• Title/Summary/Keyword: osmosis membrane

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Syntheses of chlorine resistant reverse osmosis membranes

  • Kim, Nowon;Lee, Yong-Taek
    • Proceedings of the Membrane Society of Korea Conference
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    • 2004.05a
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    • pp.170-174
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    • 2004
  • Most of thin film composite reverse osmosis membranes include amide linkages, which are susceptible to chlorine attack resulting in N-chloro derivatives. This study examined a new method based on post-treatment of reverse osmosis membrane with various silane derivatives to improve chlorine resistance. The silane derivatives contain one alkyl group and three alkoxy groups such as trifluoromethyltrimethoxysilane, 3-aminopropylmethoxydiethoxysilane and 3, 3, 3-trifluoropropyltrimethoxysilane. Compared to commercial membranes, silane derivatives coated membranes showed significantly enhanced chlorine durability.

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Effect of Salt Concentration and Temperature in Synthetic Dyestuff Wastewater Treatment using Plate and Frame Membrane Module (평판형 막모듈을 이용한 합성염료 폐수처리에 있어서 염농도 및 온도의 영향)

  • Kim, Sun-Il;Lee, Bong-Woo;Yun, Young-Jae
    • Journal of Environmental Science International
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    • v.7 no.2
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    • pp.209-216
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    • 1998
  • Nanofiltration[NF45] and reverse osmosis membrane(HR98PP) separation treatment of dyestuff wastewater was carried out In order to separate relatively pure water from synthetic dyestuff wastewater, which consists of reactive dye, acid dye, basic dye, direct dye, and disperse dye. The experiments were performed by using the plate and frame membrane module. In the nanofiltration and reverse osmosis membrane separation, When the NaCl concentration was 0.1, 5.0, and 20.091, retention was 63.0, 46.0, 0.9%, respectively. When permeate flux was 125.0, 67.5, and 45.0 L/$m^2$ h, the osmotic pressure increased with Increasing the NaCl concentration. Permeate flux of two membranes Increased as temperature Increased due to segmental movement of polymer of the membrane and the rejection rate of dyestuff was decreased gradually. It was found that the rejection rate was about 95% in the nanofiltratlon, while the reverse osmosis membrane showed a high rejection rate of 99% under all temperature and pressures conditions.

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Fouling and cleaning of reverse osmosis membrane applied to membrane bioreactor effluent treating textile wastewater

  • Srisukphun, Thirdpong;Chiemchaisri, Chart;Chiemchaisri, Wilai;Thanuttamavong, Monthon
    • Environmental Engineering Research
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    • v.21 no.1
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    • pp.45-51
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    • 2016
  • Membrane bioreactor (MBR) and reverse osmosis (RO) membrane system was applied to the treatment and reclamation of textile wastewater in Thailand. An experiment was carried out to determine the fouling behavior and effect of anti-scalant and biocide addition to flux decline and its recovery through chemical cleaning. The RO unit was operated for one month after which the fouled membranes were cleaned by sequential chemical cleaning method. RO flux was found rapidly declined during initial period and only slightly decreased further in long-term operation. The main foulants were organic compounds and thus sequential cleaning using alkaline solution followed by acid solution was found to be the most effective method. The provision of anti-scalant and biocide in feed-water could not prevent deposition of foulant on the membrane surface but helped improving the membrane cleaning efficiencies.

High School Science Teachers' and Students' Conceptions Related to Osmosis

  • Won, Jeong-Ae;Ko, Young-Hwan;Paik, Seoung-Hey
    • Journal of The Korean Association For Science Education
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    • v.27 no.2
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    • pp.144-152
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    • 2007
  • In this study, high school science teachers' and students' various conceptions related to osmosis phenomena were compared with and analyzed in relation to the content of science textbooks used in high school science classrooms and college science courses. The questionnaires developed by the researchers were administered to science teachers and students. Differences can be found between the explanations of science textbooks on osmotic pressure and semi-permeable membranes. Many science teachers and students thought of osmotic pressure as 'membrane pressure occurred by the movement of a solvent'. Moreover, the types of teachers of semi-permeable membranes were similar regardless of their academic majors. Many of the teachers thought of a semi-permeable membrane as a membrane that 'passes small-size particles'; however, many students thought of this type of membrane as being 'selectively permeable'. Also, the salt-pickling cabbage phenomenon seemed to cause significant confusion to science teachers and students. These study results show that teachers and students possess various conceptions related to the osmosis phenomena. These different conceptions related to osmosis phenomena might cause confusion and diverse conceptions including misconceptions among teachers and students.

Evaluation of FO membrane performance for each type of pre-treatment from WWTP secondary effluents (하수방류수의 전처리 조건별 FO막의 운전성능평가)

  • Jeong, Junwon;Kim, Jihoon;Kim, Geonyoub;Park, Junyoung;Kim, Hyungsoo;Kim, Hyungsook
    • Journal of Korean Society of Water and Wastewater
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    • v.30 no.2
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    • pp.131-137
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    • 2016
  • The development of alternative water resources has emerged as an effective method for solving drought of water resources due to extreme weather and increase in water consumption. Recently, in Korea, there has been active research on reverse osmosis desalination technology, wastewater reuse using forward osmosis membranes, and the forward osmosis(FO)-reverse osmosis(RO) hybrid process combining these two technologies. In this study, the basic performance of FO membranes manufactured by three domestic and international manufactures such as Microfilter Co., Ltd., Toray Chemical Korea Inc., and Hydration Technologies Inc., were investigated for wastewater reuse. In addition, as an experiment to select feed solution, the selected membranes were operated 48 consecutive hours using three secondary effluents pretreated by the UF membrane with a pore size of $0.1{\mu}m$ and auto strainer with pore sizes of $1{\mu}m$ and $100{\mu}m$ as feed solution. Although there was not much difference in the operating performance. Thus, the treated water using the $100{\mu}m$ auto strainer was selected as feed solution applied to the assessment.

Intrinsic Flux Inequality in Forward Osmosis (FO) and Pressure-Retarded Osmosis (PRO) Processes (수학적 귀납법을 이용한 정삼투 및 압력지연삼투 공정의 투과율 불균형 해석)

  • Kim, Albert S.;Lee, Seung-won
    • Membrane Journal
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    • v.25 no.4
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    • pp.367-372
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    • 2015
  • In pressure-retarded osmosis (PRO) and forward osmosis (FO) processes, solvent (permeate) flux depends on which surface the draw solution faces. There are two operation modes. PRO mode indicates that the active layer faces the draw solution, and FO mode means that the porous substrate fronts the draw stream. It is often observed that the PRO mode produces higher flux than that of FO under the same operating conditions. The current work uses the method of proof by contradiction, and mathematically proves the intrinsic flux inequality between the two modes.

Application of Microfiltration and Reverse Osmosis System to Sewage Reuse for Industrial Water (하수를 공업용수로 재이용하기 위한 정밀여과 및 역삼투 시스템 적용에 관한 연구)

  • 강신경;이해군;김지원
    • Membrane Journal
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    • v.12 no.3
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    • pp.151-157
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    • 2002
  • This research was to demonstrate the Possibility of sewage reuse for industrial purpose with use of membrane system. A bench scale test with microfiltration and reverse osmosis showed that microfiltration in the sewage treatment was not able to remove the soluble salts but 70% suspended solids (SS), suggesting that the treated water could be used as direct cooling water. In addition, the reverse osmosis removed not only soluble salts but also 95% SS, proposing that reverse osmosis-treated water could be used as both indirect cooling water and rinsing water. For a 100 ton/day pilot plant, 20 and 12 elements of microfiltration and reverse osmosis were required, respectively.

Organic fouling in forward osmosis (FO): Membrane flux behavior and foulant quantification

  • Xia, Shengji;Yao, Lijuan;Yang, Ruilin;Zhou, Yumin
    • Membrane and Water Treatment
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    • v.6 no.2
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    • pp.161-172
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    • 2015
  • Forward osmosis (FO) is an emerging membrane technology with potential applications in desalination and wastewater reclamation. The osmotic pressure gradient across the FO membrane is used to generate water flux. In this study, flux performance and foulant deposition on the FO membrane were systematically investigated with a co-current cross-flow membrane system. Sodium alginate (SA), bovine serum albumin (BSA) and tannic acid (TA) were used as model foulants. Organics adsorbed on the membrane were peeled off via oscillation and characterized by Fourier transform infrared (FTIR) spectroscopy and scanning electron microscopy (SEM). When an initial flux of $8.42L/m^2h$ was applied, both flux reduction and foulant deposition were slight for the feed solution containing BSA and TA. In comparison, flux reduction and foulant deposition were much more severe for the feed solution containing SA, as a distinct SA cake-layer was formed on the membrane surface and played a crucial role in membrane fouling. In addition, as the initial SA concentration increased in FS, the thickness of the cake-layer increased remarkably, and the membrane fouling became more severe.

Advanced Treatment for Reuse of Oil Refinery Process Wastewater using UF/RO Processes (UF/RO 공정을 이용한 정유공장 방류수의 재활용을 위한 고도처리)

  • 이광현
    • Membrane Journal
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    • v.10 no.4
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    • pp.220-229
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    • 2000
  • Deionized water and wastewater flux were discussed using module set 1-7 composed of ultrafiltration hollow fiber type modules and reverse osmosis spiral wound type modules. The separation characteristics of ultrafiltration and reverse osmosis membranes were discussed with the variation of applied pressure and temperature. Turbidity and SS were removed effectively from ultrafiltration mem¬brane, and removal efficiency of COD, T-N, and TDS using reverse osmosis membrane was very efficient. Permeate flux increased linearly with the increase of applied pressures and temperature. It was shown that ultrafiltration and reverse osmosis membranes were suitable Lo the advanced treatment and reuse of oil refinery process effluent.

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Electrospun polyamide thin film composite forward osmosis membrane: Influencing factors affecting structural parameter

  • Ghadiri, Leila;Bozorg, Ali;Shakeri, Alireza
    • Membrane and Water Treatment
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    • v.10 no.6
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    • pp.417-429
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    • 2019
  • Poly Sulfone nanofibers were electrospun to fabricate membranes of different characteristics. To fabricate the fiber mats, polymer concentration, flowrate, and current density were determined as the most influencing factors affecting the overall performance of the membranes and studied through Response Surface Methodology. The Box-Behnken Design method (three factors at three levels) was used to design, analyze, and optimize the parameters to achieve the best possible performance of the electrospun membranes in forward osmosis process. Also, internal concentration polarization that characterizes the efficiency of the forward osmosis membranes was determined to better assess the overall performance of the fabricated electrospun membranes. Water flux to reverse salt flux was considered as the main response to assess the performance of the membranes. As confirmed experimentally, best membrane performance with the minimal structural parameter value could be achieved when predicted optimal values were used to fabricate the membranes through electrospinning process.