• Proceedings of the Materials Research Society of Korea Conference
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• 2003.11a
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• pp.110-110
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• 2003

제올라이트는 다양한 유기질 분리의 촉매제 및 광학, 화학 센서, 기체 분리 등의 고기능 소재로서 크게 주목받고 있으며, 그 중 MFI type(ZSM-5, Silicalite-1) 제올라이트는 주로 석유화학공정에 주로 이용되고 있고, 분리막으로서 이산화탄소의 분리/회수 및 물/유기 혼합물의 분리 등에 대한 연구가 활발히 진행되고 있다. 본 연구에서는 분리막 제조에 유리할 것으로 판단되어지는 적합한 크기와 형상을 갖춘 나노크기의 제올라이트 분말을 수열합성법과 마이크로웨이브 합성법을 이용하여 합성하였으며, 위의 조건으로 다공질 알루미나 지지 체 위에서 알루미나/제올라이트 분리막 제조를 하는데 성공하였다. 또 한 다양한 조건(시간, 온도, 조성)에 따른 막의 두께변화와 균열발생정도를 관찰한 결과 합성시간, 건조온도에 따라서 같은 조건의 분리막 사이에서도 현격한 차이가 나타남을 알 수 있었다. 얻어진 MFI type제올라이트 분말과 분리막은 XRD, SEM, BET, TGA, FT-IR등의 분석수단을 이용하여 물성평가를 실시하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.03a
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• pp.1-23
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• 1996

투과증발(Pervaporation)이란 어원적으로 "permeation"과 "evaporation"의 합성어인데 액체혼합물이 치밀한 비다공질막을 통해 이동하는 동안 증기화되면서 분리되는 막분리 공정이다. 이 공정에서 막 한쪽면은 액체공급액과 접하고 있고 다른 한쪽면은 낮은 투과물의 증기압과 접하고 있는데 낮은 증기압은 진공(vacuum pervaporation)을 가하거나 혹은 불활성의 담체가스(sweep gas pervaporation)를 흐르게 하므로써 얻을 수 있다. 이때 막 내부에 트과증발막공정의 추진력인 화학 포텐셜(chemical potential) 구배가 발생하여 막을 통한 물질투과가 이루어지는데 각 투과성분의 투과속도는 투과성분과 막재료간의 물리화학적 인력에 의해 결정된다.의 물리화학적 인력에 의해 결정된다.

• Membrane Journal
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• v.24 no.3
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• pp.240-248
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• 2014

Porous PVDF hollow fiber membranes were prepared by hybrid process of TIPS(thermally induced phase separation) and stretching for membrane distillation. The tests were conducted to investigate that permeability of the membrane could be enhanced by reducing membrane wall thickness. During fiber spinning, dope discharge rate from nozzle was reduced and flow rate of bore fluid increased to make the wall thickness thinner. As dope discharge rate from nozzle was reduced and flow rate of bore fluid increased, the membrane wall thickness was reduced. As a result, air permeability, water permeability and vapor permeability of the membranes increased.

• Membrane Journal
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• v.1 no.1
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• pp.44-54
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• 1991

Sulfonated polystyrene-divinylbenzene(PS-DVB) copolymer membranes were prepared using different diluents (toluene, cyclohexane, cyclohexanol), various diluent ratio and DVB contents. And initial fluxes of organic acids were investigated by varying pH and initial concentration. As a results, water content and ion-exchange capacity decreased with increasing DVB concetration. Among used diluents, cyclohexanol was the most efficient for building up the highest water content and ion-exchange capacity. In the experiment of permeation, carboxylic acid such as formic acid and acetic acid showed higher fluxes when pH was lower than pKa and amino add such as L-alanine showed minimum flux when pH was isoelectric value. The relationaship between initial fluxes and initial concentrations has been expressed by saturation kinetics.

• Journal of the Institute of Electronics Engineers of Korea SD
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• v.40 no.8
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• pp.560-564
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• 2003

Thick oxide layer was fabricated by anodic reaction and complex oxidation performed by combining low temperature thermal oxidation (50$0^{\circ}C$, 1 hr at $H_2O$/O$_2$) and a RTO (rapid thermal oxidation) process (105$0^{\circ}C$, 1 min). Electrical characteristics of OPSL (oxidized porous silicon layer) were almost the same as those of thermal silicon dioxide prepared at high temperature. The leakage current through the OPSL of 20${\mu}{\textrm}{m}$ thickness was about 100 - 500 ㎀ in the range 0 V to 50 V. The average value of breakdown field was about 3.9 MV/cm. From the XPS analysis, surface and internal oxide films of OPSL prepared by complex process were confirmed completely oxidized and also the role of RTO process was important for the densification of PSL (porous silicon layer) oxidized at low temperature.

• Proceedings of the Membrane Society of Korea Conference
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• 1996.10a
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• pp.73-74
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• 1996

역삼투막은 높은 투과율과 배제율, 기계적 강도, 열적 안정성, 화학적 안정성, 성형성, 경제성 등의 여러 가지 조건을 동시에 만족시켜야 한다. 복합막을 통한 역삼투막의 제조는 위의 조건들을 만족시키는 역삼투막을 제조할 수 있는 훌륭한 제조 방법인데 지지막과 표면의 활성층을 여러 가지로 조합하여 다양한 성능의 막을 개발할 수 있기 때문이다. 지지막은 다공질의 고분자막으로 기계적 강도, 화학적.열적 안정성 등이 있어야 하는데 역삼투막이 가혹한 운전 조건에서 조작되기 때문이다. 그리고 지지막은 활성층과 안정된 결합을 할 수 있는 물리적 및 화학적 성질을 지녀야 한다. 활성층은 분리가 일어나는 곳으로 막의 배제율과 투과특성에 큰 영향을 미친다. 따라서 복합막의 제조에 있어서 고려되어야 할 사항은 지지막과 활성층의 재질의 선택, 지지막의 특성, 지지막 위에 얇고 안정된 활성층의 도포 방법, 성능향상과 활성층의 안정화를 위한 제조된 복합막의 후처리 방법 등이다. 지지막 위에 활성층을 도포시키는 방법은 계면중합법, 박층분산법, 침지코팅법, 기상증착법 등을 들 수 있는데 이 중에서 계면중합법을 이용한 복합막의 제조가 가장 실용적인 방법으로 인정되고 있고 현재 실용화되어 있다.

• Journal of the Korean Crystal Growth and Crystal Technology
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• v.9 no.1
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• pp.113-118
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• 1999

Aluminum hydrates were synthesized using $AlCl_3$.$6H_2O$as starting material by precipitation method. The phases of obtained powder were amorphous, boehmite, bayerite, nordstrandite depending on the pH of solutions. Aluminum hydrates transformed to $\alpha-Al_2O_3$via $\gamma$- $Al_2O_3$,$\delta$- $Al_2O_3$,and $\theta$-$Al_2O_3$,and particle sizes were grown by increment of heating temperature. The TEX>$\gamma$- $Al_2O_3$ powder was coated on intermediate layer of ceramic membrane by the dip-coating method, and unsupported membrane was also prepared for comparison. The supported layer showed porous structure with small grains, but the unsupported layer revealed interconnected larger grains. Grain growth is dominant in the unsupported layer than in the supported one.

• Transactions of the Korean hydrogen and new energy society
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• v.24 no.3
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• pp.200-205
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• 2013

The separation of hydrogen depends on porosity, diffusivity and solubility in permeation membrane. Dense membrane is always showing a solution diffusion mechanism but porous membrane is not showing. Therefore, porous membrane has a good hydrogen flux due to pore is carried out transferred media. This mechanism is named as the Knudsen diffusion. Hydrogen molecules or hydrogen atoms are diffused along pore that is a mean free path. In this study, complex layer hydrogen permeation membrane was fabricated by hot press process. And then, it was evaluated and calculated to relationship between hydrogen permeability and membrane porosity.

• Journal of the Korean Ceramic Society
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• v.39 no.12
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• pp.1153-1157
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• 2002

The fabrication of a three-layered asymmetric ceramic membrane was performed by slip casting of the porous alumina support and dip coating of the alumina intermediate layer using high purity ${\alpha}-Al_2O_3$ powders that have different particle size, followed by screen printing-pyrolysis of the $Tio_2$ layer as an ultrafilteration membrane using Ti-naphthenate solution. The bending strength, porosity and mean pore size of the alumina support were 231 kg/$cm^2$s, 30.26% and 0.19 ${mu}m$, respectively. The thickness of the intermediate layer was 30 ${mu}m$ and the mean pore size of that was 0.063 ${mu}m$. Also, the top layer was 0.5 ${mu}m$ thick and micropores with about 20 nm size were formed uniformly.

• Journal of the Korean Ceramic Society
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• v.25 no.1
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• pp.59-65
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• 1988

To develop porous glass membranes used for a effective membrane-separation process, porous glasses and glass membranes were prepared from the sodium borosilicate parent glass by the phaseseparation technique and effects of heat-treatment and leaching conditions on their characteristics were investigated. The crack-free glass membranes could be fabricated from the 9.4 Na2-O-30.7 B2O3-59.2 SiO2-0.7 Al2O3(wt%) parent glass by heat-treatment at the lower temperature(550-570$^{\circ}C$) and for longer than 45 hrs for the phase separation, followed by leaching with 3N-HCl＋60% ethylene glycol solution at 90$^{\circ}C$ over 25 hrs. Porous glasses prepared in this work showed large specific surface areas(400㎡/g) and narrow pore size distribution with the mean pore radius of 14${\AA}$ enough for the application as reverse osmosis membranes. The salt-rejection efficiency and product-flux of the glass membranes heat-treated at 570$^{\circ}C$ for 80 hrs were found to be 51.8% and 270cc/㎡. hr, respectively. This result suggests that the porous glass membranes fabricated in this study could be applied for the reverse osmosis process.