scholarly journals Development of Polydopamine Forward Osmosis Membranes with Low Reverse Salt Flux

Membranes ◽  
2020 ◽  
Vol 10 (5) ◽  
pp. 94
Author(s):  
Pelin Oymaci ◽  
Kitty Nijmeijer ◽  
Zandrie Borneman
Keyword(s):  
Membrane Fouling ◽  
Forward Osmosis ◽  
Salt Flux ◽  
Membrane Properties ◽  
Antifouling Coating ◽  
Dead End ◽  
Reverse Salt Flux ◽  
Stirred Cell ◽  
Coating Temperature

Application of forward osmosis (FO) is limited due to membrane fouling and, most importantly, high reverse salt fluxes that deteriorate the concentrated product. Polydopamine (PDA) is a widely used, easily applicable, hydrophilic, adhesive antifouling coating. Among the coating parameters, surprisingly, the effect of PDA coating temperature on the membrane properties has not been well studied. Polyethersulfone (PES) 30 kDa ultrafiltration membranes were PDA-coated with varying dopamine concentrations (0.5–3 g/L) and coating temperatures (4–55 °C). The quality of the applied coating has been determined by surface properties, water permeability and reverse salt flux using a 1.2 M MgSO4 draw solution. The coating thickness increased both with the dopamine concentration and coating temperature, the latter having a remarkably stronger effect resulting in a higher PDA deposition speed and smaller PDA aggregates. In dead-end stirred cell, the membranes coated at 55 °C with 2.0 g/L dopamine showed NaCl and MgSO4 retentions of 41% and 93%, respectively. In crossflow FO, a low reverse MgSO4 flux (0.34 g/m2·h) was found making a very low specific reverse salt flux (Js/Jw) of 0.08 g/L, which outperformed the commercial CTA FO membranes, showing the strong benefit of high temperature PDA-coated PES membranes to assure high quality products.

scholarly journals Influence of Membrane Properties on Pineapple Wine Clarification and Fouling Behavior

2017 ◽  
Vol 1 (1) ◽  
Author(s):  
W. Youravong ◽  
M. Phukdeekhong ◽  
P. Taksinpatanapong
Keyword(s):  
Pore Size ◽  
Membrane Fouling ◽  
Polyvinylidene Fluoride ◽  
Pilot Scale ◽  
Membrane Properties ◽  
Permeate Flux ◽  
Membrane Pore ◽  
Dead End ◽  
Membrane Pore Size ◽  
Stirred Cell

The experiment was carried out to investigate the influence of membrane pore size and hydrophobicity on the quality of clarified pineapple wine and fouling characteristics, using stirred cell dead–end microfiltration. The test membranes were mixed cellulose acetate (MCE, pore size 0.45 and 0.22 μm), modified polyvinylidene fluoride (MPVDF, 0.22 μm) and polyethersulfone (PESF, 0.22 μm). It was found that all types of membrane successfully clarified the pineapple wine. The membrane pore size and hydrophobicity played an importance role in membrane fouling, both reversible and irreversible. Regarding the permeate flux and fouling, 0.45 μm MCE was the most suitable for pineapple wine clarification. However, intensive organoleptic test with pilot scale would be needed.

scholarly journals Fabrication of a novel cyanoethyl cellulose substrate for thin-film composite forward osmosis membrane

2019 ◽  
Vol 1 (1) ◽  
pp. 18-32 ◽  
Author(s):  
Ke Zheng ◽  
Shaoqi Zhou
Keyword(s):  
Thin Film ◽  
Water Flux ◽  
Forward Osmosis ◽  
Feed Solution ◽  
Salt Flux ◽  
Sem Images ◽  
Film Composite ◽  
Thin Film Composite ◽  
Reverse Salt Flux ◽  
Cyanoethyl Cellulose

Abstract In this study, cyanoethyl cellulose (CEC) was used as a membrane material, and polyvinylpyrrolidone (PVP) was used as pore-forming agent to prepare the substrates for the thin-film composite (TFC) forward osmosis (FO) membrane for the first time. The experimental results demonstrate that the properties of the substrates were significantly improved after PVP was added. The scanning electron microscope (SEM) images show that a two-sublayer structure, a fringe-like top sublayer and macrovoids with sponge-like wall bottom sublayer, were formed after the addition of PVP. These improvements contributed to improved membrane performance during FO tests. Meanwhile, after adding PVP, the TFC membranes exhibited good water flux, and excellent specific reverse salt flux. For instance, the TFC-M2 exhibited 9.10/20.67 LMH water flux, 1.35/2.24 gMH reverse salt flux, and 0.15/0.11 g/L specific reverse salt flux in FO/pressure-retarded osmosis mode while using 1 M NaCl as the draw solution and deionized (DI) water as the feed solution.

scholarly journals Methane production in an anaerobic osmotic membrane bioreactor using forward osmosis: Effect of reverse salt flux

2017 ◽  
Vol 239 ◽  
pp. 285-293 ◽  
Author(s):  
Sheng Li ◽  
Youngjin Kim ◽  
Sherub Phuntsho ◽  
Laura Chekli ◽  
Ho Kyong Shon ◽  
...  
Keyword(s):  
Methane Production ◽  
Membrane Bioreactor ◽  
Forward Osmosis ◽  
Salt Flux ◽  
Osmotic Membrane Bioreactor ◽  
Reverse Salt Flux

scholarly journals Comparative Study for Organic and Inorganic Draw Solutions in Forward Osmosis

2017 ◽  
Vol 13 (1) ◽  
pp. 94-102
Author(s):  
Ahmed Faiq Al-Alalawy ◽  
Talib Rashid Abbas ◽  
Hadeer Kadhim Mohammed
Keyword(s):  
Flow Rate ◽  
Water Flux ◽  
Forward Osmosis ◽  
Solution Concentration ◽  
Salt Flux ◽  
Effect Of Temperature ◽  
Solution Flow Rate ◽  
Solution Flow ◽  
Draw Solution ◽  
Reverse Salt Flux

The present work aims to study forward osmosis process using different kinds of draw solutions and membranes. Three types of draw solutions (sodium chloride, sodium formate, and sodium acetate) were used in forward osmosis process to evaluate their effectiveness with respect to water flux and reverse salt flux. Experiments conducted in a laboratory-scale forward osmosis (FO) unit in cross flow flat sheet membrane cell.  Three types of membranes (Thin film composite (TFC), Cellulose acetate (CA), and Cellulose triacetate (CTA)) were used to determine the water flux under osmotic pressure as a driving force. The effect of temperature, draw solution concentration, feed and draw solution flow rate, and membrane types, were studied with respect to water flux. The results showed an increase in water flux with increasing feed temperature and draw solution concentrations In addition, the flux increased with increasing feed flow rate while the flux was inversely proportional with the draw solution flow rate. The results showed that reverse osmosis membranes (TFC and CA) are not suitable for using in FO process due to the relatively obtained low water flux when compared with the flux obtained by forward osmosis membrane (CTA). NaCl draw solution gave higher water flux than other draw solutions and at the same time, revealed higher reverse salt flux.

scholarly journals Effect of biosurfactant as a novel draw solution on photocatalytic treatment and desalination of produced water by different forward osmosis membranes

2019 ◽  
Vol 20 (1) ◽  
pp. 240-250 ◽  
Author(s):  
Maryam Taghizadeh ◽  
Daryoush Yousefi Kebria ◽  
Farhad Qaderi
Keyword(s):  
Produced Water ◽  
Membrane Surface ◽  
Water Flux ◽  
Forward Osmosis ◽  
Cellulose Triacetate ◽  
Salt Flux ◽  
Draw Solution ◽  
Benzene Toluene ◽  
Reverse Salt Flux ◽  
Contact Angle Analysis

Abstract Water stress and environmental concerns have driven research into the treatment of produced water. In this study, a combination of forward osmosis and photocatalyst system was used for simultaneous salt removal and treatment of produced water. Furthermore, biosurfactant as a novel draw solution and the three types of forward osmosis membranes (cellulose triacetate with and without titanium dioxide (TiO2) and graphene oxide (GO) nanoparticles) were investigated. The morphology and distribution of the TiO2 and TiO2/GO on the membrane surface were assessed by various analyses including field emission scanning electron microscopy, energy dispersive X-ray and contact angle analysis. The results demonstrated that the reverse salt flux was only 0.2 g/m2 h. Moreover, benzene, toluene, ethylbenzene, and xylene (BTEX) removal efficiency in the cellulose triacetate with TiO2 and TiO2/GO membrane under UVC radiation was 62% and 78%, respectively, while the data obtained in visible light reached 80%. The use of TiO2 and TiO2/GO membranes significantly improved the permeability, water flux, photocatalytic degradation of pollutants and desalination of produced water.

Fabrication of nanocomposite forward osmosis hollow fiber membrane for low reverse salt flux by modification of active layer via co-extrusion with graphene oxide

2020 ◽  
Vol 183 ◽  
pp. 121-130
Author(s):  
Kyunghoon Jang ◽  
Joohwan Lim ◽  
Jangho Lee ◽  
Abayomi Babatunde Alayande ◽  
Bumsuk Jung ◽  
...  
Keyword(s):  
Graphene Oxide ◽  
Active Layer ◽  
Hollow Fiber ◽  
Hollow Fiber Membrane ◽  
Forward Osmosis ◽  
Salt Flux ◽  
Fiber Membrane ◽  
Reverse Salt Flux

Modeling the transport of neutral disinfection byproducts in forward osmosis: Roles of reverse salt flux

2020 ◽  
Vol 185 ◽  
pp. 116255 ◽  
Author(s):  
Jiale Xu ◽  
Thien Ngoc Tran ◽  
Haiqing Lin ◽  
Ning Dai
Keyword(s):  
Forward Osmosis ◽  
Disinfection Byproducts ◽  
Salt Flux ◽  
Reverse Salt Flux

scholarly journals Performance Evaluation and Fouling Propensity of Forward Osmosis (FO) Membrane for Reuse of Spent Dialysate

Membranes ◽  
2020 ◽  
Vol 10 (12) ◽  
pp. 438
Author(s):  
Chaeyeon Kim ◽  
Chulmin Lee ◽  
Soo Wan Kim ◽  
Chang Seong Kim ◽  
In S. Kim
Keyword(s):  
Active Layer ◽  
Membrane Fouling ◽  
Membrane Filtration ◽  
Chronic Renal Disease ◽  
Membrane Surface ◽  
Water Flux ◽  
Forward Osmosis ◽  
Salt Flux ◽  
Future Research ◽  
Spent Dialysate

The number of chronic renal disease patients has shown a significant increase in recent decades over the globe. Hemodialysis is the most commonly used treatment for renal replacement therapy (RRT) and dominates the global dialysis market. As one of the most water-consuming treatments in medical procedures, hemodialysis has room for improvement in reducing wastewater effluent. In this study, we investigated the technological feasibility of introducing the forward osmosis (FO) process for spent dialysate reuse. A 30 LMH of average water flux has been achieved using a commercial TFC membrane with high water permeability and salt removal. The water flux increased up to 23% with increasing flowrate from 100 mL/min to 500 mL/min. During 1 h spent dialysate treatment, the active layer facing feed solution (AL-FS) mode showed relatively higher flux stability with a 4–6 LMH of water flux reduction while the water flux decreased significantly at the active layer facing draw solution (AL-DS) mode with a 10–12 LMH reduction. In the pressure-assisted forward osmosis (PAFO) condition, high reverse salt flux was observed due to membrane deformation. During the membrane filtration process, scaling occurred due to the influence of polyvalent ions remaining on the membrane surface. Membrane fouling exacerbated the flux and was mainly caused by organic substances such as urea and creatinine. The results of this experiment provide an important basis for future research as a preliminary experiment for the introduction of the FO technique to hemodialysis.

scholarly journals Integration of Forward Osmosis in Municipal Wastewater Treatment Applications

2021 ◽  
Author(s):  
Stavroula Kappa ◽  
Simos Malamis
Keyword(s):  
Wastewater Treatment ◽  
Membrane Fouling ◽  
Municipal Wastewater ◽  
New Technologies ◽  
Energy Content ◽  
Forward Osmosis ◽  
Treatment Plant ◽  
Oxygen Demand ◽  
Municipal Wastewater Treatment ◽  
Reverse Salt Flux

In recent years, the research community has made constant efforts to develop new technologies for the recovery and valorization of water, nutrient and energy content of municipal wastewater. However, the recovery process is significantly limited due to the low-strength of sewage. Over the last 10 years, the Forward Osmosis (FO) process, has gained interest as a low-cost process with low membrane fouling propensity, which can convert municipal wastewater into a concentrated low-volume effluent, characterized by high organic and nutrient concentration. This chapter presents the main configurations that have been implemented for the concentration of municipal wastewater using FO, including their performance in terms of contaminant removal and water/reverse salt flux (Jw/Js). Furthermore, the draw solutions and respective concentrations that have been used in FO for the treatment of sewage are reported, while at the same time the positive and negative characteristics of each application are evaluated. Finally, in the last section of this chapter, the spontaneous FO followed by anaerobic process is integrated in a municipal wastewater treatment plant (WWTP) and compared with a conventional one. The comparison is done, in terms of the mass balance of the chemical oxygen demand (COD) and in terms of the energy efficiency.

scholarly journals Sonicated membrane separation

2018 ◽  
Vol 14 (s1) ◽  
pp. 89-99
Author(s):  
Balázs Lemmer ◽  
Szabolcs Kertész ◽  
Gábor Keszthelyi-Szabó ◽  
Kerime Özel ◽  
Cecilia Hodúr
Keyword(s):  
Membrane Fouling ◽  
Membrane Separation ◽  
Fermentation Broth ◽  
Membrane Surface ◽  
Permeate Flux ◽  
Separation Processes ◽  
Xylanase Enzyme ◽  
Stirred Cell ◽  
Hydrolysis Of

Membrane separation processes are currently proven technologies in many areas. The main limitation of these processes is the accumulation of matter at the membrane surface which leads to two phenomena: concentration polarization and membrane fouling. According to the publications of numerous authors permeate flux could be increased by sonication. Our work focuses on separation of real broth by sonicated ultrafiltration. The broth was originated from hydrolysis of grounded corn-cob by xylanase enzyme. The filtration was carried out in a laboratory batch stirred cell with a sonication rod sonicator. In our work the effect of the stirring, the intensity of sonication and the membrane-transducer distance was studied on the efficiency of the ultrafiltration and on the quality of separated enzymes. Results reveal that xylanase enzyme can be effectively separated from real fermentation broth by ultrafiltration and enzymes keep their activity after the process. Enzyme activity tests show that low energy sonication is not harmful to the enzyme.

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