• Membrane Journal
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• v.31 no.3
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• pp.170-183
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• 2021

Fouling has continued to be a problem that hinders the effectiveness of membrane properties. To solve this problem of reducing fouling effects on membrane surface properties, different and innovative types of membrane patterning has been proposed. This article reviews on the progress of patterned membranes and their separation process concerning the fouling effects of membranes. The types of separation processes that utilize the maximum effectiveness of the patterned membranes include nanofiltration (NF), reverse osmosis (RO), microfiltration (MF), ultrafiltration (UF), and pervaporation (PV). Using these separation processes have shown and prove to have a major effect on reducing fouling effects, and in addition, they also add beneficial properties to the patterned membranes. Each patterned membrane and their separation processes gave notable results in threshold towards flux, salt rejections, hydrophilicity and much more, but there are also some unsolved cases to be pointed out. In this review, the effects of patterned membrane for separation processes will be discussed.

• Membrane Journal
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• v.31 no.6
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• pp.384-392
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• 2021

Growing pollution due to industrialization leads to difficulties in survival of mankind. Generation of clean water from wastewater by membrane separation process is emerging cost efficient technology. Membrane prepared from renewable resources are in lots of demand to reduce burden on synthetic polymers which is one of the source of environmental pollution. Bacterial cellulose (BC) is very pure and distinct form of cellulose nanofibrils (CNF). Nanopapers prepared from CNF are used ad ultrafiltration (UF) and nanofiltration (NF) membrane for different applications. High crystallinity of BC gives rise to excellent mechanical property, an essential criterion for wastewater treatment membrane. In this review, BC based membrane for application in dye, oil, heavy metal and chemical removal from wastewater is discussed.

• Membrane Journal
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• v.32 no.3
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• pp.198-208
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• 2022

Membrane can selectively separate various substances such as organic substances, liquids, solutes, vapors, gases, ions or electrons according to the separation technology and various uses. Membranes are largely divided into symmetric membranes and asymmetric membranes, and classified into porous and nonporous structure depending on the presence or absence of pores. Also, the interface of the membrane may be molecularly uniform, or chemically or physically non-uniform. Preparation techniques include melt extrusion, stretching, template leaching, track-etching, solution casting, phase inversion, and solution coating method. The prepared membrane can be applied to various applications such as microfiltration, ultrafiltration, nanofiltration, reverse osmosis, gas separation and energy fields. This review provides a tutorial on how to prepare membranes according to the classification and types.

• Membrane Journal
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• v.33 no.3
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• pp.87-93
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• 2023

Electrodialysis (ED) is essential in separating ions through an ion exchange membrane. The disposal of brine generated from seawater desalination is a primary environmental concern, and its recycling through membrane separation technology is highly efficient. Alkali is produced by several chemical industries such as leather, electroplating, dyeing, and smelting, etc. A high concentration of alkali in the waste needs treatment before releasing into the environment as it is highly corrosive and has a chemical oxygen demand (COD) value. The concentration of calcium and magnesium is almost double in brine and is the perfect candidate for carbon dioxide adsorption, a major environmental pollutant. Sodium hydroxide is essential for the metal carbonation process which, is easily produced by the bipolar membrane electrodialysis process. Various strategies are available for its recovery, like reverse osmosis (RO), nanofiltration (NF), ultrafiltration (UF), and ED. This review discusses the ED process by ion exchange membrane for alkali recovery are discussed.

• Membrane Journal
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• v.28 no.1
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• pp.1-20
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• 2018

Fresh water is an important resource for humans, and pressure-driven membrane technology has been widely known as an energy-efficient method to obtain water resource. However, membrane fouling phenomenon, which is one of the major issue during operation, deteriorates membrane permeability. These fouling is usually affected by interaction between surface of membrane and various foulants, therefore, modification of membrane's surface is one of the methods to improve fouling-resistance. This review focuses on the method to modify surface of pressure-driven membranes such as microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO). Specifically, there are two different surface modification methods: (1) adsorption and coating as the physical modification methods, (2) cross-linker, free radical polymerization (FRP), atom transfer radical polymerization (ATRP), plasma/UV-induced polymerization as the chemical modification methods. This review introduces the physico - chemical surface modification methods reported in recent papers and suggests research directions for membrane separation which can increase membrane fouling resistance.

• KSBB Journal
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• v.23 no.1
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• pp.37-43
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• 2008

The use of antihemophilic factor IX complex has been associated with a variety of thrombotic complications, the major cause of which was the contamination of thrombogenic proteins such as vitamin K-dependent clotting factors II, VII, and X. In order to produce a commercial factor IX (GreenNine VF) free from thrombogenic potential, industrial-scale production process for high-purity factor IX from human plasma has been developed. The purification process contains cryo-precipitation, DEAE-sephadex A-50 anion-exchange chromatography, DEAE-toyopearl 650M anion-exchange column chromatography, heparin-sepharose 6FF affinity column chromatography, and CM-sepharose FF cation-exchange column chromatography. Also the process includes two viral inactivation and removal procedures, solvent/detergent treatment and nanofiltration using Viresolve NFP filter. The purification yield was 35.4%. The specific activity in the purified concentrate was 190.8 IU/mg which exceeded that in the factor IX complex (FacNine) by a factor of 48. The activities of factor II, VII, and X were not detected in GreenNine VF. SDS-PAGE analysis showed that GreenNine VF had the highest purity in comparison with commercially available high purity factor IX concentrates, Mononine, Octanyne, Berinin HS, and Immunine STIM plus 600. One batch size of the production was 2,400 vials of 250 IU product or 1,200 vials of 500 IU product from 1,600 L cryo-poor plasma.

• Membrane Journal
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• v.30 no.3
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• pp.158-172
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• 2020

In the aspect of saving energy and water, facilitating the separation membrane for the water treatment has been rising recently as one of the possible solutions. However, microbial biofouling effect is the biggest obstacle that hinders reaching higher permeability over a prolonged period of nanofiltration operation. To solve this problem and fully utilize the filtration membranes with enhanced performance, largely two kinds of solutions are studied and the first and the most commonly mentioned type is the one using the silver nanoparticles. Since silver nanoparticles are important to be well tailored on membrane surface, various methods have been applied and suggested. Using silver nanoparticles however also has the drawbacks or possible toxicity risks, raising the need for other types of utilizing non silver particles to functionalize the membrane, such as copper, graphene or zinc oxides, and amine moieties. Each attempt included in either kind has produced some notable results in killing, preventing, or repelling the bacteria while at the same time, left some unsolved points to be evaluated. In this review, the effects of metal nanoparticles and other materials on the antifouling properties of water treatment membranes are summarized.

• Membrane Journal
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• v.19 no.4
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• pp.277-284
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• 2009

In order to select the most suitable membrane to the concentration of vanadium and silica in groundwater, two different commercial NF membrane modules (NE2540-90 and NF90-2540) and three different commercial RO membrane modules (BW30-2540, RE2540-TE, and XLE-2540) were tested. The membrane characteristics test results showed that NE2540-90 module was the most efficient because of higher permeate flux and similar rejection coefficient. Using NE2540-90 module at the transmembrane pressure of $8\;kgf/cm^2$, it was found that the rejection coefficients of vanadium, silica, aluminium, chromium, iron, boron, strontium, and barium were 98.2%, 99.0%, 92.0%, 83.6%, 96.0%, 45.1%, 98.6%, and 69.5%, respectively. It was possible that vanadium and silica contents of groundwater were concentrated into $148.9\;{\mu}g/L$ and 85.8 mg/L respectively by six-stages NF process at the recovery ratio of 15%. The waters produced by NF, which are enriched in vanadium and silica content, are expected to be commercialized the various functional mineral waters.

• Membrane Journal
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• v.32 no.5
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• pp.314-324
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• 2022

This study is aimed to design a membrane process that systematically removes contaminants including microplastics in sun-dried salt using a separation membrane. In this study, we selected the separation membrane material, pore size, and module suitable for the sun-dried salt fields, and proceeded with the experiments under the salt fields and laboratory conditions. A pilot plant was constructed and tested in our lab and in the actual saltern with the selected 200 kDa, 4 kDa ultrafiltration membranes, and 3 kDa nanofiltration membranes. Most of the impurities in the sea salt were 0.1 ㎛ in size, and more than 7 types of various microplastics were detected in the impurities. After that, as a result of checking the filtered water through the separation membrane process, no impurities were detected. As a result of comparing the existing sea salt component and the sea salt component prepared with separation membrane filtrate, impurities were effectively removed without change in the sea salt component.

• Membrane Journal
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• v.34 no.4
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• pp.205-215
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• 2024

The purpose of this paper was to preparation of organic solvent reverse osmosis (OSRO) membrane using a polyketone (PK) support. The PK support was prepared by non-solvent induced phase separation (NIPS) method, and a polyamide layer was interfacially polymerized on the PK support to fabricate OSRO membrane in the form of thin-film composite (TFC). After that, the surface and cross-sectional morphology of the OSRO membrane were analyzed, and the surface chemical structure of the membrane was analyzed. The water permeance and salt rejection of the OSRO membrane were about 1.28 LMH/bar and 99.0% respectively. The polyamide layer of the OSRO membrane was very stable during 1 day of organic solvent immersion, and the single organic solvent permeance trend was consistent with the organic solvent nanofiltration (OSN) membrane permeance model. The MWCO of the OSRO membrane is 240 g/mol in MeOH. The permeance and separation factor of the OSRO membrane for MeOH-toluene mixture were 200% and 60% higher than those of the commercial OSN membranes respectively.