• 제목/요약/키워드: Liquid membrane

검색결과 624건 처리시간 0.032초

Developing 500 MHz NB 19F-13C Double Resonance Solid-State NMR Probe for in-situ Analysis of Liquid Crystal Display Panels

  • Choi, Sung-Sub;Jung, Ji-Ho;Park, Yu-Geun;Park, Tae-Joon;Park, Gregory Hyung-Jin;Kim, Yong-Ae
    • Bulletin of the Korean Chemical Society
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    • 제33권5호
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    • pp.1577-1580
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    • 2012
  • The orientational and dynamic behavior of liquid crystal molecules on the alignment layer surfaces of liquid crystal display (LCD) devices is crucial to their performance, but there are only a few methods of experimentally elucidating the interactions between the liquid crystals and the alignment layers. Inspired by the natural and technical similarities between membrane proteins in lipid bilayers and liquid crystals in LCDs, we employed solid-state NMR methodologies originally developed for the study of membrane proteins in lipid bilayers for the in-situ analysis of liquid crystal display panels. In this article, we present a home-built 500 MHz narrowbore (NB) The orientational and dynamic behavior of liquid crystal molecules on the alignment layer surfaces of liquid crystal display (LCD) devices is crucial to their performance, but there are only a few methods of experimentally elucidating the interactions between the liquid crystals and the alignment layers. Inspired by the natural and technical similarities between membrane proteins in lipid bilayers and liquid crystals in LCDs, we employed solid-state NMR methodologies originally developed for the study of membrane proteins in lipid bilayers for the in-situ analysis of liquid crystal display panels. In this article, we present a home-built 500 MHz narrowbore (NB) $^{19}F-^{13}C$ double resonance solid-state NMR probe with a flat-square coil and the first application of this probe for the in-situ analysis of LCD panel samples. double resonance solid-state NMR probe with a flat-square coil and the first application of this probe for the in-situ analysis of LCD panel samples.

Liquid-liquid extraction process for gas separation from water in polymeric membrane: Mathematical modeling and simulation

  • Salimi, Nahid;Moradi, Sadegh;Fakhar, Afsaneh;Razavi, Seyed Mohammad Reza
    • Membrane and Water Treatment
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    • 제7권5호
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    • pp.463-476
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    • 2016
  • In this study, application of polypropylene hollow fiber membrane contactors for $CO_2$ removal from water in liquid-liquid extraction (LLE) mode was simulated. For this purpose, a steady state 2D mathematical model was developed. In this model axial and radial diffusion was considered to $CO_2$ permeation through the hollow fibers. $CO_2$ laden water is fed at a constant flow rate into the lumen side, permeated through the pores of membrane and at the end of this process, $CO_2$ solution in the lumen side was extracted by means of aqueous diethanolamine (DEA) and chemical reaction. The simulation results were validated with the experimental data and it was found a good agreement between them, which confirmed the reliability of the proposed model. Both simulation and experimental results confirmed the reduction in the percentage of $CO_2$ removal by increment of feed flow rate.

p-Dimethylaminobenzaldehyde, 1-Naphtol, Sulfosalicylic acid 등의 Carrier를 함유하는 H2O-CH2Cl2-H2O Liquid Membrane을 이용한 아미노산의 선택적 분리(II) (Selective Separation of Amino Acid Mixture Using H2O-CH2Cl2-H2O Liquid Membrane containing p-Dimethylaminobenzaldehyde, 1-Napthol and Sulfosalicylic acid as a Carrier (II))

  • 박정오;홍재진
    • 대한임상검사과학회지
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    • 제36권2호
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    • pp.115-120
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    • 2004
  • 혼합 amino acid의 선택적 분리를 위해 bulk liquid membrane system을 이용하였으며, p-diamethylaminobenzaldehyde(DAB), sulfosalicylic acid (SSA), 1-naphtol이 amino acid의 선택적 분리를 위한 효과적인 carrier로 사용될 수 있음을 확인하였다. 그 결과 sulfosalicylicacid에 대해서 Ala에 대한 선택성을 관찰할 수 있었으며, 1-naphtol에 대해서는 염기성 상태에서 Leu을 약산성 및 중성상태에서는 Val을 선택적으로 분리할 수 있었다. DAB에 대해서는 강산성에서 Phe을, 강알카리 조건에서 Ile를 선택적으로 분리할 수 있었다. Separation mechanism은 SSA와 1-naphtol의 경우에는 ion pair mechanism으로, DAB의 경우에는 imine 결합의 생성반응으로 설명할 수 있었다. 따라서, Liquid membrane을 이용한 생체시료 내의 아미노산을 선택적으로 분리함에 유용성이 클 것으로 사료된다.

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

  • 차기철;황명구;이명규;태민호
    • 한국물환경학회지
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    • 제18권2호
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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).

PET 부직포를 매트릭스로 이용한 Carrier-Facilitated Transport Membrane의 금속이온 투과성 (Selective Metal ion Transport of PET Non-woven Fabric Supported Carrier-Facilitated Transport Membrane)

  • 김용일;마석일
    • 한국섬유공학회:학술대회논문집
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    • 한국섬유공학회 2002년도 봄 학술발표회 논문집
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    • pp.462-465
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    • 2002
  • 물에 용해되어 있는 금속이온의 분리를 위한 선택성이 있는 분리 막의 개발은 환경오염이 날로 심각해지고 있는 오늘날에 환경오염의 개선, 에너지절약, 자원의 재활용 등 문제를 해결함에 있어서 아주 중요한 작용을 하게 될 것이다. 물에 용해되어 있는 금속이온을 선택적으로 분리하기 위해 일반적으로 캐리어(carrier)를 함유한 Carrier-Facilitated Transport Membrane (CFM)을 이용하게 되는데, 이 방면에 대한 연구는 주로 유기 상에 용해되어 있는 캐리어를 microporous한 필름에 지지하게 하는 방식으로 만들어진 Supported Liquid Membrane (SLM) 혹은 Elusion Liquid Membrance (ELM)의 개발에 대한 팽대한 연구가 이루어 졌다(1). (중략)

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막오염현상이 중공사정밀여과막의 물투과특성에 미치는 영향 (Influences of Membrane Fouling on Water Permeability of Hollow Fiber Microfiltration Membrane)

  • 김부길
    • 상하수도학회지
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    • 제10권3호
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    • pp.92-99
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    • 1996
  • The effects of membrane fouling on the water permeability were examined using the hollow fiber microfiltration (HMF)membrane. A membrane module with a pore size of 0.1 micron was submerged in the permeation tank and water bath. The applied pressure was 12.4 kPa for direct solid-liquid separation of activated sludge. As the concentration of MLSS(880~2180mg/l) of the feed solution increased, the decreasing rates of the water flux increased and the membrane was clogged more rapidly. The water flux through the membrane did not increase effectively even with the increase in the applied pressure(40.0~93.3kPa). When the membrane was cleaned with water, the recovery rate of water flux were larger for lower applied pressure. The results indicated that the process of direct solid-liquid separation using HMF membrane was effective at lower pressure.

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Pretreatment Process for Performance Improvement of SIES at Kori Unit 2 in Korea

  • Lee, Sang-Jin;Yang, Ho-Yeon;Shin, Sang-Woon;Song, Myung-Jae
    • 한국방사성폐기물학회:학술대회논문집
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    • 한국방사성폐기물학회 2004년도 Proceedings of the 4th Korea-China Joint Workshop on Nuclear Waste Management
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    • pp.12-27
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    • 2004
  • Pretreatment process consisted of submerged hollow-fiber microfiltration(HMF) membrane and spiral-wound nanofiltration(SNF) membrane has been developed by NETEC, KHNP for the purpose of improving the impurities of liquid radioactive waste before entering Selective Ion Exchange System(SIES). The lab-scale combined system was installed at Kori NPP #2 nuclear power plant and demonstration tests using actual liquid radioactive waste were carried out to verify the performance of the combined system. The submerged HMF membrane was adopted for removal of suspended solid in liquid radioactive waste and the SNF membrane was used for removal of particulate radioisotope such as, Ag-l10m and oily waste because ion exchange resin can not remove particulate radioisotopes. The liquid waste in Waste Holdup Tank (WHT) was processed with HMF and SNF membrane, and SIES. The initial SS concentration and total activity of actual waste were 38,000ppb and $1.534{\times}10_{-3}{\mu}Ci/cc$, respectively. The SS concentration and total activity of permeate were 30ppb and lower than LLD(Lower Limit of Detection), respectively.

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효소 고정화막의 응용에 대한 총설 (Zeolite Based Membrane for Removal of Ammonium: A Review)

  • 이주엽;라즈쿠마 파텔
    • 멤브레인
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    • 제32권3호
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    • pp.173-180
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    • 2022
  • 음용수 속 암모니아의 존재는 인간의 건강에 매우 해롭다. 농작물에서의 비료 사용, 산업 폐수, 화석 연료의 연소와 같은 활동으로 인해 가용성 암모니아는 지하수를 오염시킨다. 물에 존재하는 암모니아 농도가 낮더라도 해양생물 등의 수생환경을 훼손한다. 막 기술은 암모니아를 물로부터 효과적으로 제거하기 위한 매우 중요한 과정이다. 평평한 시트 막, 막 접촉기, 그리고 막 증류법은 암모니아를 제거하여 물을 정화하는 데 사용되는 방법들 중 하나이다. 막 접촉기는 막 증류법과는 달리 상변화 없이 액체와 가스 간의 또는 액체와 액체간의 질량 전달을 통해 암모니아를 제거하는 효율적인 공정이다. 다만 이 방법은 pH가 매우 높아 암모니아 제거에 비용이 많이 든다. 제올라이트는 우수한 이온 교환 능력을 가지고 있는데, 이는 암모니아와의 상호작용을 향상시켜 폐수로부터 흡착하는 능력을 향상시킨다. 제올라이트를 함유한 혼합 매트릭스 막은 암모니아 흡착 및 폐수로부터의 분리 효율을 향상시킨다. 이 리뷰에서는 위에서 소개된 내용이 자세히 논의될 것이다.

운반체 함침 유화액막에 의한 폐수중 크롬(VI)의 이동속도 (Tansport Rate of Chromium ion from Waste Water through the Liquid Surfactant Membrane Containing Carrier)

  • 우인성;김경호;이상진;강안수;최세영
    • Elastomers and Composites
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    • 제23권1호
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    • pp.11-17
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    • 1988
  • The transport of chromium(VI) ion from waste water through the liquid surfactant membrane containing tri-n-octylamine as a carrier, was analyzed by a slab model and was investigated through experiments. For the experiment of membrane stability, concentrations of surfactant and liquid paraffin oil were analyzed. Extraction experiments were carried out to observe the effect of system variables, such as concentrations of carrier, and initial chromium(VI) ion in external aqueous phase at $25^{\circ}C$. It is concluded that the most stable formation of liquid membrane emulsion was obtained when surfactant concentration is above 3 wt.% and liquid paraffin oil concentration is 50 vol.%. The theoretical equation on the transport of chromium(VI) ion agreed well with the experimental results.

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Separation and Concentration of L-Phenylalanine using a Supported Liquid Membrane

  • Jeong Woo Choi;Kyu
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제3권1호
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    • pp.24-31
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    • 1998
  • The separation and concentration of L-phenylalanine (L-Phe) using a supported liquid membrane (SLM) is investigated. A cation complex agent, di-2-ethylhexyl phosphoric acid (D2EHPA), is used as a carrier in the SLM with n-Heptane as a solvent. The reaction order and equilibrium constant in the formation reaction of L-phe-carrier complex are obtained from the extraction experiment. A mathematical model for a carrier mediated counter transport process is proposed to estimate the diffusion coefficient of L-phe-carrier complexly in the liquid membrant. Permeation experiments of L-phe using a SLM are performed under various operating conditions and optimum conditions for the transport of L-phe are obtained. Concentration of L-phe in the strip phase against its concentration is observed. Transport rate of glucose through liquid membrane is less than that of L-phe in the competitive transport of L-phe and glucose. And the existence of glucose reduced the transport rate of L-phe. The performance of separation with continuous strip phase is increased due to the dilution effect in the strip phase.

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