• Membrane Journal
• /
• v.23 no.6
• /
• pp.450-459
• /
• 2013

2,3,5,6-Tetramethyl-1,4-phenylenediamine (TMPD) based polyimide (PI) were crosslinked with 1,2-Diaminoethane (DAE) and 1,6-Diaminohexane (DAH) to enhance gas transport properties. Fourier transform infrared (FT-IR) studies show that imide groups were converted into amide groups during crosslinking process. Thermogravimetric analysis (TGA) results indicate that the degradation temperature of crosslinked PI membranes decreased after crosslinking. This is due to degradation of alkyl group in crosslinking agent. The d-space of crosslinked PI membranes decreased with increasing crosslinking time. The ideal permeability for $CH_4$, $N_2$, $O_2$, and $CO_2$ decreased after crosslinking and the ideal permeability of crosslinked PI membranes induced by DAH is larger than that by DAE. In contrast, the permselectivity of $CO_2/CH_4$, $CO_2/N_2$ and $O_2/N_2$ increased during crosslinking. For the gas pair of $CO_2/CH_4$, the maximum increment is about 39.5% after 6 minutes of DAE crosslinking. Also, that of $O_2/N_2$ gas pair is about 20.5% after 6 minutes of DAE crosslinking. According to these result, DAE is more suitable for enhanced permselectivity than DAH. On the contrary, DAE is not useful for $CO_2/N_2$ separation due to reduction in $CO_2/N_2$ permselectivity after 3 minutes DAE crosslinking.

• Applied Chemistry for Engineering
• /
• v.18 no.5
• /
• pp.483-489
• /
• 2007

Polyaniline (PANI)/Polyimide (PI) membranes were prepared and the effects of PANI contents and doping on the structural properties and gas separation properties were studied. The polyamic acid (PAA) solution was prepared by the polycondensation reaction of 4,4'-(hexafluoroisopropylidene) diphthalic anhydride (6FDA) and 4,4'-oxydianiline (ODA) in 1-methyl-2-pyrrolydinone (NMP) solvent. The PANI/PI blends were obtained by mixing PAA solution and PANI solution, and were doped with 1 M aqueous HCl solution for 24 h. The structural characterizations of the as-cast and doped membranes were examined by FT-IR, XRD, and TGA. The gas permeation experiments with $H_2$, $CO_2$, $O_2$, $N_2$, and $CH_4$ were carried out by variable pressure method at $30^{\circ}C$ and 5 atm. For all gases tested, the permeability coefficients of the blends decreased with increasing PANI content and the magnitude of permeability was in the order of $H_2$ > $CO_2$ > $O_2$ > $N_2$ > $CH_4$. The permeability for PANI/PI membranes decreased after the doping process while the permselectivity increased. For $H_2/CH_4$ separation, the doped PANI/PI (75/25) membrane has a permselectivity of 991.

• Elastomers and Composites
• /
• v.40 no.2
• /
• pp.136-142
• /
• 2005

Liquid crystalline poly(allylsulfone) networks having $SO_2$ in a main chain and mesogens in a side chain were synthesized and their gas permeability and permselectivity were determined. The monomer II having two allyl groups on the each end group was able to form polymer networks by polymerization reaction, while the monomer I having only one allyl group was not. Molecular motion of the poly(allylsulfone) networks were retarded with increasing the cross-linking density, and the segmental motion of networks was developed enough to show isotropic phase transition. Gas permeabilities of poly(II-5 $01/I-OCH_3$ 99) were 2.58 baller for $O_2$ and 18.4 barrer for $H_2$. It means that hydrogen gas are 7 times more permeable than oxygen. Its permselectivities were high as 23.9 for ${\alpha}(H_2/N_2)$. The permselectivity was increased with increasing the cross-linking density. For example, ${\alpha}(H_2/N_2)$ was 36.8 in poly(II-5 $10/I-OCH_3$ 90), which was shown to be the highest value among these poly(allylsulfone) networks.

• Proceedings of the Korean Society of Applied Pharmacology
• /
• 1992.05a
• /
• pp.62-62
• /
• 1992

1.이온토포레시스에 의한 ISP의 경피촙수증가는 단순투과의 약 13배로서 그 증가정도는 전류세기와 약물농도에 비례하였다. 2. 가해주는 $Na^{＋}$ 농도가 커질수록 ISP의 flux는 감소하였다. 3. ion-pairing agent률 가하면 ISP의 flux는 감소하는데, 그 감소정도는 TU>SAL>BEN 로서 이는 이 물질들이 ISP와 ion-pair를 형성하는 능력순서와 같았다. 4. ISP용액의 pH증가시 ISP의 flux는 대체적으로 증가하며 그 pattern은 피부의 pKa를 3.5로 가정할 때의 피부해리곡선과 유사하였다. ISP가 광범위한 pH에서 완벽하게 해리된다고 가정할 때 pH증가시 flux증가는 피부해리 증가에 따른 permselectivity 증가에 기인한 것으로 생각되었다.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1994.04a
• /
• pp.33-33
• /
• 1994

세라믹 막을 이용한 정밀여과 (microfiltration)나 한외여과(ultrafiltration)에 있어서 가장 중요한 점은 높은 선택적 투과성(permselectivity)을 유지하면서도 투과량(permeation flux)이 각각 500 ~ 1000 $l/m^2.hr$와 30 ~ 100 $l/m^2.hr$ 정도로 상당히 높아야 한다. 기체분리 공정에서도 마찬가지로 높은 투과성이 요구되기 때문에 이상과 같은 고투과량을 갖는 복층 세라믹막의 제조방법과 투과특성에 대한 연구를 수행하였다.

• Proceedings of the Korean Society of Applied Pharmacology
• /
• 1993.04a
• /
• pp.179-179
• /
• 1993

1. PS및 CP의 flux는 전류의 새기 및 donor의 약물농도에 비래하였다. 2. pH의 flux는 pH가 증가할수록 증가하였으나, CP(pKa=9.2)의 flux는 pH=2에서 최대치를 보였다. 이는 약물의 해리 정도와 H$^{＋}$이온의 mobility, 또 피부의 permselectivity의 balance에 의해 결정된 것으로 생각된다. 3. donor cell에 NaCl을 첨가하면 두 약물 공히, 그러나 특히 PS의 flux가 저하되었다. 이는 두 약물의 이온과 $Na^{＋}$의 mobility차이에 기인한다고 생각된다. 4. PS의 경우 taurodeoxycholate(TDC)같은 음이온을 donor cell에 공존시키면 flux가 감소하였다. 이는 PS와 TDC가 전기적으로 중성인 ion-pair complex를 형성함으로써 PS이온의 유효농도가 감소하기 때문으로 생각된다.

• Journal of the Korean Ceramic Society
• /
• v.32 no.12
• /
• pp.1349-1356
• /
• 1995

The change of permeation mechanism from Knudsen diffusion to micropore diffusion was observed after CVD modification of an alumina-sol coated alumina support which was prepared by slip coating process. Permselectivities of He/N2, H2/N2, and CO2/N2 were 5.67, 5.02, and 1.44, respectively. These values were higher than those under Knudsen diffusion controlled region.

• Proceedings of the Membrane Society of Korea Conference
• /
• 2004.05b
• /
• pp.144-146
• /
• 2004

Various polymeric hollow fiber membranes have been prepared and been used widely due to their high surface area per unit volume and high permselectivity. However, the organic materials are only limited to mild operating conditions because of their weak thermal stability and ease of fouling.(omitted)

• Proceedings of the Membrane Society of Korea Conference
• /
• 2005.05a
• /
• pp.116-118
• /
• 2005

• Proceedings of the Membrane Society of Korea Conference
• /
• 2005.11a
• /
• pp.223-226
• /
• 2005