• 제목/요약/키워드: supported membrane

검색결과 208건 처리시간 0.039초

Extraction/Separations of Cobalt by Supported Liquid Membrane: A Review

  • Swain, Basudev;Shim, Hyun-Woo;Lee, Chan Gi
    • Korean Chemical Engineering Research
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    • 제57권3호
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    • pp.313-320
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    • 2019
  • Extraction/separation of cobalt by supported liquid membrane has been reviewed. The review discusses various directions associated with the supported liquid membrane process, such as the kind of supported liquid membrane, the principle of supported liquid membrane, transport mechanism involved, and the advantages and disadvantages of the supported liquid. Finally, extraction and separation of cobalt from other metals using extractant through supported liquid membrane have been reviewed. Separation of cobalt using various reagents and cobalt recovery from scrap using commercial extractant can be a potential perspective from the application of supported liquid membrane application.

Change of Phase Transformation Temperature at Fabricated Membrane using Sol-gel Method

  • Cheong, Hun;Choi, Duck-Kyun;Cheong, Deock-Soo
    • 한국세라믹학회지
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    • 제38권10호
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    • pp.876-880
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    • 2001
  • The supported and unsupported boehmite ($\gamma$-AlOOH) membranes were prepared using a boehmite sol. The supported membrane was consisted of a porcelain support, two intermediate $\alpha-{Al_2}{O_3}$ layers, and a top boehmite membrane. XRD patterns showed that the supported top membrane had a higher $\theta-$ to $\alpha-{Al_2}{O_3}$ transformation temperature compared to the unsupported membrane. This result was also confirmed from microstructural study of the membrane. The shift in the phase transformation temperature should be explained by difference of a stress generated in the supported top membrane due to interaction between the support layers and the top membrane.

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Studies on the Macrocycle-mediated Transport of Divalent Metal Ions in a Supported Liquid Membrane System

  • 조문환;신상철
    • Bulletin of the Korean Chemical Society
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    • 제16권1호
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    • pp.33-36
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    • 1995
  • Macrocyclic ligands have been studied as cation carriers in a supported liquid membrane system. Cd2+ has been transported using nitrogen substituted macrocycles as carriers and several divalent metal ions (M2+=Zn, Co, Ni, Cu, Pb, Mg, Ca, and Sr) have been transported using DBN3O2, DBN2O2and PolyNtnoen as carriers in a supported liquid membrane system. Competitive Cd2+-M2+ transport studies have also been carried out with the same system. Ligand structure, stability constant, membrane solvent and carrier concentration are also important parameters in the transport of metal ions.

A Stable Supported Liquid membrane Composed of Polypropylene Glycol and Tributyl Phosphate for Phenol Separation from Aqueous Solution

  • Ahn, Hyo-Seong;Lee, Yong-Taek;Kim, Myung-Soo
    • Korean Membrane Journal
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    • 제1권1호
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    • pp.81-85
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    • 1999
  • Tributyl phyosphate(TBP) polypropylene glycol 4000(PPG-4000) and the mixture of two compounds were examined as a liquid membrane in a supported liquid membrane (SLM) to separate phenol from aqueous solution.The feed concentration of phenol was varied in a broad range from 500 mg/L to 5000 mg/L and different types of liquid membrane were prepared to elucidate their effects on separation of phenol. It was found that the modified PPG 4000 with TBP and toluene diisocyanate(TDI) might be used as a proper liquid membrane because the mass transfer rate examined with this membrane was higher than that through methyl isobutyl ketone (MIBK) which has been used as a conventional solvent in a solvent extraction process. The breakthrough pressure of the SLM is defined to be the pressure difference across the membrane at which the supported liquid membrane is not kept in the pores any more. it indicates how the SLM is stable., It was found that the breakthrough pressure of the modified PPG-4000 was much higher than those of typical organic solvents.

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Recent progress in supported liquid membrane technology: stabilization and feasible applications

  • Molinari, Raffaele;Argurio, Pietro
    • Membrane and Water Treatment
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    • 제2권4호
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    • pp.207-223
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    • 2011
  • Supported Liquid Membranes (SLMs) have been widely studied as feasible alternative to traditional processes for separation and purification of various chemicals both from aqueous and organic matrices. This technique offers various advantages like active transport, possibility to use expensive extractants, high selectivity, low energy requirements and minimization of chemical additives. SLMs are not yet used at large scale in industrial applications, because of the low stability. In the present paper, after a brief overview of the state of the art of SLM technology the facilitated transport mechanisms of SLM based separation is described, also introducing the small and the big carrousel models, which are employed for transport modeling. The main operating parameters (selectivity, flux and permeability) are introduced. The problems related to system stabilization are also discussed, giving particular attention to the influence of membrane materials (solid membrane support and organic liquid membrane (LM) phase). Various approaches proposed in literature to enhance SLM stability are also reviewed. Modification of the solid membrane support, creating an additional layer on membrane surface, which acts as a barrier to LM phase loss, increases system stability, but the membrane permeability, and then the flux, decrease. Stagnant Sandwich Liquid Membrane (SSwLM), an implementation of the SLM system, results in both high flux and stability compared to SLM. Finally, possible large scale applications of SLMs are also reviewed, evidencing that if the LM separation process is opportunely carried out (no production of byproducts), it can be considered as a green process.

Recovery of Levafix brilliant red E-4BA and Levafix brilliant red E-6BA from aqueous solution by supported liquid membrane

  • Muthuraman, G.;Sathya, M.;Soniya, M.;Elumalai, S.
    • Membrane and Water Treatment
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    • 제4권4호
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    • pp.277-291
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    • 2013
  • The transport and recovery of Levafix brilliant red E-4BA and Levafix brilliant red E-6BA were investigated using polytetrafluoroethylene (PTFE) fiber based supported liquid membrane containing tetra butyl ammonium bromide (TBAB) in coconut oil as a carrier. The influencing parameters studied are: pH of the feed solution, concentration of dye in the feed solution, extractant concentration, and various kind of stripping agent, rate of stirring, time of transport, reusability of membrane and stability of membrane. Increase in TBAB concentration inside the membrane enhances the flux with its maximum value at $1.553{\times}10^{-4}$ M TBAB. Further increase in the concentration of TBAB leads to decreased rate of transport due to increase in viscosity of membrane liquid. The optimum conditions for dye transport are: pH of feed ($7{\pm}0.1$), $1.553{\times}10^{-4}$ M extractant concentration, 350 rpm for stirring, $4.9{\times}10^{-1}$ M potassium hydrogen phthalate as a stripping solution, the time of transport 6 h. It was noticed that flux values were increased with increasing dye concentration in the feed phase. Applying this study to textile wastewater, dyes were transported up to 98% in 6 h. This recovery technique is rewarding to environment and economic.

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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이산화탄소 분리를 위한 이온성액체 지지분리막의 제조 (Supported Ionic Liquid Membrane Preparation for Carbon Dioxide Separation)

  • 최미영;정건용
    • 멤브레인
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    • 제22권4호
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    • pp.280-283
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    • 2012
  • 본 연구는 이산화탄소를 효율적으로 분리하기 위한 이온성액체 지지분리막 제조를 목적으로 한다. 공칭크기 0.1 ${\mu}m$ PVDF 정밀여과막에 이온성액체인 [bmim][${PF_6}^-$] (1-butyl-3-methylimidazolium hexafluorophosphate)를 분리막 세공내로 흡입시켜 고정화하였다. 제조된 이온성액체 지지막에 대한 $N_2$, $H_2$, $CO_2$ 기체의 투과도는 0.075, 0.203, 1.380 GPU로 측정되었으며 $CO_2/N_2$, $H_2/N_2$의 선택도는 각각 14.2와 2.69이었다. 또한 이온성액체 지지분리막은 이온성 액체가 운전압력 2.0 bar까지 세공 내에 고정되어 안정적으로 운전 가능하였다.

Numerical analysis of simply supported two-way reinforced concrete slabs under fire

  • Wenjun Wang;Binhui Jiang;Fa-xing Ding;Zhiwu Yu
    • Computers and Concrete
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    • 제31권6호
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    • pp.469-484
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    • 2023
  • The response mechanism of simply supported two-way reinforced concrete (RC) slabs under fire was numerically studied from the view of stress redistribution using the finite element software ABAQUS. Results show that: (1) Simply supported two-way RC slabs undergo intense stress redistribution, and their responses show four stages, namely elastic, elastic-plastic, plastic and tensile membrane stages. There is no cracking in the fire area of the slabs until the tensile membrane stage. (2) The inverted arch effect and tensile membrane effect improve the fire resistance of the two-way slabs. When the deflection is L/20, the slab is in an inverted arch effect state, and the slab still has a good deflection reserve. The deformation rate of the slab in the tensile membrane stage is smaller than that in the elastic-plastic and plastic stages. (3) Fire resistance of square slabs is better than that of rectangular slabs. Besides, increasing the reinforcement ratio or slab thickness improves the fire resistance of the slabs. However, an increase of cover thickness has little effect on the fire resistance of two-way slabs. (4) Compared with one-way slabs, the time for two-way slabs to enter the plastic and tensile cracking stage is postponed, and the deformation rate in the plastic and tensile cracking stage is also slowed down. (5) The simply supported two-way RC slabs can satisfy with the requirements of a class I fire resistance rating of 90 min without additional fire protection.