• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.65-66
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• 1997

1. 서론 : 현재의 막분리 기술로는 단 단계 분리공정(single-stage separation)으로 약 40%의 산소농축공기(oxygen-enriched air)를 얻을 수 밖에 없지만 심냉법(cryogenic techniques)보다는 에너지 소비율이 적으며, 공정이 비교적 간단하기 때문에 용도에 따라 순 산소를 꼭 필요로 하지 않는 제철소, 발전소 등의 연소분야, 호흡기 환자를 위한 의료분야, 생물공학이나 항공기 분야 등에 편리하게 이용될 수 있다. 이와 같이 용도가 다양한 산소를 분리막을 이용하여 보다 편리하고 값싸게 얻기 위해서는 산소와 질소의 막투과에 대한 새로운 지식을 얻고 막투과가 기체의 어떤 성질에 지배되고 있는가를 조사할 필요가 있다. 본 연구에서는 고무상 고분자막(rubbery polymer membrane)에 대한 산소/질소의 수착특성과 순수한 기체의 투과율(permeation rate)을 기초로 하여 혼합기체의 투과율, 분리인자(separation factor), 막분리 공정변수에 의한 중공사 분리막에서의 기체분리특성에 대하여 연구하였다.

• Membrane Journal
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• v.33 no.6
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• pp.447-453
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• 2023

The performance of computer systems and the development of various computer simulation programs have made it possible to analyze chemical systems composed of more complex elements, and accordingly, research using molecular dynamics simulation is being actively conducted. Research on calculating the gas permeation characteristics of polymer membranes by molecular dynamics, which was previously conducted mainly through experiments, is receiving attention for gas barrier membranes used in food packaging and pharmaceuticals. Recently, there has been a report that a gas barrier effect appears when a coating film is made using silk fibroin, and in this study, a study was conducted using molecular dynamics simulation to confirm whether an oxygen barrier effect appears when a composite film is made using silk fibroin. We built a single model, calculated the gas permeation characteristics, and compared it with the experimental value to confirm that the model reflects the actual experimental results. Actual composite membrane models were then built and the gas movement path within the polymer was analyzed. As a result, oxygen molecules were found that they could not pass through and was blocked in the fibroin region. Therefore, the composite membrane with silk fibroin has excellent oxygen barrier property and is expected to be useful in food packaging, etc.

• Proceedings of the Membrane Society of Korea Conference
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• 2003.05a
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• pp.133-136
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• 2003

• Proceedings of the Membrane Society of Korea Conference
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• 1999.04a
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• pp.56-60
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• 1999

• Proceedings of the Korean Nuclear Society Conference
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• 1999.05a
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• pp.99-99
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• 1999

• Proceedings of the Korean Society of Precision Engineering Conference
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• 2010.11a
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• pp.419-420
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• 2010

• International Journal of Oral Biology
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• v.37 no.1
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• pp.17-23
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• 2012

Recent studies indicate that reactive oxygen species (ROS) are critically involved in persistent pain primarily through spinal mechanisms, and that mitochondria are the main source of ROS in the spinal dorsal horn. To investigate whether mitochondrial ROS can induce changes in membrane excitability on spinal substantia gelatonosa (SG) neurons, we examined the effects of mitochondrial electron transport complex (ETC) substrates and inhibitors on the membrane potential of SG neurons in spinal slices. Application of ETC inhibitors, rotenone or antimycin A, resulted in a slowly developing and slight membrane depolarization in SG neurons. Also, application of both malate, a complex I substrate, and succinate, a complex II substrate, caused reversible membrane depolarization and enhanced firing activity. Changes in membrane potential after malate exposure were more prominent than succinate exposure. When slices were pretreated with ROS scavengers such as phenyl-N-tert-buthylnitrone (PBN), catalase and 4- hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl (TEMPOL), malate-induced depolarization was significantly decreased. Intracellular calcium above $100{\mu}M$ increased malateinduced depolarization, witch was suppressed by cyclosporin A, a mitochondrial permeability transition (MPT) inhibitor. These results suggest that enhanced production of spinal mitochondrial ROS can induce nociception through central sensitization.

• Journal of Korean Society on Water Environment
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• v.21 no.4
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• pp.337-346
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• 2005

An MSBR using a membrane for not only filtration but also aeration (MA-MSBR) was designed to reduce membrane fouling and to enhance water quality, and compared with an MSBR using a membrane for only filtration (BA-MSBR). COD removal efficiency of the MA-MSBR was similar to that of the BA-MSBR, but membrane performance of the MA-MSBR was better than that of the BA-MSBR. The MA-MSBR had more small particles in mixed liquor, so the specific cake resistance of flocs in the MA-MSBR was higher than that in the BA-MSBR. However, in the aerobic reaction step of the MA-MSBR, air went through membrane pores and out of the membrane surface, so cake layers on the membrane surface and a portion of organics adsorbed on membrane pores could be removed periodically. Therefore, cake resistance, $R_c$, and fouling resistance by adsorption and blocking, $R_f$, for the MA-MSBR increased more slowly than those for the BA-MSBR. Additionally, in order to compare the energy efficiency for two MSBRs, oxygen transfer efficiency and power to supply air into the reactor by a membrane module and a bubble stone diffuser were measured using deionized water. From these measurements, the transferred oxygen amount per unit energy was calculated, resulting that of MA-MSBR was slightly higher than that of BA-MSBR.

• Macromolecular Research
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• v.12 no.6
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• pp.553-558
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• 2004

An ultrafiltration membrane (polyethersulfone, PM 10) was surface-modified by treating it with low-tem­perature plasmas of oxygen, acrylic acid (AA), acetylene, diaminocyolohexane (DACH), and hexamethyldisiloxane (HMDSO). The effects that these modifications have on the filtration efficiency of a membrane in waste water treat­ment were investigated. The oxygen, AA, and DACH plasma-treated membranes became more hydrophilic. The water contact angles ranged from < $10^{\circ}\;to\;55^{\circ}$ depending on the type of plasma and the treatment conditions. The oxygen plasma-treated membranes displayed a higher initial flux $(312-429\%),$ but lower rejection $(6-91\%),$ than did an untreated membrane. The AA plasma-treated membranes displayed lower or higher initial flux $(42-156\%),$ depending upon the treatment conditions, but higher rejection $(224-295\%)$ in all cases. The DACH plasma-treated membranes displayed lower initial flux. All of them, especially the AA plasma-treated membrane, displayed improved fouling resistance with either a slower or no flux decline. Acetylene and HMDSO plasma-treated membranes became more hydrophobic and displayed both lower initial flux and lower fouling resistance.

• Membrane Journal
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• v.9 no.1
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• pp.25-35
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• 1999

The sorption and permeation experiments with $O_2$ and $N_2$ were performed with poly sulfone hollow-fiber membrane to obtain oxygen-enriched air. Sorption of $O_2$ on poly sulfone membrane was 1.5'||'&'||'not;2.0 times higher than that of N2. Sorption of oxygen and nitrogen in poly sulfone membrane was described satisfactorily with "dual-mode sorption model". In the low pressure range below 3kgr!cm', about 85% of total sorption was Langmuir-type sorption and only 15% was Henry-type sorption. In the higher pressure above 3kgf/${cm}^2$, Langmuir sorption sites became almost saturated and reached asymptote, and the increase in total sorption with pressurizing might be due to the Henry~type sorption. The ideal separation factor ( P $O_2$/ P $N_2$) was in the range of 2~4, while the actual separation factor for the mixture was reduced to the value of 1.7~2.2.2.2.