• Membrane Journal
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• v.24 no.6
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• pp.491-497
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• 2014

PTMSP-silica composite membranes were prepared by addition of 0, 15, 20, and 30 wt% TEOS (tetraethoxysilane), TMOS (tetramethoxysilane), MTMOS (methyltrimethoxysilane), and PTMOS (phenyltrimethoxysilane) contents to PTMSP using sol-gel process. The gas permeability of the composite membranes for $H_2$, $N_2$ and ideal selectivity for $H_2$ over $N_2$ were investigated as a function of alkoxysilane content. The permeabilities for $H_2$ and $N_2$ increased in the range of alkoxysilane contents 0~20 wt%, however decrease the range of 20~30 wt%. The ideal selectivities for $H_2$ over $N_2$ decreased in the range of TEOS and PTMOS contents 0~15 wt%, but increased in the range of 15~30 wt%. When compared to the upper bound of Robeson, PTMSP-silica composite membranes with TEOS content of 30 wt%, MTMOS content of 20 wt% and PTMOS content of 30 wt% turned out to be a simultaneous improvement in ideal selectivity and permeability.

• Membrane Journal
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• v.33 no.6
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• pp.369-376
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• 2023

In this study, the alternative to the energy-intensive conventional vacuum distillation process, an eco-friendly and energy-efficient pervaporation separation was employed in 1,2 hexane diol/water (HDO/water) mixture. The crosslinked PVA-glutaraldehyde was coated inside the alumina hollow fiber membrane (Al-HF). In the HDO/IPA pervaporation separation, optimization of the membrane concerning PVA/GA ratio, curing temperature, and pervaporation operating condition were performed. In the long-term stability test, the sustainable pervaporation separation performance giving flux in the range of 1.90~2.16 kg/m²h, and water content in permeate was higher than 99.5% (separation factor = 68) was obtained from the PVA/GA (molar ratio = 0.08, curing temperature = 80℃) coated Al-HF membrane from HDO/water (25/75, w/w, %) mixture at 40℃. Therefore, this work provides potential and inspiration for PVA-based membranes to mitigate excessive energy requirements in HDO/water separation by pervaporation.

• Journal of the Korean Society of Food Science and Nutrition
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• v.43 no.3
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• pp.454-458
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• 2014

In this study, we examined the ionization rate and permeability of nanocalcium prepared from oyster shells with various particle sizes. Four particle sizes of the calcium samples were prepared by centrifugation according to their density disparity in alcoholic solution: NC (normal calcium), C-1 (supernatant of 1,000 rpm), C-2 (supernatant of 2,000 rpm), and C-3 (supernatant of 3,000 rpm). Particle sizes of NC, C-1, C-2, and C-3 were $2,280.3{\pm}64.3nm$, $521.3{\pm}83.3nm$, $313.9{\pm}29.5nm$, and $280.0{\pm}3.4nm$, respectively. C-3 showed a slight increase in ionization rate compared with the other calcium samples, but their differences were not significant. Dialysis membrane-employed analysis showed that nanocalcium permeability increased as its particle size smaller; 32% of C-3 nanocalcium was transported to the outside of the membrane, whereas C-1 showed a 25% transport rate. We determined the permeability of the nanocalciums by using rat intestinal sacs, in order to provide different intestinal environments depending on pH level. Nanocalcium generally showed a higher permeability at pH 7, which represents an ileum environments compared to the duodenum and jejunum environments at pH 4.2 and pH 6.2, respectively. However, C-3 calcium showed the highest permeability, followed by C-2, C-1 and NS calciums. This result shows that the size of calcium positively affected its permeability in the intestinal sac. Taken together, nano-sized calcium derived from discarded oyster shell shows improved permeability in intestinal environments.

• Applied Chemistry for Engineering
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• v.26 no.4
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• pp.413-420
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• 2015

PTMSP-ZIF composite membranes were prepared by the addition of zeolitic imidazolate framework (ZIF-8) into poly (1-trimethylsilyl-1-propyne) (PTMSP) having high gas permeability to improve trade-off relationship of the polymer membrane. PTMSP-ZIF composite membranes were prepared with different amounts of ZIF-8; 0, 5, 10, 20, 30 and 40 wt%. Gas permeation properties for $H_2$, $N_2$, $CO_2$, and $CH_4$ were investigated by increasing the amount of ZIF-8 in the PTMSP. The gas permeability of PTMSP-ZIF composite membranes within 5~30 wt% of ZIF-8 contents increased as ZIF-8 contents went up and decreased thereafter. The gas permeability for $CO_2$ showed the maximum value of 76080 barrer at 30 wt% of ZIF-8 content and PTMSP-ZIF composite membrane containing 20 wt% of ZIF-8 content had the highest selectivity ($CO_2/N_2$) with the value of 8.2. The selectivity ($H_2/N_2$) and selectivity ($CO_2/CH_4$) were almost the same as PTMSP in the range 10~40 wt% of the ZIF-8. Overall, PTMSP-ZIF composite membranes resulted in maintained selectivity and increased permeability compared to those of PTMSP membranes.

• Membrane Journal
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• v.23 no.5
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• pp.332-342
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• 2013

In the present study, carbon molecular sieve (CMS) hollow fiber membranes were prepared by carbonizing a methyl imide hollow fiber precursor, which was spun by non-solvent induced phase separation process. And effects of carbonization parameters such as pre-oxidation, pyrolysis, and post-oxidation on the gas permeation were systematically investigated. CMS membrane having the highest gas flux was obtained by carbonizing the precursor through a combined process of air pre-oxidation at $250^{\circ}C$ for 2h, nitrogen pyrolysis at $550^{\circ}C$ for 2h, and oxygen post-oxidation at $250^{\circ}C$ for 2h. The optimized membrane showed a considerable gas permeance : the $H_2$, He, $CO_2$ permeances were 69.72, 35.61, 31.01 GPU, respectively, and the $O_2$ and $N_2$ permeances were ignorable. Therefore, it was clear that the prepared CMS hollow fiber membrane was a promising membrane for recovering small gases such as hydrogen and hellium and carbon dioxide.

• Applied Chemistry for Engineering
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• v.10 no.6
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• pp.954-959
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• 1999

Radiation-induced grafting of 2-hydroxyethyl methacrylate(HEMA), acrylic acid(AAc) and methacrylic acid(MAAc) onto polypropylene microfiltration membrane has been studied. The effect of grafting conditions such as solvent composition(MeOH and $H_2O$) and monomer concentration on the grafting yield in investigated. The highest degree of grafting is obtained at a solvent composition of 25% $H_2O$:75% MeOH for HEMA, pure water for AAc and 50% $H_2O$:50% MeOH for MAAc. Modification of the PP membranes with hydrophilic monomers is shown to cause an increase in the water permeation flux of the membranes. It is found that HEMA is the best monomer to increase the water permeation flux and the highest water permeation flux is obtained at 99% degree of grafting. The water permeation flux of AAc-grafted PP membrane and MAAc-grafted PP membrane is very sensitive to environmental pH and $Cu^{2+}$ ion, but the water permeation flux of HEMA-grafted PP membrane scarcely depends on pH and $Cu^{2+}$ ion.

• Membrane Journal
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• v.22 no.1
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• pp.16-22
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• 2012

The influence of co-existing gases on the hydrogen permeation without sweep gas was studied through a Pd-coated $V_{99.8}B_{0.2}$ alloy membrane. Membranes have been investigated in the pressure range 1.5-8.0 bar under pure hydrogen, hydrogen-carbon dioxide and hydrogen-carbon monoxide gas mixture without sweep gas at $400^{\circ}C$. Preliminary hydrogen permeation experiments without sweep gas have been confirmed that hydrogen flux was $40.7mL/min/cm^2$ for a Pd-coated $V_{99.8}B_{0.2}$ alloy membrane (thick : 0.5 mm) using pure hydrogen as the feed gas. In addition, hydrogen flux was $21.4mL/min/cm^2$ for $V_{99.8}B_{0.2}$ alloy membrane using $H_2/CO_2$ as the feed gas. The hydrogen permeation flux decreased with decrease of hydrogen partial pressure irrespective of pressure when $H_2/CO_2$and $H_2/CO$mixture applied as feed gas respectively and permeation fluxes were satisfied with Sievert's law in different feed conditions. It was found from XRD, SEM/EDX results after permeation test that the Pd-coated $V_{99.8}B_{0.2}$ alloy membrane had good stability and durability for various mixtures feeding condition.

• Membrane Journal
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• v.28 no.4
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• pp.279-285
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• 2018

The pervaporation separation of isopropanol/water mixture was carried out on a series of chemically cross-linked poly(vinyl alcohol)(PVA) composite membranes. The membranes were prepared by casting three kinds of PVA solutions with varying concentrations of PVA and GA onto polyacrylonitrile (PAN) support followed by thermal cross linking. As the PVA concentration increased, the flux decreased but separation factor was increased. It was confirmed that the composite membrane coated with PVA-3 (98~99% hydrolyzed) at a concentration of 7 wt% PVA and 20 wt% glutaraldehyde (GA) exhibited a flux of $209g/m^2h$ and a separation factor of more than 100. The submerged module test was carried out with controlled feed tank temperature and IPA concentration of the feed solution. The continuous concentration of IPA solution was increased from 90% to 99% after 60 h.

• Proceedings of the Korean Vacuum Society Conference
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• 2000.02a
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• pp.84-84
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• 2000

수소화된 비정질 실리콘(a-Si:H)과 미세결정질 실리콘 ($\mu$c-Si:H)은 저온.건식 공정인 PECVD로 값싼 유리 기판을 사용하여 넓은 면적에 증착이 가능하다는 큰 장점으로 인해 광전소자(photovoltaic device)와 박막 트랜지스터(TFTs)등에 폭넓게 응용되어 왔으며 최근에는 nm 크기의 실리콘 결정(nc-Si)에서 가시광선 영역의 발광 현상이 발견됨에 따라 광소자로서의 특성을 제어하기 위해서는 성장 조건과 공정 변수에 따른 구조 변화에 대한 연구가 선행되어야 한다. 본 연구에서는 UHV-ECR-PECVD 법을 이용하여 H2로 희석된 SiH4로부터 a-Si:H과 $\mu$c-Si:H를 증착하였다. 그림 1은 SiH4 20sccm/H2 50sccm/25$0^{\circ}C$에서 기판의 DC bias를 변화시키면서 박막을 증착시킬 때 나타나는 박막의 구조 변화를 raman spectrum의 To phonon peak의 위치와 반가폭의 변화로 나타낸 것이다. 비정질 실리콘 박막은 DC bias를 증가시킴에 따라 무질서도가 증가하다가 어떤 critical DC bias에서 최대치를 이룬후 다시 질서도가 증가한다. 이온의 충격력에 의해 박막내에 응력이 축적되면 박막의 에너지 상태가 높아지고 이 축적된 응력이 ordering에 대한 에너지 장벽을 넘을 수 있을 만큼 커지게 되면 응력이 풀리면서 ordering이 가능해지는 것으로 생각된다. 그림 2는 수소 결합 형태의 변화이다. 박막의 무질서도가 증가할 경우 알려진 바와 같이 2000cm-1근처의 peak은 감소하고 2100cm-1 부근이 peak이 증가하는 현상을 보였다. 본 논문에서는 여러 공정 변수, 특히 DC bias에 따르는 박막의 구조 변화와 다른 성장 조건(온도, 유량비)이 critical DC bias나 결정화, 결정성 등에 미치는 영향에 대한 분석결과를 보고하고자 한다.등을 이용하여 광학적 밴드갭, 광흡수 계수, Tauc Plot, 그리고 파장대별 빛의 투과도의 변화를 분석하였으며 각 변수가 변화함에 따라 광학적 밴드갭의 변화를 정량적으로 조사함으로써 분자결합상태와 밴드갭과 광 흡수 계수간의상관관계를 규명하였고, 각 변수에 따른 표면의 조도를 확인하였다. 비정질 Si1-xCx 박막을 증착하여 특성을 분석한 결과 성장된 박막의 성장률은 Carbonfid의 증가에 따라 다른 성장특성을 보였고, Silcne(SiH4) 가스량의 감소와 함께 박막의 성장률이 둔화됨을 볼 수 있다. 또한 Silane 가스량이 적어지는 영역에서는 가스량의 감소에 의해 성장속도가 둔화됨을 볼 수 있다. 또한 Silane 가스량이 적어지는 영역에서는 가스량의 감소에 의해 성장속도가 줄어들어 성장률이 Silane가스량에 의해 지배됨을 볼 수 있다. UV-VIS spectrophotometer에 의한 비정질 SiC 박막의 투과도와 파장과의 관계에 있어 유리를 기판으로 사용했으므로 유리의투과도를 감안했으며, 유리에 대한 상대적인 비율 관계로 투과도를 나타냈었다. 또한 비저질 SiC 박막의 흡수계수는 Ellipsometry에 의해 측정된 Δ과 Ψ값을 이용하여 시뮬레이션한 결과로 비정질 SiC 박막의 두께를 이용하여 구하였다. 또한 Tauc Plot을 통해 박막의 optical band gap을 2.6~3.7eV로 조절할 수 있었다. 20$0^{\circ}C$이상으로 증가시켜도 광투과율은 큰 변화를 나타내지 않았다.부터 전분-지질복합제의 형성 촉진이 시사되었다.이것으로 인하여 호화억제에 의한 노화 방지효과가 기대되었지만 실제로 빵의 노화는 현저히 진행되었다. 이것은 quinua 대체량 증가에 따른 반죽의 안정성이 저하되어 버린 것으로 생각되어진다. 더욱이 lipase를 첨가하면 반죽이 분화하는 경향이 보여졌지만 첨가량 75ppm에 있어서 상당히 비용적의 증대가 보였다. 이것은 lipase의 가수분해에 의해

• Proceedings of the Membrane Society of Korea Conference
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• 1992.10a
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• pp.39-40
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• 1992

분리막법이 기체 분리에 응용된후 에너지 소비의 절감, 열안전성 등과 같은 장점들로 인해 수소회수 및 $H_2/CO_2$의 비율조정, $CH_4/CO_2$ 분리, $O_2/N_2$의 분리 등에 이용되고 있다. 이러한 분리막의 특성은 투과도와 선택투과도에 의해 결정되어지는데, 이들은 서로 상반된 경향을 나타낸다. 즉 투과도가 높으면 선택투과도는 낮아지고, 선택투과도가 높으면 투과도는 감소하게 된다. 그러나 이러한 두가지 특성 모두를 높이기 위한 연구가 활발히 진행되고 있는데, 그 연구방향은 새로운 고분자의 합성 및 고분자의 개질, 복합재료의 개발, 액정, 촉진수송법 등으로 나눠질 수 있다. 이중 촉진수송이란 특정한 기체와 가역적 친화력 또는 흡착력을 갖는 운반체를 액체나 고체막에 분산시켜 원하는 특정 기체만을 선택택으로 수송하는 것을 말한다.