• Membrane Journal
• /
• v.2 no.1
• /
• pp.67-73
• /
• 1992

The effects of after-treatment condition on the permeability of polysulfone hollow fiber membranes were investigated. It was well known that the permeability of and the rejection of hollow fiber membranes prepared by dry-wet spinning technique was highly affected by spinning conditions such as composition of spinning solution, inner and outer coagulant and spinning height. But these are also governed by after-treatment condition such as drying, hot water treatment and glycerine treatment. Since it was difficult to remove DMAc and NMP in membranes by washing with in cold water and even traces of such solvent affected the reproducibility of the membrane characteristics, the hot water-treatment should be required.

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

• Bulletin of Korea Environmental Preservation Association
• /
• v.28 s.366
• /
• pp.41-45
• /
• 2006

• Proceedings of the Membrane Society of Korea Conference
• /
• 1998.04a
• /
• pp.76-78
• /
• 1998

1. 서론 : 수처리공정에서의 막오염은 효과적인 공정운용을 위해 주요 문제로 인식되고 있으며 막오염은 막표면이나 세공에서 물질의 흡착, 부착 그리고 축적 등과 같은 일련의 메카니즘에 의해 투과율을 저하시키는 결과를 초래한다. 본 연구는 주기적인 역세척(frequency backpulsing)에 의한 중공사막에서의 오염 현상을 규명하여 정수 처리 공정에서 막오염을 최소화시키는 운전 조건을 확립하는 것을 목적으로 하고 있다.

• Journal of Korean Society of Environmental Engineers
• /
• v.36 no.2
• /
• pp.147-152
• /
• 2014

In this research, polysulfone hollow fiber membrane was used to recover $CO_2$ which is one of greenhouse gases from flue gas stream being emitted after the combustion of fossil fuels. The prerequisite requirement is to design the membrane process producing high-purity $CO_2$ from flue gas. For separation of $CO_2$, a membrane module and flue gas containing 10% carbon dioxide was used. The effects of operating conditions such as pressure, temperature, feed gas composition and multi-stage membrane on separation performance were examined at various stage cuts. Higher operating pressure and temperature increased carbon dioxide concentration and recovery ratio in permeate. Recovery ratio and separation efficiency increased if a higher content of $CO_2$ injection gas composition. Three-stage membrane system was producing a 95% $CO_2$ with 90% recovery from flue gas. The separation efficiency of three-stage membrane system was higher than one-stage system.

• Membrane Journal
• /
• v.28 no.3
• /
• pp.180-186
• /
• 2018

The nano-composite membranes were prepared onto the polyvinylidene fluoride (PVDF) hollow fiber membranes through twice dip-coating known layer-by-layer method. For the first coating, poly(vinylsulfonic acid, sodium salt)(PVSA) and Poly(styrene sulfonic acid)(PSSA) were used with varying the concentration and ionic strength (IS) and the poly(ethyleneimine)(PEI) as the second coating material was fixed at 10,000 ppm and IS = 0.3. To characterize the prepared nano-composite membranes, the permeabilities and rejection ratio were measured for each 100 ppm NaCl, $CaSO_4$, $MgCl_2$, and 25 ppm MO aqueous solution. The rejections were increased as the concentrations of coating materials increased. And it was confirmed that the salt rejections for PSSA as the coating material were higher than for PVSA. Typically, the permeability, 1.848 LMH and the rejection for MO 76.3% were obtained at the coating conditions of PSSA 30,000 ppm and I.S = 1.0.

• Korean Chemical Engineering Research
• /
• v.56 no.3
• /
• pp.297-302
• /
• 2018

Bead type and hollow fiber type catalyst (HFC, Hollow Fiber type Catalyst) was prepared by $La_{0.1}Sr_{0.9}Co_{0.2}Fe_{0.8}O_{3-{\delta}}$ (LSCF1928) perovskite powder catalyst which showed excellent methane complete oxidation characteristics through previous studies. The HFC have a cylindrical shape with an empty interior, and pores can be formed through Phase inversion method so the specific surface area can be remarkably improved. In the case of the bead type catalyst prepared by adding Methyl Cellulose (MC), $SrCO_3$ was produced in addition to the original catalyst composition of LSCF1928 due to the reaction of $CO_2$ emitted from MC and Sr of the catalyst. In the case of the HFC, a single phase perovskite structure was obtained without impurities. The HFC calcined at $700{\sim}900^{\circ}C$ showed pore structure of finger-sponge-finger structure, and 99.9% oxygen conversion rate was achieved through complete oxidation of methane at $475^{\circ}C$. Air gap and spinning pressure condition were changed to control the HFC pore. 2 cm air gap and 7 bar spinning pressure showed the best catalytic performance and achieved oxygen conversion rates of more than 70.65%, 93.01%, and 99.99% at $425^{\circ}C$, $450^{\circ}C$ and $475^{\circ}C$, respectively.

• Journal of the Society of Cosmetic Scientists of Korea
• /
• v.24 no.1
• /
• pp.7-24
• /
• 1998

게 껍질로부터 얻은 키틴을 탈아세틸화하여 키토산을 얻었으며, 얻어진 키토산의 유기용매에 대한 용해성을 향상시키기 위해 알칼리 조건에서 고압반응ㅇ기를 사용하여 프로필렌옥사이드와 반응시켜 치환율 3.5의 히드록시프로필 키토산을 합성하였다. 합성된 히드록시프로필 키토산은 고체상 CP/MAS 13C-NMR, 1H-NMR, FT-IR을 통해 반응이 키토산의 6번 탄소의 수산기와 2번 탄소의 아민기에 주로 일어났음을 알 수 있었다. 또한 X-선 회절분석을 통해 키토산의 결정성이 프로필렌옥사이드와의 반응에 의해 크게 감소하였음을 알 수 있었고, 그 결과 유기 용매에 대한 용해성이 현저히 증가되는 현상을 나타내었다. 한편, 히드록시프로필 키토산을 수상에 녹인 후 W/O 에멀젼상에 서 알칼리 촉매를 사용항 에피클로로히드린과 가교반응을 실시한 결과 내부가 비어있는 중공 마이크로비드를 얻을 수 있었다. 전자현미경을 통한 분석결과 중공 마이크로비드의 껍질의 내부에는 스킨층이 형성되어 있었으며, 외부 표면은 다공성이 높은 비대칭 막으로 되어 있음을 확인할 수 있었다.

• Journal of the Korean Society of Hazard Mitigation
• /
• v.3 no.2 s.9
• /
• pp.127-137
• /
• 2003

In locations where the cost of concrete is relatively high, or in situations where the weight of concrete members is to be kept to a minimum, it may be economical to use hollow R.C. members. The ductility of circular hollow R.C. columns with one layer of longitudinal and spiral reinforcement placed near the outside face of the section and the steel tube placed on the inside face of the section is investigated. Such hollow sections are confined through the wall thickness since the steel tube is placed. In this study, moment-curvature analyses are conducted with Mander's confined concrete stress-strain relationship. The variables influenced on the ultimate strain is the ratio and yield strength of confining reinforcement and the compression strength for confined concrete. From this ultimate strain - the transverse reinforcement ratio relationship, the transverse reinforcement ratio for circular hollow reinforced columns with confinement is proposed. The proposed transverse reinforcement ratio is confirmed by experimental results.

• Membrane Journal
• /
• v.31 no.6
• /
• pp.456-470
• /
• 2021

In this study, polyetherimide-based hollow fiber membranes were manufactured using the NIPS (nonsolvent induced phase separation) method. THF, Ethanol, and LiNO₃ were used as additives to control the morphology of the PEI-hollow fiber membranes. Furthermore, for the development of a high hydrogen separation membrane, the spinning conditions were optimized through the characterization of SEM and gas permeance. As a result, as the content of THF increased, the hydrogen/carbon dioxide selectivity increased. However, the permeance decreased due to the trade-off relationship. When ethanol was added, a finger-like structure was shown, and when LiNO₃ was added, a sponge structure was shown. In particular, in the case of a hollow fiber membrane with an optimized PDMS coating layer, the permeance was 40 GPU and the hydrogen/carbon dioxide selectivity was 5.6.