• 제목/요약/키워드: Bulk liquid membrane

검색결과 23건 처리시간 0.022초

Dibenzo-16-crown-5 Lariat Ether와 금속이온과의 착물형성에 관한 연구 (Thermodynamic Studies on Complexes for Dibenzo-16-crown-5 Sulfur Lariat Ether with Metal Ions)

  • 조문환;이상철;조재훈;김응태;이창환;최영섭;이종찬
    • 대한화학회지
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    • 제42권4호
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    • pp.443-448
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    • 1998
  • 용액열량계를 이용하여, 25$^{\circ}C$ 메탄올 용액에서 dibenzo-16-crown-5(DB16C5)의 유도체들과 금속이온과의 착물형성에 관한 열역학적인 파라미터인 log K, ${\Delta}H$, $T{\Delta}S$를 결정하고, dibenzo-16-crown-5의 유도체들을 운반체로 사용하여 벌크액체막과(bulk liquid membrane, BLM) 지지액체막(supported liquid membrane, SLM) 실험을 통하여 금속이온의 이동현상을 관찰하였다. BLM과 SLM에서 운반체로 DB16C5유도체를 사용했을 때 $Ag^+$ 이온이 많이 이동되었고 다른 금속이온들은 약간 이동된 것으로 관찰되었다. 액체막을 통한 그속이온의 이동에서 중요한 파라미터로 작용하는 인자는 리간드의 구조, 곁가지의 길이, 주개원자의 수와 종류, 안정도상수, 리간드의 농도 등을 들 수 있다.

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Heat and mass transfer analysis in air gap membrane distillation process for desalination

  • Pangarkar, Bhausaheb L.;Sane, Mukund G.
    • Membrane and Water Treatment
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    • 제2권3호
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    • pp.159-173
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    • 2011
  • The air gap membrane distillation (AGMD) process was applied for water desalination. The main objective of the present work was to study the heat and mass transfer mechanism of the process. The experiments were performed on a flat sheet module using aqueous NaCl solutions as a feed. The membrane employed was hydrophobic PTFE of pore size 0.22 ${\mu}m$. A mathematical model is proposed to evaluate the membrane mass transfer coefficient, thermal boundary layers' heat transfer coefficients, membrane / liquid interface temperatures and the temperature polarization coefficients. The mass transfer model was validated by the experimentally and fitted well with the combined Knudsen and molecular diffusion mechanism. The mass transfer coefficient increased with an increase in feed bulk temperature. The experimental parameters such as, feed temperature, 313 to 333 K, feed velocity, 0.8 to 1.8 m/s (turbulent flow region) were analyzed. The permeation fluxes increased with feed temperature and velocity. The effect of feed bulk temperature on the boundary layers' heat transfer coefficients was shown and fairly discussed. The temperature polarization coefficient increased with feed velocity and decreased with temperature. The values obtained were 0.56 to 0.82, indicating the effective heat transfer of the system. The fouling was observed during the 90 h experimental run in the application of natural ground water and seawater. The time dependent fouling resistance can be added in the total transport resistance.

Fundamental parameters of nanoporous filtration membranes

  • Wei Li;Xiaoxu Huang;Yongbin Zhang
    • Membrane and Water Treatment
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    • 제14권3호
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    • pp.115-120
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    • 2023
  • The design theory for nanoporous filtration membranes needs to be established. The present study shows that the performance and technical advancement of nanoporous filtration membranes are determined by the fundamental parameter I (in the unit Watt1/2) which is formulated as a function of the shear strength of the liquid-pore wall interface, the radius of the filtration pore, the membrane thickness, and the bulk dynamic viscosity of the flowing liquid. This parameter determines the critical power loss on a single filtration pore for initiating the wall slippage, which is important for the flux of the membrane. It also relates the membrane permeability to the power cost by the filtration pore. It is shown that for biological cellular membranes its values are on the scale 1.0E-8Watt1/2, for mono-layer graphene membranes its values are on the scale 1.0E-9Watt1/2, and for nanoporous membranes made of silica, silicon nitride or silicon carbonized its values are on the scale 1.0E-5Watt1/2. The scale of the value of this parameter directly measures the level of the performance of a nanoporous filtration membrane. The carbon nanotube membrane has the similar performance with biological cellular membranes, as it also has the value of I on the scale 1.0E-8Watt1/2.

(Allyloxy)methyl-Crown Ether를 이용한 액체막계에서의 Pd(Ⅱ) 및 Pb(Ⅱ)의 분리 (Separation of Pd(Ⅱ) and Pb(Ⅱ) Using (Allyloxy)methyl-Crown Ethers in a Bulk Liquid Membrane System)

  • 이용구;조현성;김태순;이동구;김응태;조문환;이영길;채영복
    • 대한화학회지
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    • 제41권9호
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    • pp.460-464
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    • 1997
  • (Allyloxy)methyl-Crown Ether를 액체막계에서 금속이온의 운반체로 사용하였다. 운반체로 사용한 AMDT18C6는 경쟁이동반응에서 Pd(II)를 선택적으로 분리하였으며 AM18C6는 Pb(II)의 선택성이 있었다. 거대고리리간드와 금속이온과의 착물형성에 관한 연구는 전위차법과 용액열량계법을 이용하였다.

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Selective Transport of Pb(II) Ion by Acyclic Polyethers Bearing Amide End-Groups

  • 김종승;이상철;김응태;조재훈;조문환;유재형;이종해
    • Bulletin of the Korean Chemical Society
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    • 제18권12호
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    • pp.1256-1260
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    • 1997
  • A series of acyclic polyethers bearing amide end-groups and lipophilic alkyl chains (3-5) were successfully synthesized with quantitative yields. Based upon the transport experiment in a bulk liquid membrane (BLM) system and solvent extraction, a very high selectivity of Pb2+ over other transition metal cations was observed. Measurement of thermodynamic parameters for complexation in methanol at 25 ℃ gave a strong evidence for excellent selective complexation for lead ion over other transition metal ions.

운반체로 $NtnOenH_4$$NdienOenH_4$를 포함한 액체막을 통한 전이금속 양이온의 운반속도 (Transport Rate of Transition Metal Cations through a Bulk Liquid Membrane Containing $NtnOenH_4$ and $NdienOenH_4$ as Carriers)

  • 김해중;장정호;신영국
    • 대한화학회지
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    • 제41권2호
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    • pp.77-81
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    • 1997
  • 거대고리 리간드인 1,12-diaza-3,4;9,10-dibenzo-5,8-dioxacyclopentadecane$(NtnOenH_4)$와 1,12,15-triaza-3,4;9,10-dibenzo-5,8-dioxacyclo-heptadecane$(NdienOenH_4)$를 운반체로 포함한 클로로포름 액체막을 통한 운반속도는 Ni(II)$({\Delta}Gp)$값을 구하여 본 결과, 운반속도의 순위는 전이금속 양이온들이 갖는 분배수화 자유에너지의 음의 값의 크기에 비례함을 알 수 있었다.

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Ag(Ⅰ) 이온 선택성을 갖는 거대고리 리간드: 벤질 치환기를 갖는 질소-산소 주개 거대고리 리간드의 착물 형성과 액체막 이동 현상 (Ag(Ⅰ) Ion Selective Macrocyclic Ligands: The Complexation and Liquid Membrane Transport Phenomena of Benzylated Nitrogen-Oxygen Donor Macrocyclic Ligands)

  • 김정;안태호;이명노;조문환;김시중
    • 대한화학회지
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    • 제43권2호
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    • pp.167-171
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    • 1999
  • 벤질 치환기를 포함하는 질소-산소 혼합 주개 거대고리 리간드와 Co(II), Ni(II), Cu(II), Zn(II), Cd(II), Pb(II) 그리고 Ag(I)와의 상호작용에 관한 연구를 수행하였다. 95% 메탄올 용액에서 각 착물의 안정도 상수를 전위차 적정법을 통해 결정하였으며 또한 이들 거대고리 리간드를 포함하는 액체막을 통하여 금속 이온의 이동을 조사하였다. 그 결과 Cu(II)와 Ag(I) 이온의 경우만 사용한 두 리간드와 안정한 착물을 형성하는 것으로 조사되었으며 액체막 이동 실험에서는 Ag(I) 이온의 선택적 이동이 일어남을 확인하였다.

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음식물 탈리액 처리를 위한 파일럿 규모의 막결합형 2상 혐기성 소화 공정 가능성 평가 (A feasibility study of a pilot scale two-phase anaerobic digestion with ultra filtration for the treatment of garbage leachate)

  • 이은영;허안희;김형국;김희준;배재호
    • 상하수도학회지
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    • 제23권5호
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    • pp.539-545
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    • 2009
  • A feasibility of a pilot scale two-phase anaerobic digestion with ultra filtration system treating garbage leachate were evaluated. The treatment system consisted of a thermophilic acidogenic reactor, a mesophilic methanogenic reactor, and an UF membrane. The average COD removal efficiency of the treatment system was 95% up to the OLR of 3.1 g COD/L/d. The higher COD removal efficiency with membrane unit resulted from the removal of some portion of soluble organics by membrane as well as particulate materials. When the membrane unit was in operation, bulk liquid in acidogenic and methanogenic reactors was partially interchanged, which maintained the acidogenic reactor pH over 5.0 without external chemical addition. Also, with the production of methane in the acidogenic reactor, the organic loading rate of the methanogenic reactor reduced. The initial flux of the membrane unit was $50{\sim}60L/m^2/hr$, but decreased to $5 L/m^2/hr$ after 95 days of operation due to clogging caused by particulate materials such as fibrous materials in garbage leachate. To prevent clogging caused by particulate materials, a pretreatment system such as screening is required. With the improvement with membrane unit operation, the two-phase anaerobic digestion with ultra filtration system is expected to have the possibility of treating garbage leachate.

In situ UHV TEM studies on nanobubbles in graphene liquid cells

  • Shin, Dongha;Park, Jong Bo;Kim, Yong-Jin;Kim, Sang Jin;Kang, Jin Hyoun;Lee, Bora;Cho, Sung-Pyo;Novoselov, Konstantin S.;Hong, Byung Hee
    • 한국진공학회:학술대회논문집
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    • 한국진공학회 2016년도 제50회 동계 정기학술대회 초록집
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    • pp.102-102
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    • 2016
  • Water, which is most abundant in Earth surface and very closely related to all forms of living organisms, has a simple molecular structure but exhibits very unique physical and chemical properties. Even though tremendous effort has been paid to understand this nature's core substance, there amazingly still lefts much room for scientist to explore its novel behaviors. Especially, as the scale goes down to nano-regime, water shows extraordinary properties that are not observable in bulk state. One of such interesting features is the formation of nanoscale bubbles showing unusual long-term stability. Nanobubbles can be spontaneously formed in water on hydrophobic surface or by decompression of gas-saturated liquid. In addition, the nanobubbles can be generated during electrochemical reaction at normal hydrogen electrode (NHE), which possibly distorts the standard reduction potential at NHE as the surface nanobubble screens the reaction with electrolyte solution. However, the real-time evolution of these nanobubbles has been hardly studied owing to the lack of proper imaging tools in liquid phase at nanoscale. Here we demonstrate, for the first time, that the behaviors of nanobubbles can be visualized by in situ transmission electron microscope (TEM), utilizing graphene as liquid cell membrane. The results indicate that there is a critical radius that determines the long-term stability of nanobubbles. In addition, we find two different pathways of nanobubble growth: i) Ostwald ripening of large and small nanobubbles and ii) coalescence of similar-sized nanobubbles. We also observe that the nucleation and growth of nanoparticles and the self-assembly of biomolecules are catalyzed at the nanobubble interface. Our finding is expected to provide a deeper insight to understand unusual chemical, biological and environmental phenomena where nanoscale gas-state is involved.

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