• Title/Summary/Keyword: Organic membrane

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Production of enantiopure epoxides by yeast epoxide hydrolase using a two-phase membrane bioreactor (한국생물공학회 정기총회 및 연구논문발표회 발표논문)

  • Choe, Won-Jae;Choe, Cha-Yong
    • 한국생물공학회:학술대회논문집
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    • 2000.04a
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    • pp.145-148
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    • 2000
  • Large-scale resolution of epoxides by the yeast Rhodotorula glutinis was demonstrated in an aqueous/organic two-phase cascade membrane bioreactor. Due to the chemical instability and low solubility of epoxides in aqueous phases, an organic solvent was introduced into the reaction mixture in order to enhance resolution of epoxide. A cascade hollow-fiber membrane bioreactor was used (i) to minimize the toxicity of organic solvents towards the epoxide hydrolase of Rhodotorula glutinis, and (ii) to remove inhibitory amounts of formed diol from the yeast cell containing aqueous phase. Dodecane was selected as a suitable solvent and 1,2-epoxyhexane as a model substrate. By use of this membrane bioreactor, highly concentrated (0.9 M in dodecane) enantiopure (>98% ee) (S)-1,2-epoxyhexane (6.5 g, 30% yield) was obtained from its racemic mixture.

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Natural Organic Matter Removal and Fouling Control in Low-Pressure Membrane Filtration for Water Treatment

  • Cui, Xiaojun;Choo, Kwang-Ho
    • Environmental Engineering Research
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    • v.19 no.1
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    • pp.1-8
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    • 2014
  • Natural organic matter (NOM) is a primary component of fouling in low-pressure membrane filtration, either solely, or in concert with colloidal particles. Various preventive measures to interfere with NOM fouling have been developed and extensively tested, such as coagulation, oxidation, ion exchange, carbon adsorption, and mineral oxide adsorption. Therefore, this article aims to conduct a literature review covering the topics of low-pressure membrane processes, NOM characteristics and fouling behaviors, and diverse fouling control strategies. In-depth explanations and discussion are made regarding why some treatment options are able to remove NOM from source water, but do not reduce fouling. This review provides insight for hybridized membrane processes with respect to NOM removal and fouling mitigation in water treatment.

Organic / inorganic composite membrane for Polymer Electrolyte Membrane Fuel Cell (고분자전해질 연료전지용 유기/무기 복합 전해질)

  • Choi Seong Ho;Hong Hyeon Sil;Lee Heung Chan;Kim Yu Mi;Kim Geon
    • 한국전기화학회:학술대회논문집
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    • 2003.07a
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    • pp.169-171
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    • 2003
  • Organic/inorganic hybrid membranes have been prepared and evaluated as polymer electrolytes in a polymer electrolyte membrane fuel cell (PEMFC). Previously, partially fluorinated poly (arylenether) was synthesized and the polymer was sulfonated by fuming sulfuric acid$(30\%\;SO_3)$. Modification of these polymers with coupling agent and inorganic materials was carried out to prepare membranes. Membranes cast from these materials were investigated in relation to the proton conductivity and weight loss at the room temperature. It was found that these membranes had a higher conductivity of $10^{-2}\;Scm^{-1}$ at the room temperature. But inorganic materials have leaked out from the hybrid membrane. If this problem is resolved, organic/inorganic hybrid membranes will become satisfactory Polymer electrolytes for the PEMFC.

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The thermal stabilization characteristics of electrolyte membrane in high temperature electrolysis[HTE] (고온 수전해 전해질 막의 열안정화 특성 고찰)

  • Choi, Ho-Sang;Son, Hyo-Seok;Sim, Kyu-Sung;Hwang, Gab-Jin
    • Transactions of the Korean hydrogen and new energy society
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    • v.16 no.2
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    • pp.150-158
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    • 2005
  • Added ratio of 8YSZ powder and organic compounds (solvent, plasticizer, dispersant, binder) properly. It manufactured electrolysis membrane by wet process that make slurry and dry process that do not use organic compounds. In the case of wet process, harmony combination and method of organic compound are an importance element in slurry manufacture. This slurry did calcine at temperature of 140$^{\circ}C$ in Furnace and manufactured electrolyte disk by Dry pressing method. Like this, manufacturing disk sintered at temperature of $1300^{\circ}C,\;1400^{\circ},\;1500^{\circ}C$ in Furnace and completed electrolysis membrane. Confirmed change of crystal structure and decision form through analysis of density, SEM, XRD according to change of sintering temperature, and considered relation with ion conductivity.

Evaluation on Chemical Cleaning Efficiency of Organic-fouled SWRO Membrane in Seawater Desalination Process (해수담수화 공정에서 역삼투막의 유기 막오염에 대한 SWRO 막의 화학세정 효율 평가)

  • Park, Jun-Young;Hong, Sung-Ho;Kim, Ji-Hoon;Jeong, Woo-Won;Nam, Jong-Woo;Kim, Young-Hoon;Jeon, Min-Jung;Kim, Hyung-Soo
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.2
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    • pp.177-184
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    • 2011
  • Membrane fouling is an unavoidable phenomenon in operation of seawater reverse osmosis (SWRO) and major obstacle for economic and efficient operation. When fouling occurs on the membrane surface, the permeate flux is decreased, on the contrary, the trans-membrane pressure (TMP) is increased, therefore operation and maintaining costs and potential damage of membranes are able to the pivotal risks of the process. Chemical cleaning process is essential to prevent interruptions for effective RO membrane filtration process. This study focused on proper chemical cleaning condition for polyamide RO membranes of 4 companies. Several chemical agents were applied for chemical cleaning under numbers of operating conditions. Additionally, a monitoring tool of FEEM as autopsy analysis method is adapted for the prediction of organic bio-fouling.

Applicability of Temperature Correction Trans-membrane Pressure as a Fouling Index of Membrane Water Treatment Process (막여과 정수처리 공정에서 온도보정차압 식의 파울링 지표로서의 활용성 검토)

  • Kim, Minjae;Lim, Jae-Lim;Lee, Kyung-Hyuk;Lee, Young-Joo;Kim, Suhan
    • Journal of Korean Society of Water and Wastewater
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    • v.30 no.1
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    • pp.1-8
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    • 2016
  • Temperature correction trans-membrane pressure (TC-TMP) is frequently used as a fouling index in membrane water treatment plants. TC-TMP equation is derived based on an assumption that the total membrane resistance (i.e. the sum of the intrinsic membrane resistance and fouling resistance) is not affected by temperature. This work verified the validity of this assumption using microfiltration (MF) and ultrafiltration (UF) membranes with and without fouling. The foulants used in the work were kaolin (inorganic) and humic acid (organic). The intrinsic resistances of MF and UF membranes remains at constant values regardless of temperature change. When the same amount of foulants were accumulated on the membrane, inorganic fouling resistance with kaolin was constant regardless of temperature change while organic fouling resistance with humic acid decreased at higher temperatures, which means that TC-TMP cannot be used as a fouling index when organic fouling occurs in a real field application. Since TC-TMP underestimates the amount of fouling at higher temperatures, more attention should be necessary in the operation of membrane water treatment plant in a hotter season like summer.

Synthesis and Characterization of Ion Exchange Particles for Application of Anion Exchange Membrane (음이온교환막 적용을 위한 이온교환입자의 합성 및 특성평가)

  • Dong Jun Lee;Kwang Seop Im;Ka Yeon Ryu;Sang Yong Nam
    • Membrane Journal
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    • v.33 no.3
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    • pp.137-147
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    • 2023
  • In this study, Br-PPO was developed by applying additive organic particles through a suspension polymerization synthesis method. The anion exchange membrane fuel cell system performance was evaluated using it to an anion exchange membrane. To improve the performance, organic ion exchange particles were prepared and added to the anion exchange membrane. Chemical structure analysis and synthesis were determined through FT-IR and NMR, and tensile strength and thermal stability were measured through TGA and UTM to determine whether it could be driven. Before the anion exchange membrane fuel cell test, the performance was evaluated by measuring the ion conductivity and ion exchange capacity. Finally, the Br-PPO-TMA-SDV (0.7%) anion exchange membrane with excellent ion conductivity and ion exchange capacity was introduced into the fuel cell system. Its performance was compared with FAA-3-50, a commercial membrane, to determine whether it could be introduced into a fuel cell system.

Dependence of Electrical Resistance in Porous Silicon Layer for Detecting Organic Vapors (유기 가스 검지를 위한 다공질 실리콘층의 전기 저항 의존성)

  • Park, Kwang-Yeol;Kim, Seong-Jeen;Lee, Sang-Hoon;Choi, Bok-Gil
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2002.07b
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    • pp.792-796
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    • 2002
  • In this work, porous silicon(PS) layer is used as a sensing material to detect organic gases. To do this, PS sensors with membrane structure are fabricated. The sensors were made by applying the technologies of membrane formation by anisotropic etching of silicon, and PS layer formation by anodization in HF solution. From fabricated sensors, current-voltage (I-V) curves were measured against ethanol (called alcohol), methanol and acetone gases evaporated from 0.1 to 0.5% solution concentrations at $36^{\circ}C$. As the result, all curves showed rectifying behavior due to a diode structure between Si and PS, and the conductance of sensor devices increased largely with the organic solution concentration at high voltage of 5V.

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Determination of the Formation Constants of Metal Complexes with Organic Acids by Adsorption Method (흡착법에 의한 금속이온과 유기산간의 착염 생성계수의 측정법)

  • Jae, Won-Mok
    • Journal of the Korean Chemical Society
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    • v.15 no.4
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    • pp.199-203
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    • 1971
  • The adsorption method for the determination of the formation constants of the metal complexes with organic acids was developed by using membrane filters. The adsorption method involved the measurements of radioactivities of the adsorbed metal on membrane filters and the filtrate solution after the radioactive metal ion were filtered through membrane filters in the presence of organic ions of varying concentration. Comparing the adsorption method with the ion exchange method, it was seen that the adsorption method was simpler and faster than the ion exchange method. As an example of the metal complex with organic acid yttrium citrate complex was chosen, and the formation constant of the complex obtained by the adsorption method showed $K_f=2.0{\times}10^{-4}(l. mole^{-1})$ at a pH of 7. Also the present study revealed that the carrierfree state of yttrium in aqueous solution was present in the completely ionized state.

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MEMBRANE PROCESSES IN ENVIRONMENTAL TECHNOLOGY

  • Blume, I.;Smolders, C.A.
    • Proceedings of the Membrane Society of Korea Conference
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    • 1992.04a
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    • pp.11-28
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    • 1992
  • In this paper we will first give a short overview of the more recent developments in MF, UF and RO. This is followed by a closer look on newer technologies applied in environmental problems. The applications looked an are the recovery of organic components from solvent laden gas streams and the separation of organic volatiles from aqueous waste waters via pervaporation. Technical solutions, the advantages and disadvantages of the processes and, where possible, cost estimations will be presented.

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