• Proceedings of the Membrane Society of Korea Conference
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• 2004.05b
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• pp.69-72
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• 2004

So far the most practical polymer electrolytes are gel systems, which contain a polymeric matrix, a lithium salt, and aprotic organic solvents. This has met with success but has had disadvantages that the addition of solvents promotes deterioration of the electrolyte's mechanical properties and increases its reactivity towards the lithium metal anode.[1](omitted)

• Bulletin of the Korean Chemical Society
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• v.24 no.1
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• pp.109-112
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• 2003

• Proceedings of the Membrane Society of Korea Conference
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• 2004.05a
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• pp.161-165
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• 2004

Since Loeb and Souriajan first introduced phase inversion method [1], much investigation has been made for understanding the mechanism of formation of asymmetric membranes. Phase inversion is the most extensively used technique for the preparation of asymmetric membranes, which is that cast solution film on a substrate is immersed and is precipitated in water bath.(omitted)

• Proceedings of the Membrane Society of Korea Conference
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• 2004.05a
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• pp.140-143
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• 2004

Compatibility of polymeric materials governs their suitability for nearly all potential applications. An aspect of compatibility that is frequently important for fluoropolymers is their ability to isolate fluids by serving as a barrier to mass transport. This property is commonly expressed as permeability. In ideal cases, both solubility and diffusivity are constant at any given temperature and so the permeability is also a constant.(omitted)

• Membrane Journal
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• v.7 no.4
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• pp.157-166
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• 1997

고분자를 크게 두가지로 대별해 보면 유리상 고분자(Glassy polymer)와 고무상 고분자(Rubbery polymers) 혹은 일레스토머로 나눌수가 있으며 이는 고분자의 유리전이온도(Glass transition temperature)에 따른 분류이다. 즉 유리전이온도가 상온 보다 높아 상온에서 유리상인 고분자를 유리상 고분자라 하고 유리전이온도가 상온보다 낮아서 상온에서 고무상인 고분자를 고무상 고분자라 한다. 이들 두 종류 고분자는 화학적 구조, 화학적 성질, 그리고 물리적 성질면에 있어서 상당히 다르다.

• Membrane Journal
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• v.7 no.2
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• pp.49-56
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• 1997

In order to understand the formation of polymeric membranes or microcellular foams, phase separation phenomena in polymer solutions should be understood. The present review examines the progress made in the understanding of these phenomena, with emphasis on selected polymer-solvent systems. In the case of polymer-solvent systems, coarsening is of particular importance as it may come to dominate or overshadow spinodal decomposition effects within the first minute or few minutes of phase separation. In this article, some of the most important theoretical models of late stage of phase separation are reviewed, and recent experimental studies on coarsening in polymer-solvent systems are studied.

• Journal of Korean Society of Environmental Engineers
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• v.30 no.12
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• pp.1273-1280
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• 2008

This study sought to establish the optimum operating condition for the recovery of caustic (NaOH) solution from mercerization in textile process. As main factors, the silt density index (SDI) evaluation of ceramic membrane for the application of nanofiltration/reverse osmosis (NF/RO) membrane, the recovery yield measurement of caustic solution for the application of polymeric membrane, the optimum condition of chemical cleaning for the membrane regeneration, the optimum removal condition of total organic carbon (TOC), turbidity, color, and the permeate flux of ceramic membrane/polymeric membrane combined process were investigated. As results, ceramic ultrafiltration (UF) in the first step and nanofiltration (NF) in the second step were found to be suitable for the removal of total suspended solid (TSS), residual organics, turbidity including color, and the recovery of caustic solution from caustic wastewater stream in mercerization process. When only the ceramic UF membrane was used, the rejection efficiency of both of TSS and turbidity was more than 99.0%, and the color and TOC were rejected about 74.7% and 49.2%, respectively. Meanwhile, the combined membrane precess of UF and NF membranes showed even more efficient removal abilities and thus more than 99.9% of TSS and turbidity, 87.7% of color, and 78.2% of TOC were removed. In particular, 91.3% of NaOH was successfully recovered with 83.7% of total volume in the combined membrane process. With this regard, a clean caustic solution was obtained in a high purity, which can be reused for mercerization process, expecting to offer economical benefits.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.04a
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• pp.16-19
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• 1996

Separation with synthetic membrane have become increasingly important processes in many fields. In the most application of membrane process, polymer membrane is used. the main advantage of polymers as a material for membrane preparation is the relative simplicity of this film formation which enables one to obtain rather high permeability rates. However, polymeric membranes have several limitations, such as high temperature instability, swelling and decomposition in organic solvent, et. al.. These limitations can be overcome by inorganic membrane. At the present time, commercially available inorganic membranes have pore diameters ranging 5nm to 50mm, and the predominant flow regime in such membrane is Knudsen diffusion. Since the Knudsen permeability is directly proportional to the molecular velocity, gases can be separated due to their molecular masses. However, this separation mechanism is only of important for light gases such as H2 and He. Other separation mechanisms like surface diffusion, active diffusion can play an important role only with very small pore diameters(2nm) and give rise to large permselectivities. Therefore, preparation of inorganic membrane with nano-sized pore have been attracting more and more attention.

• Journal of Environmental Science International
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• v.20 no.9
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• pp.1079-1085
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• 2011

The purpose of this study is to find the operational characteristics of nitrifier-dominated membrane bioreactor (MBR), which has been extensively studied for organic removal, especially in terms of nitrite ($NO_2$-N) build-up and membrane fouling. Membrane fouling is one of the important factor which determines the economics of MBR system. The characteristics of membrane fouling was monitored in terms of the fouling indices such as sludge volume index (SVI), the concentration of total organic carbon (TOC) and extracellular polymeric substances (EPS) in a membrane permeate or sludge extract, the absorbance of supernatant at 260 nm. Most of index values except for protein concentration in EPS had a close relation with the increase of suction pressure and SVI value. Nitrifying MBR was superior to the conventional organic-oxidizing MBR in terms of membrane fouling since the fouling index value of nitrifying MBR was lower than that of BOD-oxidizing MBR.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.04a
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• pp.55-56
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• 1994

There has been many attempts to improve the membrane performance using pervaporation processes[l-3]. They are 1) blending polymer with the high flux and one with high selectivity, 2) an incorporation of functional groups interacting with permeants into a membrane through copolymerization or modification, 3) composite membrane or asymmetric membrane structure with a thin skin layer which acts as a selective layer. Among them, a polymeric membrane containing ion complex group receives an extensive attention recently because ionic complex is known to activate the water transport through ion-dipole interaction. It is especially advantageous in the separation of organic-water system. We applied the ideas of the activation of water transport through ion-dipole. We have reported on the in-sire complex membrane to separate water from aqueous aceiic acid and pyridme solution[4-5] based on the simple acid-base theory. Water transport was enhanced through in-situ complex between pyridine moiety in the membrane and the incoming acetic acid in the feed. In this case, catalytic transport mechanism was proposed. In the present study we used pyridine solution as a feed and the sulfonic acid group in the membrane.