• Title/Summary/Keyword: permeability of membrane

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Preparation of Pore-filled Anion-exchange Membrane with PVDF and Poly(vinylbenzylchloride)

  • Park, Byungkyu;Byungpyo Hong;Kwangsoo Yu;Hongsik Byun
    • Proceedings of the Membrane Society of Korea Conference
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    • 2004.05a
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    • pp.207-210
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    • 2004
  • The pore-filled anion-exchange membranes were prepared in this study with an asymmetric poly(vinylidene fluoride)(PVDF) membrane as a nascent membrane and poly(vinylbenzyl chloride)(PVBCl) as a polyelectrolyte. The solution of PVBCI having the chloromethylate aryl ring of 80 percents and 1,4-diaminobicyclo [2,2,2]octane(DABCO) was made with the solvent of tetrahydrofuran(THF) and N,N-Dimethylformamide(DMF), which is in the rotio of 8:2. A new preparation method in this study, i.e. in-situ crosslinking, enabled us to produce the pore-filled membranes without change of size, and to control the properties of final membrane with various degree of cross-linking. From the result of surface morphologies of SEM and AFM the polyelectrolyte exists in the pores of nascent membrane as a certain configuration. From the investigation of the solvent affecting much to the permeability and rejection, it was found. that the membranes using DMF and THF showed better performances than the membranes produced by THF only. The water permeability of the final membrane at low pressure(100㎪) showed a typical ultrafiltation membrane's permeability (8-10kg/㎡hr) and good values of rejection(55∼60 percent).

Synthesis and Characterization of Alumina Composite Membrane by Al Evaporation and Thermal Oxidation (알루미늄의 진공증발과 열산화에 의한 알루미나 복합분리막의 제조 및 특성분석)

  • 이동호;최두진;현상훈
    • Journal of the Korean Ceramic Society
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    • v.32 no.3
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    • pp.349-358
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    • 1995
  • The ceramic composite membrane was synthesized by thermal oxidation after evaporation of Al on the support prepared by slip casting process. Oxidation was performed at $700^{\circ}C$ and 80$0^{\circ}C$ under dry oxygen atmosphere. It was considered as optimum oxidation condition that the membrane showed a knudsen behaviro. A further oxidation resulted in an increase of gas permeability because top layer became densified. Then, a multi-layered composite membrane was synthesized through a sol-gel method, evaporation and thermal oxidation of Al coating processes. While the membrane was thermally stable up to 80$0^{\circ}C$, gas permeability was rapidly decreased even at a slight amount of deposition of Al.

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Preparation and Oxygen Permeability of True-IPN's based on Silicone Rubber and Polystyrene (실리콘 고무와 폴리스틸렌을 이용한 True-IPNs의 제조 및 산소투과 특성)

  • Kim, Jun-Hyun;Byun, Hong-Sik
    • Membrane Journal
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    • v.10 no.4
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    • pp.205-212
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    • 2000
  • The true-lPN's based on silicone rubber(SR)rrubbery polymer) and polystyrenc(PS)(glass polymer) were prepared by using the sequential IP!\' method_ The characteristic of permeability of oxygen/nitrogen was investigated with the control of the amount of PSOO-70 wt%) in the true-lPN, As a results of fTlR and N1Vm. the SRIPS membrane was synthesised successfully with the IPN synthetic method, Thermal analysis resulls indicated that the degree of mixing of IPN increased with increase of the amount of PS in the IPN. Regarding the characteristic of gas permeability, the membrane showed a trend of decrease in oxygen permeability as the PS content increased, The oxygen permeability of membrane having 50 wt% of PS. however, increased momentarily, Selectivity, meanwhile, increased slightly as the contents of I'S increased. However, the maximum value of oxygen selectivity, which is 20.6% enhanced Value, was obtained with the membrane containing 50 wt% of PS. This can be explained that the behavior of lPN, i.e. mutual assistance, is pronounced in the membrane having 50 wt% of PS.

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Differential Effect of Harmalol and Deprenyl on Dopamine-Induced Mitochondrial Membrane Permeability Change in PC12 Cells

  • Lee, Chung-Soo
    • Biomolecules & Therapeutics
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    • v.12 no.1
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    • pp.9-18
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    • 2004
  • Opening of the mitochondrial permeability transition pore has been recognized to be involved in cell death. The present study investigated the effect of ${\beta}$-carbolines (harmaline and harmalol) and deprenyl on the dopamine-induced change in the mitochondrial membrane permeability and cell death in differentiated PC12 cells. Cell death due to 250 4{\mu}$M dopamine was inhibited by caspase inhibitors (z-IETD.fmk, z-LEHD.fmk and z-DQMD.fmk) and antioxidants (N-acetylcysteine, ascorbate, superoxide dismutase, catalase and carboxy-PTIO). ${\beta}$-Carbolines prevented the dopamine-induced cell death in PCl2 cells, while deprenyl did not inhibit cell death. ${\beta}$-Carbolines decreased the condensation and fragmentation of nuclei caused by dopamine in PC12 cells. ${\beta}$-Carbolines inhibited the decrease in mitochondrial transmembrane potential, cytochrome c release, formation of reactive oxygen species and depletion of GSH caused by dopamine in PC12 cells, whereas deprenyl did not decrease dopamine-induced mitochondrial damage. ${\beta}$-Carbolines, deprenyl and antioxidants depressed the formation of nitric oxide and melanin in dopamine-treated PC12 cells. The results suggest that cell death due to dopamine PC12 cells is mediated by caspase-8, -9 and -3. Unlike deprenyl, ${\beta}$-carbolines may attenuate the dopamineinduced cell death in PC12 cells by suppressing change in the mitochondrial membrane permeability through inhibition of the toxic action of reactive oxygen and nitrogen species.

Poly(ether block amide) (PEBA) Based Membranes for Carbon Dioxide Separation (이산화탄소 분리를 위한 PEBA공중합체 기반 분리막)

  • Lee, Jae Hun;Patel, Rajkumar
    • Membrane Journal
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    • v.29 no.1
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    • pp.1-10
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    • 2019
  • Poly(ether block amide) (PEBA) is one of the commercially important class of block copolymer very much suitable specifically for $CO_2$ separation. Gas separation membrane need to have good mechanical strength as well as high gas permeability. The crystalline polyamide (PA) block provides the mechanical strength while the rubbery polyether (PE) group being $CO_2$-philic facilitate $CO_2$ permeation though the membrane. Composition of thermoplastic and rubbery phase in the polymer are changed to fit into suitable gas separation application. Although PEBA has good permeability, the selectivity of the membrane can be enhanced by incorporating molecular sieve without affection much the gas permeability. Mixed matrix membrane (MMM), a class of composite membrane combine the advantage of polymer matrix with the inorganic fillers. However, there are some disadvantages based on the compatibility of the inorganic fillers and polymeric phase. This review covers both the advantage and limitations of PEBA block copolymer based composite membrane.

Effect of Nonsolvent and Metal Salt Concentration on Oxygen Separation Performances of Polycarbonate/Metal Salt Membrane (Polycarbonate/Metal Salt 막의 산소분리특성에 미치는 비용매와 금속염 농도의 영향)

  • Seo, Sang-Hun;Lee, Woo-Tai
    • Journal of the Korean Society of Industry Convergence
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    • v.4 no.1
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    • pp.61-69
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    • 2001
  • Polycarbonate(PC) membranes for oxygen enrichment from air were prepared by the wet phase inversion method. In order to improve oxygen separation performances of the PC membrane, the effect of the added ethanol(nonsolvent) and $CuCl_2$(metal salt) concentration in the casting solution on morphology, oxygen permeability ami $O_2/N_2$ separation factor of the membrane was studied. In addition, tensile strength and elongation at break of the membrane were investigated. An asymmetric membrane with a dense top layer and a porous sublayer was obtained. The thickness of the dense top layer decreased with increasing amount of nonsolvent additive. Compared with pure PC membrane without additive(metal salt), the oxygen permeability and $O_2/N_2$ separation factor of the $PC/CuCl_2$ membrane are significantly improved. The oxygen permeability and $O_2/N_2$ separation factor is $5.25{\times}10^{-9}cm^3(STP){\cdot}cm/cm^2{\cdot}sec{\cdot}cmHg$ and 4.5, respectively. This improvement might be due to good interaction between metal salt and oxygen.

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Accumulation of Food Wastes Liquid Fertilizer using Reverse Osmosis Membrane System (역삼투막을 이용한 음식폐기물 액비의 농축)

  • Cha, Gi-Cheol;Hwang, Myoung-Goo;Lee, Myung-Gyu;Tae, Min-Ho
    • Journal of Korean Society on Water Environment
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    • v.18 no.2
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    • pp.159-168
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    • 2002
  • A lab-scale Reverse Osmosis(RO) membrane reactor was installed to investigate the membrane permeability, characteristics of membrane fouling at each conditions, and performance of elimination at different trans-membrane pressure(TMP) in the liquid fertilizer accumulated system. Experimental setup was divided to three different TMP conditions. As a result of experiment, permeability of RO membrane was proportional to the increase of TMP and temperature. After experiment was completed, two types chemical cleaning(remove the organic foulant and inorganic foulant) was done, and recover rate of permeability was each 99.8, 99.7 and 99.7%, respectively. From this experimental data, membrane fouling could be determined that the most of it was recoverable in this system, and major reason of fouling was concentration polarization. Elimination rate of solute substance in the liquid fertilizer indicated very stable(above 99%), except ammonia nitrogen, and the most stable elimination rate was investigated at the highest TMP condition (Run 3).

Experimental Study of Water Penetration Rate Via Graphene Oxide Membrane According to Driven Pressure Difference (산화 그래핀 맴브레인의 물투과 속도와 차압 조건 간 상관관계에 대한 실험적 연구)

  • Kim, Ji-Min
    • Journal of the Korean Society of Mechanical Technology
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    • v.20 no.6
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    • pp.858-864
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    • 2018
  • Graphene oxide (GO) laminate is a new promising material for water purification system, which has extraordinary permeability only for water molecule. It consists of numerous nano-channels, in which water molecules could be nano-confined, resulting in slip of the molecules for very fast transportation speed. In this study, water penetration rate via different thickness of GO membrane according to driven pressures are measured experimentally, so that speed of water molecules and permeability are evaluated. Generally, water penetration rate via a membrane with macroscopic-sized channel increases linearly with pressure difference between up and bottom side of the membrane, but that via GO membrane approaches asymptotic value (i.e. saturation) as like a log function. Moreover, the permeability of GO membrane was observed in inverse proportion to its thickness. Based on the experimental observations, a correlation for volume flux via GO membrane was suggested with respect to its thickness and external pressure difference.

Separation of Aqueous Ethanol Solution Using a PAA-PAN Composite Membrane Through Pervaporation (PAA-PAN 복합막을 이용한 에탄올 수용액의 투과증발 분리)

  • 원장묵;하백현;최호상
    • Membrane Journal
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    • v.6 no.3
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    • pp.182-187
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    • 1996
  • Hydrophilic poly(acrylonitrile) [PAN] membrane with good molecular weight cut-off characteristics were prepared by using the phase inversion method. Permeability and molecular weight cut-off of the membranes were measured through the ultrafiltration test. On the surface of the PAN support membranes, poly(acrylic acid) [PAA] was deposited by dip-coating. The water permeability of the PAN support membrane had $0.17~31\textrm{mm}^3/m^{2} \cdot s \cdot Pa$, the molecular weight cut-off 42, 000~150, 000. The transport characteristics of the prepared composite membranes were significantly affected by the variation of the support membrane mophology. The permeability of the composite membrane was decreased with increasing molecular weight cut-off of the support membrane, and the separation factor was slightly changed depending on the feed concentration.

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Application of Molecular Simulation Techniques to Estimation of Gas Permeability in Zeolite Membranes

  • Takaba, Hiromitsu;Yamamoto, Atsushi;Nakao, Shin-Ichi
    • Proceedings of the Membrane Society of Korea Conference
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    • 2004.05a
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    • pp.33-38
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    • 2004
  • Molecular modeling of gas permeation through zeolite membranes with/without intercrystalline region was carried out. Molecular dynamics (MD) and Monte Carlo (MC) simulations were performed to estimate the diffusion coefficient and adsorption parameters respectively, and our proposed combined method of molecular simulation techniques with a permeation theory (CMP) was used to estimate gas permeability. The calculated permeability of gases (Ar, He, Ne, $N_2$, $0_2$, $CH_4$) at 301 K for the single crystal membrane model was about one order of magnitude larger than the experiential values, although the dependence on the molecular weight of the permeating species agreed with experiments. On the other hand, the estimated permeability using the diffusivity and adsorption parameters of the intercrystalline region model was in good agreement with the experiments. The consistency between experiments and the estimated values means the importance of considering the intercrystalline region and the validity of CMP method to predict the performance of zeolite membranes.

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