read more.
Lactic acid (LA) is an important chemical material facing rapid demand in recent years. The oriented fermentation of kitchen waste is a promising route for economic LA production. However, the refinement of LA from fermentation broth is a spiny issue. In this study, the performance of ultrafiltration (UF) process for the refinement of LA from the pre-microfiltered broth of kitchen waste fermentation was first investigated. The results showed that with 50 KDa polyethersulfone membrane, under the optimum pressure of 120 KPa, the pH of 6.0, and the backflushing mode with the deionized water for 3 min, the best performance was achieved with the chroma removal efficiency, turbidity removal efficiency, protein removal efficiency and total sugar removal efficiency of 54.3%, 89.8%, 71.7% and 58.5%, respectively, and LA recovery efficiency was 93.6%. The results indicated that the UF process could further effectively refine the pre-microfiltered broth of kitchen waste fermentation, and the combination of microfiltration and UF process is ideal for achieving desirable LA refinement performance. This study verified the feasibility of UF process in LA refinement from pre-microfiltered broth of kitchen waste fermentation, and based on the results, the further exploration of proper post-process to treat UF filtrate for obtaining LA product with higher quality should be explored in the future. Full article
(This article belongs to the Special Issue Separation Techniques and Circular Economy)
Show Figures

Figure 1

Figure 1
<p>The illustration of the filtration configuration.</p>
Full article ">Figure 2
<p>The selection of ultrafiltration membrane type: (<b>a</b>) the pure water flux of four kinds of ultrafiltration membrane under different operating pressure; (<b>b</b>) the filtration performance of four kinds of ultrafiltration membrane for protein, total sugar and lactic acid in simulated broth.</p>
Full article ">Figure 3
<p>The effect of different pressure on filtration performance: (<b>a</b>) the flux change; (<b>b</b>) the chroma removal; (<b>c</b>) the turbidity removal; (<b>d</b>) the protein removal efficiency, the total sugar removal efficiency, and the lactic acid recovery efficiency.</p>
Full article ">Figure 4
<p>The effect of different pH on filtration performance: (<b>a</b>) the flux change; (<b>b</b>) the chroma removal; (<b>c</b>) the turbidity removal; (<b>d</b>) the protein removal efficiency, the total sugar removal efficiency and the lactic acid recovery efficiency.</p>
Full article ">Figure 5
<p>The effect of different flushing operations on flux recovery efficiency of microfiltration: (<b>a</b>) the flushing methods; (<b>b</b>) the flushing agents; (<b>c</b>) the effect of washing time on flushing efficiency.</p>
Full article ">Figure 6
<p>The surface observation of the microfiltration membrane by SEM instrument: (<b>a</b>) the new membrane; (<b>b</b>) after the blocking; (<b>c</b>) after the flushing with 1% NaClO.</p>
Full article ">Figure 7
<p>The effect of different flushing cycles on filtration performance: (<b>a</b>) the flux change; (<b>b</b>) the pure water flux; (<b>c</b>) the turbidity removal; (<b>d</b>) the chroma removal; (<b>e</b>) the protein removal efficiency and the total sugar removal efficiency.</p>
Full article ">Figure 8
<p>The whole removal performance of the microfiltration membrane separation (<b>a</b>) and the removal percentage of each component (<b>b</b>).</p>
Full article ">
15 pages, 647 KiB  
Article
Effects of Microfiltered Seawater Intake and Variable Resistance Training on Strength, Bone Health, Body Composition, and Quality of Life in Older Women: A 32-Week Randomized, Double-Blinded, Placebo-Controlled Trial
by Alvaro Juesas, Pedro Gargallo, Javier Gene-Morales, Carlos Babiloni-López, Angel Saez-Berlanga, Pablo Jiménez-Martínez, Jose Casaña, Josep C. Benitez-Martinez, Rodrigo Ramirez-Campillo, Ivan Chulvi-Medrano and Juan C. Colado
Int. J. Environ. Res. Public Health 2023, 20(6), 4700; https://doi.org/10.3390/ijerph20064700 - 7 Mar 2023
Cited by 1 | Viewed by 2272
Abstract
The aim was to explore the effects of a 32-week resistance training (RT) intervention with elastic bands with or without microfiltered seawater (SW) supplementation on isokinetic strength, bone mineral density (BMD), body composition, and subjective quality of life in postmenopausal women. Ninety-three untrained [...] Read more.
The aim was to explore the effects of a 32-week resistance training (RT) intervention with elastic bands with or without microfiltered seawater (SW) supplementation on isokinetic strength, bone mineral density (BMD), body composition, and subjective quality of life in postmenopausal women. Ninety-three untrained women (age: 70.00 ± 6.26 years; body mass index: 22.05 ± 3.20 kg/m2; body fat: 37.77 ± 6.38%; 6.66 ± 1.01 s up-and-go test) voluntarily participated in this randomized, double-blinded, controlled trial. Participants were allocated into four groups (RT+SW, RT+PLA, CON+SW, and CON+PLA). The RT intervention (twice weekly) consisted of different exercises for the whole body performed at submaximal intensities with elastic bands. Both control groups were not involved in any exercise program. A two-way mixed analysis of variance of repeated measures revealed significant improvements in almost all the variables in both intervention groups (p < 0.05). However, significant differences with controls were encountered in isokinetic strength, body fat percentage, and bodily pain. Although the group with SW supplementation obtained greater effect sizes, non-significant differences between both RT groups were observed. In conclusion, the determinant factor of the adaptations seems to be RT rather than SW. Full article
(This article belongs to the Section Exercise and Health-Related Quality of Life)
Show Figures

Figure 1

Figure 1
<p>Flowchart of participation. RT: resistance training; PLA: placebo; SW: microfiltered seawater; CON: control group.</p>
Full article ">
13 pages, 6891 KiB  
Article
Field Evaluation of UF Filtration Pretreatment Impact on RO Membrane Scaling
by Yakubu A. Jarma, John Thompson, Bilal M. Khan and Yoram Cohen
Water 2023, 15(5), 847; https://doi.org/10.3390/w15050847 - 22 Feb 2023
Cited by 2 | Viewed by 2594
Abstract
Pretreatment of reverse osmosis (RO) feed water of high mineral scaling propensity was evaluated with respect to downstream RO membrane scaling, for two different feed pretreatment configurations. The pretreatment schemes included (i) media sand filtration, followed by a hydrocyclone (HC) and (ii) a [...] Read more.
Pretreatment of reverse osmosis (RO) feed water of high mineral scaling propensity was evaluated with respect to downstream RO membrane scaling, for two different feed pretreatment configurations. The pretreatment schemes included (i) media sand filtration, followed by a hydrocyclone (HC) and (ii) a hydrocyclone, microfilter, and a UF module, where both configurations included mesh screens for added protection. The first pretreatment configuration reduced the source water turbidity to ~0.5 NTU, while treatment that included UF feed yielded turbidity of <˜0.1 NTU; both pretreatment strategies provided feed water turbidity within the range recommended for RO desalination. Membrane scaling tests, with the pretreated water without antiscalant dosing, using a plate-and-frame RO unit and a membrane monitoring system, provided real-time membrane surface images that were quantified with respect to the progression of mineral scaling. RO desalting of source water pretreated with the first configuration revealed flux decline that was 75% greater and scale coverage (primarily gypsum) a factor of approximately eight higher relative to desalting of UF-treated source water. The results suggest that RO desalting of high mineral scaling propensity water can significantly benefit from added UF treatment to achieve feedwater turbidity to well below the typically recommended 0.5 NTU upper limit. Full article
(This article belongs to the Section Wastewater Treatment and Reuse)
Show Figures

Figure 1

Figure 1
<p>(<b>A</b>) Location of field-testing site in the San Joaquin Valley of California (adapted from [<a href="#B30-water-15-00847" class="html-bibr">30</a>]). (<b>B</b>) External view of the containerized RO plant. (<b>C</b>) Internal view of the RO plant. (<b>D</b>) Membrane monitoring system (MMS) inside the RO plant trailer.</p>
Full article ">Figure 2
<p>Schematic illustration of the sequence of two RO feed water pretreatment trains: (<b>A</b>) media filtration, followed by a hydrocyclone and 80-mesh strainer; and (<b>B</b>) hydrocyclone, followed by a 200 µm microfilter (MF), ultrafiltration (UF), and 80-mesh strainer.</p>
Full article ">Figure 3
<p>Schematic representation of the plate-and-frame RO (PFRO) membrane monitoring system (MMS). The applied pressure and crossflow in the PFRO unit were controlled via the variable frequency drive (VFD) of the feed pump and an automated control valve (V3). Online sensors included feed pressure (P), concentrate and permeate flow rate sensors (F), and conductivity sensors (C).</p>
Full article ">Figure 4
<p>Normalized RO permeate flux during filtration tests for feed water treatment with configurations A (without UF) and B (with UF pretreatment). Crossflow velocity = 4.5 cm/s, <span class="html-italic">Y<sub>plant</sub></span> = 63%, initial permeate flux = 33 L/m<sup>2</sup>h, and <span class="html-italic">SI<sub>g,m</sub></span> = 1.9–2.0. P and P<sub>O</sub> are permeate flux values at time t and initially. Dotted vertical lines 1 and 2 denote early detection of particles/small crystals formed for RO operation with feedwater pretreated via configurations A and B, respectively (<a href="#water-15-00847-f002" class="html-fig">Figure 2</a>).</p>
Full article ">Figure 5
<p>Real-time membrane monitoring system (MMS) surface images during desalination RO feed water treated via a filtration train without UF (configuration A). PFRO operating conditions: crossflow velocity = 4.5 cm/s, initial permeate flux = 33 L/m<sup>2</sup>-h (19 gallons/ft<sup>2</sup>-day), and <span class="html-italic">SI<sub>g,m</sub></span> = 1.9–2.0 corresponding to equivalent RO plant recovery of 63%.</p>
Full article ">Figure 6
<p>RO membrane surface images during desalination of RO feed water pretreated via a filtration train that included UF (configuration B, <a href="#water-15-00847-f002" class="html-fig">Figure 2</a>) without antiscalant dosing. PFRO operating conditions: crossflow velocity = 4.5 cm/s, initial permeate flux = 33 L/m<sup>2</sup>-h (19 gallons/ft<sup>2</sup>-day), and initial <span class="html-italic">SI<sub>g,m</sub></span> ~ 2 corresponding to equivalent RO plant recovery of 63%.</p>
Full article ">Figure 7
<p>Comparison of surface coverage and crystal number density analyzed from real-time membrane images during prefiltration testing indicating a comparison of observed mineral scaling configurations A and B. PFRO operating conditions: crossflow velocity = 4.5 cm/s, initial permeate flux = 33 L/m<sup>2</sup>-h (19 gallons/ft<sup>2</sup>-day), and <span class="html-italic">SI<sub>g,m</sub></span> = 1.9–2.0 corresponding to equivalent RO plant recovery of 63%. RO feed pretreatment with media filtration and hydrocyclone and without UF and with UF pretreatment identified as configurations A and B, respectively (<a href="#water-15-00847-f002" class="html-fig">Figure 2</a>).</p>
Full article ">Figure A1
<p>EDS spectra of MMS membrane fouled/scaled after 14 h of filtration with raw water treatment (<a href="#water-15-00847-f004" class="html-fig">Figure 4</a>) that includes UF (configuration B, <a href="#water-15-00847-f002" class="html-fig">Figure 2</a>). The presence of calcium and sulfur are consistent with the presence of calcium sulfate as also suggested by the gypsum (calcium sulfate dihydrate) rosette-type crystal structures. The presence of calcium and oxygen are consistent with the expected presence of calcite given the supersaturation of the raw feedwater with respect to calcite (<a href="#water-15-00847-t001" class="html-table">Table 1</a>). Note: Au peak is present since the membrane sample was coated with gold (Au) prior to EDS analysis.</p>
Full article ">Figure A2
<p>SEM images of mineral scale crystals formed on the RO membrane in the membrane monitoring system (MMS) during RO desalination of AD water showing different mineral crystal morphologies. Mineral crystals resembling “flattened” gypsum rosettes (<b>A</b>–<b>C</b>), and high mag. image of a “flattened” crystal rod or arm (<b>D</b>).</p>
Full article ">
16 pages, 2818 KiB  
Article
Application Effect of MF-OP on Collection of Trivalent Holmium from Rare Earth Mining Wastewater
by Liang Pei and Liying Sun
Int. J. Environ. Res. Public Health 2023, 20(2), 1498; https://doi.org/10.3390/ijerph20021498 - 13 Jan 2023
Viewed by 1103
Abstract
Microtube microfilter with organic phosphoric acid (expressed as MF-OP) containing a wastewater portion with buffer fluid and an enriched portion with nitric acid fluid and organic phosphoric extractant dissolved in benzin has been studied for its trivalent holmium (expressed as Ho(III) collection from [...] Read more.
Microtube microfilter with organic phosphoric acid (expressed as MF-OP) containing a wastewater portion with buffer fluid and an enriched portion with nitric acid fluid and organic phosphoric extractant dissolved in benzin has been studied for its trivalent holmium (expressed as Ho(III) collection from rare earth wastewater. Common parameters affecting the collection effect have been investigated, including hydrogen ion molar concentration (molar concentration can be expressed as Cm) or pH value, initial concentration (expressed as Co) of Ho(III), ion-force of rare earth wastewater, voluminal proportion of organic phosphoric extractant with benzin and nitric acid fluid (expressed as Vr), nitric acid Cm, extractant Cm, and type of acid fluid in an enriched portion. The virtues of MF-OP compared to the traditional collection was explored. The impacts of hydrodynamic characteristics (steadiness and current speed) and MF parameter factors (inradius of tube, tube–shell thickness, proportion of holes) on the collection performance of MF-OP for Ho(III) collection were also considered. The test results displayed that the greatest collection conditions of Ho(III) were attained as nitric acid Cm was 4.00 mol/L, extractant Cm was 0.220 mol/L, and Vr was 0.8 in the enriched portion, and pH value was 4.60 in the wastewater portion. Ion- force of rare earth wastewater had no noticeable outcome on Ho(III) collection. The collection proportion of Ho(III) was attainable to 93.1% in 280 min, while Co was 1.80 × 10−3 mol/L. Full article
(This article belongs to the Special Issue Water Quality and Purification)
Show Figures

Figure 1

Figure 1
<p>Installation of microtube microfilter reactor with organic phosphoric system procedure.</p>
Full article ">Figure 2
<p>Diagrammatic sketch and description of Ho <sup>3+</sup> collection MF-OP.</p>
Full article ">Figure 3
<p>The constancy comparison of MF-OP and traditional SFF.</p>
Full article ">Figure 4
<p>The comparison between MF-OP and traditional SLM for current speeds influence on collection of Ho(III) in both portions (I).</p>
Full article ">Figure 5
<p>The comparison between MF-OP and traditional SLM for current speeds influence on collection of Ho(III) in both portions (II).</p>
Full article ">Figure 6
<p>Influence of wastewater pH.</p>
Full article ">Figure 7
<p>Influence of different acid fluids as resolving reagents.</p>
Full article ">Figure 8
<p>Influence of nitric acid <span class="html-italic">Cm</span> on collection of Ho(III).</p>
Full article ">Figure 9
<p>Influence of <span class="html-italic">Vr</span>.</p>
Full article ">Figure 10
<p>Influence of organic phosphoric <span class="html-italic">Cm</span>.</p>
Full article ">Figure 11
<p>Influence of ion-force on collection of Ho(III) (III).</p>
Full article ">Figure 12
<p>Retention in microtubes and resolving influences.</p>
Full article ">Figure 13
<p>Influence of tube–shell thickness.</p>
Full article ">Figure 14
<p>Influence of tube holes’ proportion.</p>
Full article ">Figure 15
<p>Influence of tube inradius.</p>
Full article ">
18 pages, 1017 KiB  
Article
Olive Mill Wastewater Fermented with Microbial Pools as a New Potential Functional Beverage
by Paola Foti, Paride S. Occhipinti, Nunziatina Russo, Antonio Scilimati, Morena Miciaccia, Cinzia Caggia, Maria Grazia Perrone, Cinzia L. Randazzo and Flora V. Romeo
Molecules 2023, 28(2), 646; https://doi.org/10.3390/molecules28020646 - 8 Jan 2023
Cited by 3 | Viewed by 2213
Abstract
Olive mill wastewater (OMWW) represents a by–product but also a source of biologically active compounds, and their recycling is a relevant strategy to recover income and to reduce environmental impact. The objective of the present study was to obtain a new functional beverage [...] Read more.
Olive mill wastewater (OMWW) represents a by–product but also a source of biologically active compounds, and their recycling is a relevant strategy to recover income and to reduce environmental impact. The objective of the present study was to obtain a new functional beverage with a health–promoting effect starting from OMWW. Fresh OMWW were pre–treated through filtration and/or microfiltration and subjected to fermentation using strains belonging to Lactiplantibacillus plantarum, Candida boidinii and Wickerhamomyces anomalus. During fermentation, phenolic content and hydroxytyrosol were monitored. Moreover, the biological assay of microfiltered fermented OMWW was detected versus tumor cell lines and as anti-inflammatory activity. The results showed that in microfiltered OMWW, fermentation was successfully conducted, with the lowest pH values reached after 21 days. In addition, in all fermented samples, an increase in phenol and organic acid contents was detected. Particularly, in samples fermented with L. plantarum and C. boidinii in single and combined cultures, the concentration of hydroxytyrosol reached values of 925.6, 902.5 and 903.5 mg/L, respectively. Moreover, biological assays highlighted that fermentation determines an increase in the antioxidant and anti–inflammatory activity of OMWW. Lastly, an increment in the active permeability on Caco-2 cell line was also revealed. In conclusion, results of the present study confirmed that the process applied here represents an effective strategy to achieve a new functional beverage. Full article
(This article belongs to the Special Issue Food Bioactive Compounds: Chemical Challenges and Opportunities)
Show Figures

Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>Microbial counts detected in MRS and SAB during fermentation in microfiltered OMWW differently inoculated. Data are expressed as means of Log CFU/mL ± standard deviations.</p>
Full article ">Figure 2
<p>Concentration of HT and TYR during fermentation in microfiltered OMWW differently inoculated. Different letters indicate statistical differences within the columns for the same compound (significance at <span class="html-italic">p</span> ≤ 0.01).</p>
Full article ">Figure 3
<p>Evaluation of antioxidant activity expressed as % RSA. Each graph corresponds to a volume (µL) used for each sample: (<b>A</b>) 50 µL of samples; (<b>B</b>) 37.50 µL of samples; (<b>C</b>) 25 µL of samples; (<b>D</b>) 12.5 µL of samples.</p>
Full article ">Figure 4
<p>Fermentation process and OMWW obtained Trials.</p>
Full article ">
11 pages, 2148 KiB  
Article
Adipose Autologous Micrograft and Its Derived Mesenchymal Stem Cells in a Bio Cross-Linked Hyaluronic Acid Scaffold for Correction Deep Wrinkles, Facial Depressions, Scars, Face Dermis and Its Regenerations: A Pilot Study and Cases Report
by Lorenzo Svolacchia, Claudia Prisco, Federica Giuzio and Fabiano Svolacchia
Medicina 2022, 58(11), 1692; https://doi.org/10.3390/medicina58111692 - 21 Nov 2022
Cited by 3 | Viewed by 1903
Abstract
The aim of this clinical study was to demonstrate that through a micrograft of viable adipose tissue cells microfiltered at 50 microns to exclude fibrous shoots and cell debris in a suspension of cross-linked hyaluronic acid, we were able to improve visible imperfections [...] Read more.
The aim of this clinical study was to demonstrate that through a micrograft of viable adipose tissue cells microfiltered at 50 microns to exclude fibrous shoots and cell debris in a suspension of cross-linked hyaluronic acid, we were able to improve visible imperfections of the dermis and to improve clinically observable wrinkles, with a beneficial effect also in the extracellular matrix (ECM). Background and Objectives: With the passage of time, the aging process begins, resulting in a progressive impairment of tissue homeostasis. The main reason for the formation of wrinkles is the involution of the papillary dermis, as well as the loss of stem cell niches with compromise of the extra-cytoplasmic matrix (ECM), and the loss of hyaluronic acid, which helps to maintain the shape and resistance and that is contained in the connective tissue. Materials and Methods: This study involved 14 female patients who underwent dermal wrinkle correction and bio-regeneration over the entire facial area through a suspension containing 1.0 mL of viable micrografts from adipose tissue in a 1.0 mL cross-linked hyaluronic acid. To verify the improvement of the anatomical area concerned over time, the various degrees of correction obtained for wrinkles, and in general for texture, were objectively evaluated by using a Numeric Rating scale (NRS) 10–0, a modified Vancouver scale and a Berardesca scale. Results: The Berardesca, NRS and Modified Vancouver scales showed that with this technique it was possible to obtain excellent results both when the suspension was injected into wrinkles with the linear retrograde technique, and when it was injected with the micropomphs technique to correct furrows, with the intent to revitalize the tissue through progenitors with adult stemness markers. Conclusions: The combination of microfragmented and microfiltered adipose tissue and cross-linked hyaluronic acid at 50 microns is safe new method to treat soft tissue defects such as deep wrinkles. Full article
Show Figures

Figure 1

Figure 1
<p>Procedure to mix microfragmented fat with hyaluronic acid. (<b>A</b>) Hyaluronic acid prefilled syringe; (<b>B</b>) Filtration of the collected and fragmented fat tissue; (<b>C</b>,<b>D</b>) mixing of the fragmented adipose tissue with hyaluronic acid in a closed system to guarantee sterility.</p>
Full article ">Figure 2
<p>Berardesca Scale for the patient’s satisfaction evaluation. Subjects’ evaluation of their satisfaction in comparison to D0 (before treatment), after 1 day, 80 and 150 days, by giving scores on firmness and cutaneous relief. Scale of 0–4 for each criterion (0 = unsatisfactory; 4 satisfactory).</p>
Full article ">Figure 3
<p>Numeric Rating Scale (NRS) evaluating defect severity and wrinkles. 10–0 Numeric Rating Scale (NRS) with separate scores for each site (10 = High wrinkle signs or High defect severity; 5 = Medium wrinkle signs or medium defect severity; 0 = Low wrinkle signs or medium defect severity); * <span class="html-italic">p</span> &lt; 0.05.</p>
Full article ">Figure 4
<p>Modified Vancouver scale for the evaluation of ductility, height, vascularity and pigmentation. Modified Vancouver Scale used to estimate the improvement of the skin appearance in comparison to D0 (before treatment), after 1 day, 80 and 150 days. The parameters considered are ductility, height, vascularity and pigmentation. * <span class="html-italic">p</span> &gt; 0.05.</p>
Full article ">Figure 5
<p>Example of treatment on a patient. (<b>A</b>) before treatment; (<b>B</b>) 80 days after treatment.</p>
Full article ">
15 pages, 1634 KiB  
Article
Comparison of Membrane-Based Treatment Methods for the Removal of Micro-Pollutants from Reclaimed Water
by Sukanyah Devaisy, Jaya Kandasamy, Tien Vinh Nguyen, Md Abu Hasan Johir, Harsha Ratnaweera and Saravanamuthu Vigneswaran
Water 2022, 14(22), 3708; https://doi.org/10.3390/w14223708 - 16 Nov 2022
Cited by 8 | Viewed by 2636
Abstract
Dual membrane hybrid systems generally produce reclaimed water for non-potable uses by blending microfiltered biologically treated sewage effluent (BTSE) and reverse osmosis (RO) permeate. This reclaimed water is found to contain a significant amount of micro-pollutants, which possibly cause toxicity effects to aquatic [...] Read more.
Dual membrane hybrid systems generally produce reclaimed water for non-potable uses by blending microfiltered biologically treated sewage effluent (BTSE) and reverse osmosis (RO) permeate. This reclaimed water is found to contain a significant amount of micro-pollutants, which possibly cause toxicity effects to aquatic organisms and plants when exposed to it. Therefore, removing such pollutants from the reclaimed water before reaching the community is highly emphasized nowadays. The currently used treatment of the RO treatment of microfiltered BTSE is energy intensive and not cost effective. This paper focuses on less costly and efficient membrane-based hybrid treatment systems such as the microfiltration-adsorption (MF-GAC) hybrid system, Nano filter (NF) and RO in the removal of micro-pollutants from the microfiltered BTSE. Both the MF-GAC hybrid system and NF (with NTR 729HF membrane) removed 70 to 95% of micropollutants from microfiltered BTSE. The removal depends on the hydrophobicity, charge, and size of the micropollutants. RO was excellent in removing more than 90% of pollutants, while MF was inefficient, as the latter primarily depends on the size exclusion mechanism. Based on the finding, it is suggested to treat only a portion of microfiltered BTSE through the MF-GAC or NF membrane before blending with RO permeate to enhance the removal of micro-pollutants from reclaimed water. The development of sustainable hybrid systems for the removal of all micropollutants of different chemical and physical properties is the key for the water reclamation. Full article
(This article belongs to the Topic Membrane Separation Technology Research)
Show Figures

Figure 1

Figure 1
<p>Schematic diagram of a water reclamation plant at Sydney, Australia (modified from [<a href="#B4-water-14-03708" class="html-bibr">4</a>]).</p>
Full article ">Figure 2
<p>MF-GAC hybrid system (GAC initial dose of 2 g/L).</p>
Full article ">Figure 3
<p>NF/RO membrane filtration unit: (<b>a</b>) schematic diagram; (<b>b</b>) laboratory set-up.</p>
Full article ">Figure 4
<p>Proposed system for the WTP to produce environmentally safe reclaimed water.</p>
Full article ">
Back to TopTop