• 제목/요약/키워드: Supported liquid membrane

검색결과 40건 처리시간 0.026초

고정화 액막(BMIBF4/PVDF)에 의한 디플루오로-클오로메탄과 헥사플루오로프로필렌의 청정분리 (Clean Separation of Difluoromonochloromethane(R22)/Hexafluoropropylene(HFP) by Using Liquid-Supported Membrane(BMIBF4/PVDF))

  • 최평호;김철웅;김범식;이정민;구기갑
    • 청정기술
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    • 제9권4호
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    • pp.169-177
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    • 2003
  • 온도(0 to $30^{\circ}C$)와 압력(4 bar까지)의 함수로서 이온성액체인 buthylmethylimidazolium tetrafluoride ($BMIBF_4$)에 관한 디플루오로클로로메탄($CHCIF_2$, R22)과 헥사플루오로프로필렌($C_3F_6$, HFP) 가스의 용해도 실험을 실시하였는데, R227가스의 용해도는 온도가 낮거나, 압력이 증가할수록 거의 선형적으로 증가한 반면, HFP 가스는 거의 용해도를 나타내지 않았다. 이어서 이 이온성액체를 고분자지지체인 polyvinylidenefluoride(PVDF)에 함침량을 달리하여 액막을 제조하였으며, 일정한 압력(3 atm)에서 가스분리막 장치를 사용하여 액막의 이온성액체 함침량 변화와 조업온도의 함수로 R22, HFP 및 $N_2$ 가스의 투과특성 실험을 실시하였다. 실험결과, R22의 투과도는 주로 이온성액체의 함침량에 의존하여 급격히 증가하였으며, HFP 및 $N_2$의 투가도는 거의 0에 가까운 매우 낮은 값을 나타내었다. 또한 R22의 확산계수 및 용해도계수는 조업온도가 낮거나 액막에서 이온성액체의 함침량에 비례하여 증가하였다. 결과적으로 R22에 관한 HFP가스의 선택도는 조업온도와 액막의 이온성액체 함침량에 의존하여 10-45배 정도까지 매우 높은 값올 나타내었다.

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Separation of Cd(II) from Aqueous Solutions by A New Consecutive Process Consisting of Supported Liquid Membrane and Electrodialysis

  • Altin, Sureyya;Altin, Ahmet
    • Journal of Electrochemical Science and Technology
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    • 제10권1호
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    • pp.14-21
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    • 2019
  • Supported liquid membrane process usually is used for recovering or enrichment of valuable metals in the industrial wastewater. But, even if the metals in the wastewater was separated with high chemical selectivity, it cannot be enough concentrated since separation performance of supported liquid membrane (SLM) process is limited by concentration gradient between feed solution and stripping solution. If metal concentration in the stripping solution to be enough low, transport of metal through membrane can be accomplishment constantly. Therefore, Electrodialysis (ED) has been placed after SLM process and the stripping solution of SLM was used as the feed solution for the ED process. Transport of ions in the solutions is successfully performed by ED process. Thus, the metal concentration in the stripping solution does not rise as to stop ion transport. Besides, valuable metals easily are concentrated by ED process for re-use. In this study, effects of operation parameters like initial Cd(II) concentration, HCl concentration in the feed solution of SLM and applied voltage are investigated on separation efficiency, flux and permeability of the both processes. As the feed solution concentration increased, all performance values has increased. When initial concentration of 100 mg/L is used, separation performances (SP) are 55% and 70%, for SLM and consecutive process, respectively. The best HCl concentration in the feed solution of SLM has determined as 2 M, in this conditions SP are 64% and 72%, for SLM and consecutive process, respectively. With increased of applied voltage on ED process, SP of the consecutive process has been raised from 72% to 83%. According to the obtained experimental data, consecutive process has better separation performance than SLM. When the separation performances of both processes were compared for the same operating conditions, it was determined higher the separation efficiency, permeability and flux values of the consecutive process, 8%, 9% and %10.6, respectively. Consequently, the use of the consecutive process increases the performance efficiency of both processes. The consecutive process studied has quite a good chemical separation efficiency, and enrichment capability. Moreover, this process requires few water and energy.

Tri-n-butyl phosphate와 액상고분자 지지액막을 이용한 페놀의 분리 (Supported Liquid Membrane Composed of Tri-n-butyl Phosphate or Liquid Polymer for Phenol Separation)

  • 안효성;이용택;윤인주;김명수
    • 멤브레인
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    • 제8권4호
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    • pp.228-234
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    • 1998
  • 다양한 수질 오염원 중 페놀과 같은 유기화합물은 배출조건이 비정상적인 경우 기존의 처리방법으로 제거하거나 파괴하기 어렵다. 수용액으로부터 페놀을 분리하기 위한 최근의 연구들은 활성탄에 의한 흡착, 용매 추출 등에 의해 수행되어져 왔으며, 물-기름 유화에 기초를 둔 액막법이 기존의 기술들을 대체하기 위한 방법으로 시험되어져 왔다. 본 연구에서는 tri-n-butyl phosphate(TBP)와 액상 고분자를 지지액막의 액막용액으로 선정하여 수용액상의 페놀을 분리하였다. 공급측 페놀 농도를 변화시키고 다양한 액막용액을 사용하여 이들이 페놀분리에 미치는 효과를 연구하였다. TBP를 운반체로 사용한 경우의 실험결과들은 용매추출에서 주로 사용되고 있는 methyl isobutyl ketone(MIBK)보다 높은 물질전달속도를 보여주었으며, 선택한 액상고분자 중 polypropylene glycol 4000(PPG-4000), polybutylene glycol 500(PBG 500)의 경우 MIBK와 유사하거나 조금 높은 값을 나타내었다.

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Facilitated Transport of Cr(VI) through a Supported Liquid Membrane with a Carrier

  • Park, Sang-Wook;Lee, Jae-Wook;Kim, Sung-Soo;Choi, Byoung-Sik
    • 한국응용과학기술학회지
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    • 제20권2호
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    • pp.154-164
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    • 2003
  • This paper has applied a simple model to the mass transfer mechanism of Cr(VI) with crownether in a batch-type, supported liquid membrane module. Concentration at pH 3 are as follows : 0.012 kmol/$m^3{\le}$18-crown-6${\le}$0.036 kmol/$m^3$ and 20 g/$m^3{\le}$ Cr(VI)${\le}$500 g/$m^3$. The measured values of forward- and backward-reaction rate constants between Cr(VI) and 18-crown-6 were used to simulate the model with the mass conservation equation and associated boundary conditions. Comparison between the experimental and simulated facilitated factor of Cr(VI) transport led to classification of reaction regions.

PARTIAL OXIDATION OF PROPANE ON NAFION SUPPORTED CATALYTIC MEMBRANE

  • F. Frusteri;C. Espro;F. Arena;F. Arena;E. Passalacqua;A.Patti;A. Parmaliana
    • 한국막학회:학술대회논문집
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    • 한국막학회 1999년도 The 7th Summer Workshop of the Membrane Society of Korea
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    • pp.55-58
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    • 1999
  • Nafion supported catalytic membranes were found to be active, stable and selective in th partial oxidation of propane to oxygenates with H2O2 under mild condition. Addition of Fe2+ in liquid phase enhances the reaction rate. Reaction proceeds according to a radical mechanism based on th electrophilic activation of propane on superacid sites and subsequent reaction of the activated paraffin with OH radicals. The use of a catalytic membrane, which allow separation of the intermediate products from the liquid phase containing the oxidant, was found to be effective to perform selective partial oxidation of propane with high yields to oxygenated products.

Development of a Supported Emulsion Liquid Membrane System for Propionic Acid Separation in a Microgravity Environment

  • Li, Jin;Hu, Shih-Yao B.;Wiencek, John M.
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제6권6호
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    • pp.426-432
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    • 2001
  • Perstractive fermentation is a good way to increase the productivity of bioreactors. Us-ing Propionibacteria as the model system, the feasibility of using supported emulsion liquid mem-brane(SELM) fro perstractive fermentation is assessed in this study. Five industrial solvents were considered as the solvent for perparing the SELM. The more polar a solvent, is the higher the par-tition coefficeint However, toxicity of a solvent also increases with its polarity. CO-1055(indus-trial decanol/octanol blend)has the highest partition coefficient toward propionic acid among the solvents that has no molecular toxicity toward Propionibacteria, A preliminary extraction study was conducted using tetradecane as solvent in a hydrophobic hollow fiber contactor. The results confirmed that SELM eliminates the equilibrium limitation of conventional liquid-liquid extrac-tion and allows the use of a non-toxic solvent with low partition coefficient.

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캐리어 막에 의한 알카리 금속 이온의 업-힐 수송의 특성 연구 (Study of Characteristic of Up-hill Transport in Alkali Metal-ions Through a Carrier Membrane)

  • 박근덕;양원강
    • 분석과학
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    • 제12권3호
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    • pp.224-229
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    • 1999
  • 최근 캐리어를 이용한 액체막의 연구가 대단히 활발하다. 항생물질의 모넨신을 사용하여 옥타놀의 유기용매에 용해시켜 양이온교환막을 제조하였다. 이막의 평가를 Nernst-Planck식과 Fick식으로 막전위와 물질의 투과선택도를 분석하였다. 사용한 알카리이온의 농도에 대한 높은 투과선택성을 확인하였고, 시간에 따른 이온농도값은 선형관계를 알았다. 그러나 이온의 높은농도에서 변화량은 선형이 아니였다. 이를 위한 해석은 정지층(Stagnent Layer)을 하나 더 도입하여 업 - 힐 수송에서 직선관계를 얻었다.

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