• Journal of the Korean Ceramic Society
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• v.38 no.1
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• pp.34-38
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• 2001

Hot filament CVD 방법에서 가스압을 증가시키는 방법을 사용하여 nanocrystalline 다이아몬드 막을 합성하였다. 메탄-수소 혼합가스를 사용하고 메탄함량, 유량, 기판온도합성시간은 각각 4%, 100sccm, 110$0^{\circ}C$, 10시간으로 일정하게 유 였다. 합성 변수로서 가스압을 40 Torr에서 300 Torr 구간에서 변화시켰다. High-resolution SEM으로 막 표면의 형상을 관찰하고, TEM, XRD, micro-Raman spectroscopy를 사용하여 합성된 막의 구조 및 특성을 분석하였다. 합성된 다이아몬드 막은 압력이 높아짐에 따라 mocrocrystalline 다이아몬드 막에서 점진적으로 nanocrystalline 다이아몬드 막으로 변화해갔으며, 가스압에 다라 비다이아몬드 상의 량이 증가하였다. 증착속도는 microcrystalline 다이아몬드 막이 형성되는 구간에서는 압력에 따라 1.1~1.3 $\mu\textrm{m}$/h까지 증가하다가 nanocrystalline 다이아모느 막이 형성되는 구간에서는 압력에 따라 감소하였다. 감소하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.10a
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• pp.30-31
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• 1994

분리막을 이용한 분리기술은 일반증류법에 의한 분리 또는 정제에 어려운 액체 혼합물을 분리하는데 적용될 수 있고 또한 미래 산업적인 중요성 때문에 최근 유용한 정제법으로 주목을 끌고 있다. 한편, 투과증발법에 의한 액체혼합물의 분리는 공정자체는 매우 간단하면서도 분리막의 투과성능에 따라 분리효율이 달라지기 때문에 이에 적합한 고분자 분리막의 개발은 아직도 많은 연구과제로 남아있는 상태이다. 따라서 본 연구에서는 증류법이나 기타방법에 의하여 회수된 저 농도의 유기수 용액으로부터 물을 보다 효율적으로 분리하여 고농도의 특정순수 유기용제를 얻으려는데 목적을 두고 보다 높은 물 선택성과 투과율을 갖는 새로운 복합막을 개발하기 위해 고흡수성 고분자재료인 CMC와 PVA 그리고 PAA를 소재로 하여 목적하는 분리기능을 갖는 새로운 복합막을 제조하여 실용가능성을 검토하기 위하여 투과증발 분리실험을 하였다.

• Membrane Journal
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• v.13 no.4
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• pp.291-299
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• 2003

Polymer membranes such as poly(1-trimethylsilyl-1-propyne)-polyetherimide (PTMSP-PEI) and poly(dimethylsiloxane)- polyetherimide (PDMS-PEI) composite membrane were prepared by solution casting method. To investigate the characteristics of these membranes, the analytical methods such as FT-IR, $^1H-NMR,$ DSC, TGA, GPC, and SEM have been utilized. The number-average (equation omitted) and weight-average (equation omitted) molecular weight of PTMSP were 477,920 and 673,329 respectively. The glass transition temperature ($T_g$) of PTMSP was $224^{\circ}C.$ The separation of the gas mixture ($H_2/N_2$) through the composite membranes were studied as a function of pressure. The separation factor (${\alpha}, {\beta},$ quation omitted) of the composite membranes used in this work increased as the pressure of permeation cell increased. The real separation factor (${\alpha}$), head separation factor (${\beta}$), and tail separation factor (equation omitted) of PTMSP-PEI composite membrane were 2.28, 1.17, and 1.96 respectively at ${\Delta}P$ 30psi and $25^{\circ}C.$ (${\alpha}, {\beta}$ and equation omitted of PDMS-PEI composite membrane were 3.70, 1.53, and 2.42 respectively at ${\Delta}P$ 30psi and $25^{\circ}C$.

• Membrane Journal
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• v.10 no.3
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• pp.148-154
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• 2000

Poly(vinyl alcohol)(PVA)/sulfur-siccinic acid(SSA) membrane performances have been studied for the vapor permeation separation of methyl tort-butyl ether(MTBE)/methanol mixtures with varying operation temperatures, amount of cross-linking agents, and feed compositions. 1'here are two factors, the membrane network and the hydrogen bonding, in the swelling measurements of PVA/SSA membranes. These two factors act interdependently on the membrane swelling. The sulfuric acid group in SSA took an important role in the membrane performance. The cross-linking effect might be more dominant than the hydrogen bonding effect due to the sulfuric acid group at 7% SSA membrane. Hydrogen bonding effect was more important for 5% SSA membrane. In vapor permeation, density or concentration of methanol in vapor feed is lower than that of methanol in liquid feed, as a result, the hydrogen bonding portion between the solvent and the hydroxyl group in PVA is reduced in vapor permeation. In this case, the 7% SSA membrane shows the highest separation factor of 2187 with the flux of 4.84g/$m^2$hr for MTBE/methanol=80/20 mixtures at 3$0^{\circ}C$.

• Membrane Journal
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• v.33 no.6
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• pp.377-382
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• 2023

In this study, a PEBAX/PVDF composite membrane was fabricated, and its pervaporation performance was tested in an ethanol/water mixture. In addition, we attempted to improve the pervaporation performance of the composite membrane by forming a ZIF-8 layer on the surface of the PVDF substrate. The thickness of selective layer was optimized by comparing the pervaporation performance depending on the PEBAX thickness. A pervaporation test was performed on the Ethanol/Water mixture. As a result, the composite membrane using PVDF substrate with ZIF-8 layer had a flux of 1.98 kg/m²h and separation factor of 3.88, showing higher values of both permeation flux and selectivity than the composite membrane using bare PVDF substrate.

• Membrane Journal
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• v.34 no.3
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• pp.192-203
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• 2024

The advancement of commercially viable gas separation membranes plays a pivotal role in improving CO₂ separation efficiency. High-molecular-weight poly(ethylene oxide) (high-Mw PEO) emerges as a promising option due to its high CO₂ solubility, affordability, and robust mechanical attributes. However, the crystalline nature of high-Mw PEO hinders its application in gas separation membranes. This study proposes a straightforward blending approach by incorporating various polymeric additives into high-Mw PEO to address this challenge. Four commercially available, water-soluble polymers, i.e. poly(ethylene glycol) (PEG), poly(propylene glycol) (PPG), poly(acrylic acid) (PAA), and poly(vinyl pyrrolidone) (PVP) are examined as additives to enhance membrane performance by improving miscibility and reducing PEO crystallinity. Contrary to expectations, PEG and PPG fail to inhibit the crystalline structure of PEO and result in membrane flaws. Conversely, PAA and PVP demonstrate greater success in altering the crystal structure of PEO, yielding defect-free membranes. A thorough investigation delves into the correlation between changes in the crystalline structure of high-Mw PEO blend membranes and their gas separation performance. Drawing from our findings and previously documented outcomes, we offer insights into designing and selecting additive polymers for high-Mw PEO, aiming at the creation of cost-effective, commercially viable CO₂ separation membranes.

• Proceedings of the Membrane Society of Korea Conference
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• 1994.10a
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• pp.24-25
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• 1994

고분자 분리막을 통한 메탄과 이산화탄소의 분리는 천연가스에서 불순물로 작용하는 이산화탄소를 분리시켜 천연가스의 순도를 향상시키는데 활용할 수 있으며, 바이오가스나 제철소 폐가스로부터의 이산화탄소의 분리, enhanced oil revovery 공정에서의 이산화탄소의 분리, 그리고 지구 온난화의 원인이 되는 대기중의 이산화탄소 농도의 감소등에서 활용될수 있다. 이러한 분리막 공정은 여러 혼합기체에 대해 단순하고 간편하며 에너지 소비가 적다는 장점에 의해 기체분리에 효과적이고 응용성있는 공정으로 대두되고 있는데, 그 중에서도 분리막의 투과도(Permeability)와 선택도(Selectivity)를 동시에 높일수 있는 새로운 막재료의 개발에 관한 연구가 활발히 진행되고 있다. 이를 위해 고분자 구조를 화학적으로 변화시키는데, 이 경우에는 고분자의 구조 변화와 투과특성간의 관계를 밝히는 것이 매우 중요하다.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.10a
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• pp.109-111
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• 1998

TIPS 공정에 의한 고분자막 제조기술은 기존의 적정용매가 없어서 분리막 소재로 상용할 수 없었던 결정성 고분자 및 고강도 엔지니어링 플라스틱 등에 대하여 소재의 폭을 넓힐 수 있고 적정 희석제와의 혼합으로 고분자 소재의 용융점을 강화 시킬 수 있어 가공온도의 제약을 어느정도 해결할 수 있다는 장점을 가지고 있다. 또한 TIPS 공정에 의해 제조되는 고분자 matrix, 혹은 고분자 막의 미세구조는 선택된 고분자와 희석제의 종류 및 상분리 mechanism에 따라 크게 달라지므로 이들 제조 변수의 적절한 조절을 할 수 있다. 본 연구에서는 열유도 상분리 공정과 연신공정을 통해 몇가지 제조변수를 조절하여 미세다공성 중공사막을 제조하였다. 고분자-희석제 용융액의 melt viscosity를 변화시켜 보았고, 희석제의 추출 후 열처리를 하여 이에 따른 영향을 알아보았다. 상분리 속도가 막의 구조 및 성능에 미치는 영향을 알아보기 위해 coagulation bath temperature를 변화시켜 보았으며, 몇가지 종류의 coagulant를 사용하여 막을 제조한 후 성능을 측정해 보았다. 또한 기존의 상업용 막과 성능 및 구조를 비교하여 보았다.

• Membrane Journal
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• v.28 no.6
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• pp.424-431
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• 2018

The gas separation performance of a mixed membrane structure based on a mixture of polyethersulfone (PES) and cobalt tetraphenylporphyrin-benzylimidazole (CoTpp-BIm) as an oxygen carrier was investigated. The CoTpp-BIm mixed PES membrane had an asymmetric structure with a mixture of finger structure and sponge-like structure, and the upper surface was dense. The gas separation performance test was carried out using $94%\;N_2$ gas and $6%\;O_2$ mixed gas. Oxygen and nitrogen permeability coefficients were measured at ${\Delta}P$ ranging from 15 to 228 cmHg and the permeate side of the PES membrane was maintained at vacuum level. The oxygen permeability coefficient of CoTpp-BIm mixed PES membranes increased as supplied pressure was decreased. When the supply pressure was 15 cmHg, the gas permeability ($P_{O_2}$) was 6676 Barrer, the $O_2/N_2$ selectivity (${\alpha}$) was 6.1, and the promoting factor (F) was 2.39. Based on these results, it was confirmed that the addition of CoTpp-BIm to the PES film improved the oxygen separation characteristics.

• Membrane Journal
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• v.31 no.3
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• pp.200-211
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• 2021

In this study, mixed matrix membranes were prepared by mixing the synthesized zeolitic imidazolate framework-7 (ZIF-7) with poly(ether-b-amide) 2533 (PEBAX2533). A single gas (N₂, CO₂) was permeated through the membrane to investigate the properties of the gas. Through FT-IR, XRD, and FE-SEM, the peaks and shapes of ZIF-7 were confirmed, and it was determined that the synthesis was successful. Through TGA, it was confirmed that ZIF-7 has excellent thermal stability and that when incorporated into the membrane, the thermal stability is improved compared to pure PEBAX2533. It was found that ZIF-7 synthesized through BET had excellent CO₂ adsorption capacity and CO₂/N₂ adsorption selectivity showed a high value of about 49.64. For the gas permeation, as the ZIF-7 content in the mixed membrane increases, the N₂ permeability decreases and the CO₂ permeability slightly decreases, while the CO₂/N₂ selectivity steadily increases. In particular, when 20 wt% of ZIF-7 was added, the CO₂ permeability did not decrease significantly and the CO₂/N₂ selectivity increased considerably, resulting in the performance approaching to the Robeson upper-bound.