Surface Morphology Of Membranes Research Articles

Pluronic P123/DMSO Lyotropic Liquid Crystal for Incorporating Bioactive Substances for Topical Application.

Lyotropic liquid crystals (LLCs) have attracted considerably growing interest in drug delivery applications over the last years. The structure of LLC matrices is complementary to cell membranes and provides an efficient, controlled, and selective release of drugs. In this work, a complex of experimental methods was used to characterize binary LLCs Pluronic P123/DMSO and triple LLC systems Pluronic P123/DMSO/Ibuprofen, which are interesting as transdermal drug delivery systems. Liquid crystalline, thermal, and rheological properties of LLCs were studied. Concentration and temperature areas of the lyomesophase existence were found, and phase transition enthalpies were evaluated. Intermolecular interactions among the components were studied by infrared (IR) spectroscopy. In vitro studies of Ibuprofen (Ibu) release from various LLCs allow differentiation of its release depending on the polymer content. Atomic force microscopy and contact angle methods were used to characterize the surface morphology of the hydrophobic membrane, which was used as a stratum corneum model, and also evaluate the adhesion work of the LLCs. A complex analysis of the results provided by these experimental methods allowed revealing correlations between the phase behavior and rheological characteristics of the LLCs and release kinetics of ibuprofen. The proposed biocompatible systems have considerable potential for a transdermal delivery of bioactive substances.

Investigating the use of coagulants and Ca2+-rich steel residues as an anti-fouling strategy in the ultrafiltration of microalgae: Towards sustainable resource recovery from wastewater

This study aimed to assess the impact of various coagulants and alternative sources of Ca2+ as pre-treatment on a microalgae suspension undergoing ultrafiltration. Two commercial coagulants, namely aluminum polychloride (PAC) and Tanfloc SL, were compared against two calcium-rich residues from the steel industry: blast oxygen furnace slag and bag filter powder. The filterability of the samples was assessed through permeate flux measurement, analysis of added membrane resistances, and examination of fouling formation mechanisms. Additionally, the characteristics of the formed deposit, including membrane surface morphologies and functional groups, were characterized. Coagulation-flocculation significantly influenced floc characteristics, thereby impacting the filterability of the microalgae samples. Both aluminum polychloride and Tanfloc demonstrated a slight reduction in flux decay, except at 40 mg.L-1 doses, which notably increased normalized final flux. However, Tanfloc exhibited poorer performance compared to coagulated filtrations with calcium-rich residues in terms of fouling. Bag filter powder displayed a 30 % lower fouling resistance than the microalgae suspension without a coagulant. The predominant mechanism observed in fouling formation was attributed to cake layer formation, with the observed fouling being mostly reversible.

Thermo‐responsive polymer to clean fouled forward osmosis membrane after wastewater treatment: Excellent flux recovery

AbstractThermally responsive polymers (TRPs) have gained significant attention in the past decade due to their unique phase transition behavior, those exhibiting changes in properties with temperature variations. In water, hydrophilic block copolymers form helical structures that can transform into hydrophobic globules above the lower critical solution temperature (LCST). Fouling is one of the limiting issues for the forward osmosis (FO) process in wastewater treatment. In this work, after the treatment of wastewater from the paper and pulp industries, foulants were removed from the surface of the commercial polyamide thin‐film composite membrane of the FO process using polyvinyl methyl ether (PVME), a TRP with an LCST of 35–37°C. PVME was mixed with different aqueous solutions to form cleaning solutions. Foulant cleaning experiments utilized a 1% PVME (w/v) solution in 300 mL of de‐ionized (DI) water, while 1 M NaCl solution served as the draw solution (DS) in the FO process. Comparing the water flux (J) and change in membrane hydraulic resistance (Rf) among pristine, fouled, and cleaned membranes revealed a 56.67% increase in water flux and a 51.68% decrease in membrane resistance after PVME mixed with DI water cleaning solution showcasing its effectiveness in improving membrane performance and reducing fouling. The cleaning efficiency of two solutions, that is, 1% PVME mixed in DI water and 1% PVME mixed in 1 M aqueous urea solution, is compared. Results showed that the former cleaning solution helped to obtain 32.62% higher water flux and 56.05% less membrane resistance. Various membrane characterizations are performed, such as field emission scanning electron microscopy (FE‐SEM), which characterizes the membrane's pore structure and surface morphology, while a contact angle analyzer assesses hydrophilicity. This research highlights the use of TRPs as effective cleaning agents, enhancing membrane performance by effectively removing foulants on the membrane surface. Investigating alternative cleaning solutions also provides insights for optimizing water treatment processes.Highlights Cleaning of fouled thin‐film composite membrane using thermal‐responsive polymers (TRPs). Polyvinyl methyl ether, a TRP with an lower critical solution temperature of 35–37°C used as a cleaning agent. 60% increase in water flux was observed after the single‐step cleaning process. Multiple uses of TRP for cleaning performed with no membrane damage.

Role of plasma process gas on permeate flux augmentation of cellulose nitrate membrane for mud water treatment

A comparative study between Nitrogen (N2) and Argon (Ar) plasma is carried out to investigate its effect on surface morphology, hydrophilicity, permeate flux and ageing of cellulose nitrate polymeric membranes in the present work. Langmuir probe and Optical Emission Spectroscopy are used to characterize the plasma. The SEM analysis reveals the noticeable macro-void creations and pore enlargement for both N2 and Ar plasma. The AFM analysis shows a higher surface roughness for Ar plasma treatment as compared to N2 plasma treatment. XPS analysis confirms the changes in the polymer matrix along with the incorporation of various functional groups on the membrane surface as a result of the plasma treatment. A better hydrophilic nature with prolonged plasma treatment is observed for Ar plasma as compared to N2 plasma treatment. The present results show a higher permeate flux with a high rejection rate for Ar plasma treatment in comparison to N2 plasma, which might be due to the pore size and pore area enlargement of the membrane. The hydrophobic recovery for both the plasma-treated membranes is found significant for the initial ageing period of 7 days and found almost stable in nature after 7 days. A diffusion-based theoretical model is developed to study the hydrophobic recovery of plasma-treated membranes. A strong alignment between experimental and theoretical results is observed in the present work. The Cake Filtration model, derived from the Hermia model, is identified as the most suitable model for describing the fouling mechanisms for the present work.

Thermally induced phase separation PVDF membrane fabricated by using NaCl coagulation bath: Relation of membrane surface morphology and permeation performance

Efforts have been made in thermally induced phase separation (TIPS) process to modify the morphology of polyvinylidene fluoride (PVDF) membranes in order to improve their permeation performance and mechanical properties. Nevertheless, many methods not only altered the outer surface but also impacted the overall membrane structure, resulting in a trade-off between permeability and mechanical properties. In this study, we utilized a modified TIPS process to refine the outer surface morphology without altering the bulk structure. This was achieved by introducing NaCl in the coagulation bath. The PVDF membranes were fabricated using a dope with water insoluble diluent dimethyl phthalate (DMP) as main solvent and water-soluble additives polyethylene glycol 400 (PEG400)/triethylene glycol (TEG) as pore formers. The inclusion of NaCl in the coagulation bath serves to decrease the solubility of PEG within this medium, owing to the salting-out effect. Consequently, the NaCl concentration in the coagulation bath emerges as a crucial factor in regulating the migration of PEG400 toward the membrane surface. This control mechanism facilitates the precise adjustment of the outer surface morphology in the fabrication of membranes. As the NaCl concentration increases in the coagulation bath, the outer surface of the fabricated membrane transited from a mesh-like structure to a spherulite structure. As 0.5 mol L−1 NaCl was added to the coagulation bath, the membranes displayed a pure water permeability of 1073.9 L m−2 h−1 bar−1 while maintaining a narrow pore size distribution. Compared to the membranes fabricated without NaCl addition, the increment of the PWP contributed to the slight increase in mean pore size from 65 nm to 84 nm. Meanwhile, the water-insoluble diluent DMP was not affected by the addition of NaCl, which means that the bulk structure of the membrane could be maintained. Consequently, the increase in permeability did not compromise the mechanical properties of the membranes. All the membranes fabricated in this study maintained a reasonable tensile strength of approximately 3 MPa. This study introduces a simple and environmental method to increase the permeability effectively and fine-tune the pore size of the TIPS membranes while having little effect on the bulk structure. Furthermore, the study provides valuable insights into how changes in outer surface morphology can impact the pore size and permeability of TIPS PVDF membranes.

Preparation and surface hydrophilic modification of MOR zeolite membrane potentially appling for acetic acid aldol condensation reaction system

High-performance MOR zeolite membranes were prepared by loading hydrophilic metal oxides onto the surface of α-Al2O3 support via secondary hydrothermal synthesis method. The effects on the surface morphology and hydrophilicity of MOR zeolite membranes were discussed by means of different metal oxides (TiO2, V2O5, CeO2, ZrO2, WO3) and loadings in combination with SEM, XRD, Raman and Water Contact Angle (WCA) characterization. TiO2-MOR zeolite composite membranes were found that TiO2 could increase interface hydrophilicity. The pervaporation performances of TiO2-MOR zeolite membranes at different temperatures and feed concentrations were investigated. The mass transfer model combining Maxwell-Stefan mechanism, Kundsen diffusion and viscous flow was used to describe the mass transfer process of water molecules through the zeolite layer, and within the α-Al2O3 scaffolds, respectively. The permeation fluxes of water molecules of TiO2-MOR zeolite membranes with the loading of 2 wt% were 0.91 kg m−2 h−1, 1.00 kg m−2 h−1 and the separation factors were up to 10000 at 348 K with 90 wt% AcOH/H2O and 90 wt% AA/H2O solutions. TiO2-MOR zeolite membranes with well acid resistance and high hydrophilicity had promising prospects in the reaction scene where carboxylic acid and water exist simultaneously, such as esterification, ester hydrolysis, acetic acid aldol condensation, etc.

Zwitterionic Tröger's Base Microfiltration Membrane Prepared via Vapor-Induced Phase Separation with Improved Demulsification and Antifouling Performance.

The fouling of separation membranes has consistently been a primary factor contributing to the decline in membrane performance. Enhancing the surface hydrophilicity of the membrane proves to be an effective strategy in mitigating membrane fouling in water treatment processes. Zwitterionic polymers (containing an equimolar number of homogeneously distributed anionic and cationic groups on the polymer chains) have been used extensively as one of the best antifouling materials for surface modification. The conventional application of zwitterionic compounds as surface modifiers is intricate and inefficient, adding complexity and length to the membrane preparation process, particularly on an industrial scale. To overcome these limitations, zwitterionic polymer, directly used as a main material, is an effective method. In this work, a novel zwitterionic polymer (TB)-zwitterionic Tröger's base (ZTB)-was synthesized by quaternizing Tröger's base (TB) with 1,3-propane sultone. The obtained ZTB is blended with TB to fabricate microfiltration (MF) membranes via the vapor-induced phase separation (VIPS) process, offering a strategic solution for separating emulsified oily wastewater. Atomic force microscopy (AFM), scanning electron microscopy (SEM), water contact angle, and zeta potential measurements were employed to characterize the surface of ZTB/TB blended membranes, assessing surface morphology, charge, and hydrophilic/hydrophobic properties. The impact of varying ZTB levels on membrane surface morphology, hydrophilicity, water flux, and rejection were investigated. The results showed that an increase in ZTB content improved hydrophilicity and surface roughness, consequently enhancing water permeability. Due to the attraction of water vapor, the enrichment of zwitterionic segments was enriched, and a stable hydration layer was formed on the membrane surface. The hydration layer formed by zwitterions endowed the membrane with good antifouling properties. The proposed mechanism elucidates the membrane's proficiency in demulsification and the reduction in irreversible fouling through the synergistic regulation of surface charge and hydrophilicity, facilitated by electrostatic repulsion and the formation of a hydration layer. The ZTB/TB blended membranes demonstrated superior efficiency in oil-water separation, achieving a maximum flux of 1897.63 LMH bar-1 and an oil rejection rate as high as 99% in the oil-water emulsion separation process. This study reveals the migration behavior of the zwitterionic polymer in the membrane during the VIPS process. It enhances our comprehension of the antifouling mechanism of zwitterionic membranes and provides guidance for designing novel materials for antifouling membranes.

Performance investigation on a self-powered microbial pollutant adsorption cell with N-LAC/PVDF cation exchange membrane

A high-efficiency, self-powered microbial pollutant adsorption cell with an N-LAC/PVDF cation exchange membrane was proposed to remove metal ions and organic dyes in high-salt wastewater. Nitrogen-doped alkali lignin (N-LAC) was synthesized using chitosan nanoparticles (CS) and alkali lignin (AL) using a blending method. The N-LAC/PVDF cation exchange membrane was prepared by chemically grafting polyvinylidene fluoride (PVDF). With modification, hydroxyl, carboxyl, carbonyl, and other hydrophilicity groups were introduced into the cation exchange membrane. The addition of N-LAC improved the membrane's hydrophilicity and adsorption capacity. FITR and SEM, respectively, characterized the surface morphology of the exchange membrane. The result showed that the contact angle reached 74.89° when the amount of N-LAC was 1 wt.%, and the desalination efficiency was 93.5 %, which increased by 70 %. The adsorption capacity of organic dye Pb and metal ion MB was 91 % and 94 %, respectively, showing an increase of 31.9 % and 43.5 %.

Enhancing separation and long-term performance of reverse osmosis desalination through the incorporation of 15-crown-5 in thin-film composite membranes with Li+ and Na+ augmentation

Thin-film composite (TFC) membranes have been intensively studied for the purpose of improving separation performance. Different additives have been attempted during the interfacial polymerization. In this study, 15-Crown-5 (CE15) was employed as the additive to produce TFC membranes for reverse osmosis. The influences of CE15 on the membrane surface morphology, chemical composition and separation performance were then investigated. By adjusting the CE15 concentration, the optimal membrane demonstrated a significant enhancement in water permeance, which was 117% higher than that of the original TFC membrane while sustaining a comparable salt rejection. Additionally, the effects of introducing Li+ and Na+ in the fabrication of CE15 membranes were explored and found to enhance the performance and long-term stability. Overall, our results indicate the potential for enhancing the separation performance of TFC membranes through the synergistic combination of CE15 with Li+ and Na+, offering a simple way of modifying membranes to achieve a higher efficiency and durability in water purification and other separation processes.

Highly permeable nanofibrous polyamide membranes for multi-component wastewater treatment: Exploration of multiple separation mechanism

Multi-component wastewater containing a variety of organic toxins, e.g., dyes and inorganic particulates induces serious environmental concerns, which must be addressed by innovative approaches instead of conventional chemical and physical processes, which are limited by purification efficiency, secondary pollution, and cost-effectiveness. Therefore, it is important to find new avenues of purification methods that are both sustainable and effective. Ultra-fine nanofibrous microfiltration membranes were fabricated by multi-nozzle electrospinning of polyamide-66 (PA-66) and were employed to remove 0.2-μm-nanoparticles and dyes simultaneously from wastewater through filtration and dynamic adsorption performance, in an attempt to discover a one-step filtration system for both dyes and nanoparticles. The fiber diameter and surface morphology of the nanofibrous membranes varied with the concentrations of polyamide solutions, where the ultra-fine nanofibrous membrane exhibited optimum mechanical properties at a specific concentration of PA-66 (11 wt%). The nanofibrous membranes had adsorption capabilities of 133.3 and 204.5 mg/g, respectively, against both anionic dyes (e.g., metanil yellow) and cationic dyes (e.g., chrysoidine), respectively. The membrane also selectively filtrated fine nanoparticles with a nearly 100% rejection ratio. A multiple separation mechanism, including adsorption based on electrostatic interaction, hydrogen bonding interaction, and hydrophobic interaction, as well as depth filtration, was proposed. As an applicable demonstration, the spiral wound cartridge fabricated by PA-66 nanofibrous membrane was used for a simulated multi-component wastewater treatment that contained dyes and nanoparticles of different concentrations. During the multicomponent test at flow rate 1 mL/min, a rejection rate of 97% and greater than 99% were achieved against dyes and nanoparticles, respectively.

One-step rejuvenation for prolonging running lifespan of nanofiltration membranes

Commercial nanofiltration (NF) membranes based on polyamides may experience a decline in permeation performance after prolonged operation. The short lifespan of NF membranes will lead to waste and additional carbon emissions. Thus, rejuvenating membranes and extending their lifespan seem more meaningful than investigating new materials. In this paper, polyamide NF membranes were modified with various polyphenol monomers to improve their permeation performance. The effects of different polyphenols on pore size, surface morphology, and permeation performance of the NF membranes were thoroughly investigated. After modification with tannic acid, the NF membrane exhibits improved salt rejection while experiencing an acceptable decrease in water flux. It should be noted that the commercial NF membrane element fabricated by Koch can recover its Na2SO4 rejection from 83.0% to 94.2% and demonstrate long-term stability after rejuvenation with tannic acid. Combined with the environmental friendliness of polyphenols, this straightforward modification method has the potential for prolonging the operational lifespan of industrial NF membrane products.

Thermal treatment enhanced the hydrophobicity of PVDF hollow fibers membrane for brine treatment using membrane distillation

The objective of this research was to explore the impact of thermal treatment on the characteristics and performance of Poly (vinylidene fluoride) (PVDF) hollow fiber (HF) membranes utilized in direct contact membrane distillation (DCMD). To assess the effects of thermal treatment, the PVDF polymer's allotropy and crystallinity were analyzed using Fourier transform infrared ATR-FTIR and Differential scanning calorimetry (DSC). The thermal treatment predominantly affected the α-phase of the membrane, leading to increased hydrophobicity. On the other hand, Atomic Force Microscopy (AFM) characterized the membrane surface morphology. The AFM characterization revealed an increment in surface membrane roughness leading to an improvement in membrane hydrophobicity. This straightforward technique of thermal treatment resulted in improved membrane properties for DCMD application, such as increased LEP, porosity, and hydrophobicity, as well as reduced water uptake. The DCMD's efficacy was then evaluated using seawater reverse osmosis (SWRO) brine and it was observed that thermal treatment improved flux while slightly reducing salt rejection. In conclusion, these findings display the potential of thermal treatment to enhance the performance of PVDF HF membranes for DCMD applications.

Synergistic roles of oxidation and self-aggregation in efficient ultrafiltration membrane fouling alleviation using a flow-through Sb-SnO2 anode during wastewater reclamation

The application of ultrafiltration (UF) in wastewater reclamation alleviates the demand for limited water supplies. However, the membrane fouling caused by the effluent organic matter (EfOM) becomes a major obstacle for UF application. In this study, a pre-oxidation strategy for UF using a Sb-SnO2 (ATO) anode in flow-through mode was proposed with the hopes to improve the performance of UF during wastewater reclamation. The results indicated that this flow-through ATO (FA) anode significantly outperformed a boron-doped diamond (BDD) anode in terms of EfOM degradation and membrane fouling control. It is noteworthy that apart from oxidation, the self-aggregation behavior of foulants was also involved in the mechanisms of membrane fouling mitigation. On the one hand, FA pre-oxidation relieved the burden of membrane fouling by decomposing the macromolecular EfOM into small molecular organic matter, and even mineralizing it. The effective destruction of unsaturated EfOM by FA pre-oxidation made a remarkable contribution to fouling mitigation due to the strong correlation between the total fouling index and UV254. On the other hand, the surface morphology of membrane and interface properties of foulants revealed the self-aggregation behavior of foulants. FA pre-oxidation made the foulants aggregate spontaneously and reduced the potential of forming a dense cake layer on the membrane surface, which was conductive for water permeation. Overall, FA pre-oxidation proved to be a feasible and chemical-free option for UF pretreatment to simultaneously produce high-quality reused water and alleviate membrane fouling during wastewater reclamation.

Facile Preparation of PVDF/CoFe2O4-ZnO Hybrid Membranes for Water Depollution.

In this investigation, CoFe2O4-PVDF and CoFe2O4-ZnO-PVDF hybrid membranes were prepared using a modified phase inversion method in which a magnetic field was applied during the casting process to ensure a uniform distribution of nanomaterials on the membrane surface. Thus, better absorption of light and increased participation of nanoparticles in the photodegradation process is ensured. The influence of nanomaterials on the crystalline structure, surface morphology, and hydrophilicity properties of the PVDF membrane was investigated. The obtained results indicated that the hybrid membrane exhibited significant differences in its intrinsic properties due to the nanomaterials addition. The hydrophilicity properties of the PVDF membrane were improved by the presence of nanoparticles. The photocatalytic decomposition of aqueous Rhodamine B solution in the presence of the prepared membrane and under visible light irradiation was tested. The hybrid membrane containing CoFe2O4-ZnO on its surface exhibited a high removal rate.

Photocatalytic and antifouling performance of titania-coated alumina membranes produced using a facile sol-gel dip-coating approach

ABSTRACT Photocatalytic membranes (PM) have been investigated as an antifouling strategy for membrane separation processes. Coating ceramic membranes with photocatalytic layers can provide a highly active surface capable of degrading foulants and smaller molecules improving the membrane’s performance when the surface is irradiated by a suitable light. Nevertheless, the coating process often leads to pore blockage due to the formation or deposition of thick layers of photocatalyst on membrane surfaces, which modifies the original membranes’ average pore size and reduces membrane permeability. A facile sol-gel dip coating process was used to produce PM without modifying the original surface morphology of alumina microfiltration membranes. A 3.7-fold increase in permeate volume after 90 min of permeation of an acetaminophen solution in continuous filtration mode under UV light (λ = 365 nm LED, 10W) using titania as photocatalyst compared to the bare alumina membrane without irradiation. Furthermore, fouling modelling proved a reduction in the fouling constant, while fouling mechanisms were not modified. Raman analysis showed 100% anatase formed on the membrane surface. Although membranes could remove up to 87% TOC for oily wastewater filtration, antifouling capabilities for this type of effluent were not observed for the photocatalytic membranes mainly due to fouling inside the pores and light attenuation due to the thick fouling layer on the membrane surface.

Cleaning efficiency and mechanism of ozone micro-nano-bubbles on ceramic membrane fouling

Membrane separation technology using ceramic membrane as carrier has attracted wide attention in drinking water treatment. However, the inevitable problem of irreversible contamination requires high intensity chemical cleaning in place (CIP) to ensure efficient ultrafiltration performance. Therefore, this study discussed the causes of membrane pollution, and further evaluated the purification effects of sodium hypochlorite, different aeration methods and different dosage of ozone as cleaning agents on membrane pollution. Comparison of the physicochemical properties and surface morphology of ceramic membranes before and after cleaning showed that ozone micro-nano-bubbles (O3-MNBs) had excellent cleaning efficiency at the same dosage. MNBs could provide shear forces, while their high mass transfer efficiency increased the dissolved ozone concentration rapidly. The degradation of fouling on the membrane surface was achieved by direct ozone oxidation and indirect oxidation by the generation of OH, resulting in a 100% flux recovery rate in a short time. Our results suggest that O3-MNBs, as a promising CIP method for ceramic membranes, not only significantly improves cleaning efficiency, but also reduces the negative environmental impact of chemical agents.

Insights into the alleviation of membrane fouling in AGMBR through thermal/Fe2+-activated persulfate pre-oxidation: Performance and mechanisms

Aerobic granular sludge membrane bioreactors (AGMBRs) are a viable option for municipal sewage reuse; however, the issue of membrane fouling remains a significant obstacle to overcome to achieve large-scale implementation. Therefore, a novel thermal/Fe2+/persulfate (PDS) system was proposed to investigate its alleviation effect on membrane fouling in AGMBR. The findings indicated that the thermal/Fe2+/PDS system demonstrated superior efficacy in eliminating pollutants from raw sewage. Radical scavenging experiments demonstrated that sulfate radicals and coagulation were the primary contributors to mitigating membrane fouling in the thermal/Fe2+/PDS system, effectively reducing fouling resistance and retarding the decline in membrane flux. Analysis of interfacial interaction energy indicated that increasing the electrostatic double-layer repulsion between foulant–membrane and foulant–foulant could mitigate membrane fouling. Additionally, the interfacial characteristics (membrane surface morphology and foulant content) of the fouled membranes were characterized to further validate the efficacy of this system in alleviating membrane fouling. The correlation analysis revealed a positive association between the mitigation of membrane fouling and the substantial elimination of various pollutants, such as chemical oxygen demand, polysaccharides, and suspended solids. This study highlights the exceptional performance of the thermal/Fe2+/PDS system and provides novel insights into alleviating AGMBR membrane fouling.

Acid mine drainage (AMD) treatment using a novel tannic acid functionalized Boehmite/polyether sulfone nanofiltration membrane

This study focuses on the fabrication of TA-BM/PES membranes by the incorporation of tannic acid functionalized Boehmite nanoparticles into the PES membrane matrix through the phase inversion technique. The presence of TA-BM nanoparticles in the TA-BM/PES membranes was confirmed by analysis of the FT-IR spectra of the embedded membranes. The hydrophilicity, permeability, surface morphology, and fouling resistance properties of membranes modified with TA-BM nanoparticles were compared to those of the naked membrane. The fouling behavior of the modified membranes was assessed in the presence of a foulant solution containing 200 ppm BSA (bovine serum albumin) and 200 ppm Na2SO4. The flux recovery ratio results showed an improvement in all modified membranes, especially M2 membrane. The modified membranes shown remarkable efficiency in the rejection of heavy metal ions (over 72 %), sulfate (over 80 %), and salt (Na2SO4 > 84 % and NaCl>48 %). The M2 membrane was chosen as the most suitable membrane and shown effective performance in eliminating heavy metals (Fe2+ = 65.5, Mn2+ = 88.8, Mg2+ = 83.5 and Ca2+ = 78.6 %) as well as sulfate (SO42− = 83.5 %) from a synthetic acid mine drainage (AMD) wastewater. Based on the findings presented in this research, it can be concluded that the TA-BM/PES nanofiltration membrane has potential for effective use in the treatment of AMD wastewater.

Deep Eutectic Solvent Coated Cerium Oxide Nanoparticles Based Polysulfone Membrane to Mitigate Environmental Toxicology.

In this study, ceria nanoparticles (NPs) and deep eutectic solvent (DES) were synthesized, and the ceria-NP's surfaces were modified by DES to form DES-ceria NP filler to develop mixed matrix membranes (MMMs). For the sake of interface engineering, MMMs of 2%, 4%, 6% and 8% filler loadings were fabricated using solution casting technique. The characterizations of SEM, FTIR and TGA of synthesized membranes were performed. SEM represented the surface and cross-sectional morphology of membranes, which indicated that the filler is uniformly dispersed in the polysulfone. FTIR was used to analyze the interaction between the filler and support, which showed there was no reaction between the polymer and DES-ceria NPs as all the peaks were consistent, and TGA provided the variation in the membrane materials with respect to temperature, which categorized all of the membranes as very stable and showed that the trend of stability increases with respect to DES-ceria NPs filler loading. For the evaluation of efficiency of the MMMs, the gas permeation was tested. The permeability of CO2 was improved in comparison with the pristine Polysulfone (PSF) membrane and enhanced selectivities of 35.43 (αCO2/CH4) and 39.3 (αCO2/N2) were found. Hence, the DES-ceria NP-based MMMs proved useful in mitigating CO2 from a gaseous mixture.

Synthesis and Characterization of Antibacterial Chitosan Films with Ciprofloxacin in Acidic Conditions.

This work presents the results of research on obtaining chitosan (CS) films containing on their surface ciprofloxacin (CIP). A unique structure was obtained that not only gives new properties to the films, but also changes the way of coverage and structure of the surface. The spectroscopic test showed that in the process of application of CIP on the surface of CS film, CIP was converted from its crystalline form to an amorphic one, hence improving its bioavailability. This improved its scope of microbiological effect. The research was carried out on the reduction of CIP concentration during the process of CIP adhesion to the surface of chitosan films. The antibacterial activity of the CS films with and without the drug was evaluated in relation to Escherichia coli and Staphylococcus aureus, as well as Candida albicans and Penicillium expansum. Changes in the morphology and roughness of membrane surfaces after the antibacterial molecule adhesion process were tested with atomic force microscopy (AFM) and scanning electron microscopy (SEM). Structural analysis of CS and its modifications were confirmed with Fourier-transform spectroscopy in the infrared by an attenuated total reflectance of IR radiation (FTIR-ATR) and solid-state nuclear magnetic resonance (NMR).