• 제목/요약/키워드: Water permeation

검색결과 480건 처리시간 0.027초

막 축전식 탈염용 비불소계 아민화 Poly(vinylbenzyl chloride-co-ethyl methacrylate-co-styrene) 음이온교환막의 합성 및 특성 (Synthesis and Properties of Nonfluoro Aminated Poly(vinylbenzyl chloride-co-ethyl methacrylate-co-styrene) Anion Exchange Membranes for MCDI Process)

  • 구진선;곽노석;황택성
    • 폴리머
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    • 제36권5호
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    • pp.564-572
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    • 2012
  • 본 연구에서는 막축전식 탈염(membrane capacitive deionization, MCDI) 공정용 음이온교환막의 제조를 위하여 vinylbenzyl chloride-co-ethyl methacrylate-co-styrene(VBC-EMA-St) 공중합체를 합성하였으며, 아민화 반응과 열처리를 통하여 음이온교환막을 제조하였다. 구조확인을 위하여 FTIR 분석을 하였고, GPC와 TGA를 통하여 합성한 고분자의 분자량과 분자분포, 열안정성을 분석하였으며, 함수율 및 이온교환용량을 측정하였다. 또한 LCR meter로 전기저항을 측정하고, MCDI 공정에 적용하기 위하여 제조한 음이온교환막을 충방전 시험 측정하였다. 이온교환용량, 함수율, 전기저항, 분자량은 각각 1.69 meq/g, 23.7%, 1.61 ${\Omega}{\cdot}cm$, $3.4{\times}10^4$ g/mol이었으며, CDI 충방전 시험 결과 상용화막인 AMX보다 우수한 성능을 나타내었다.

고강도 PVDF 중공사 정밀여과막 제조 특성 (Preparation of Higher Reinforced PVDF Hollow Fiber Microfiltration Membrane)

  • 최호상;박헌휘
    • 멤브레인
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    • 제20권4호
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    • pp.320-325
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    • 2010
  • 화학적 안정성이 양호하고, 제막조건이 온화한 재료인 poly(vinylidene fluoride) (PVDF)를 주재료로 사용하여 용매, 첨가제, 혼합고분자 및 제막조건의 변화에 따른 고강도 친수성 정밀여파(microfiltration, MF) 중공사 분리막의 실험에 의해 고찰하였다. 제조된 MF 중공사막의 막성능은 평균 공경 $0.3{\mu}m$, 인장강도 $42kg_f/cm^2$, 순수 투과유량은 600 LMH을 얻었다. 제막과정에서 다양한 첨가제의 막성능을 검토한 결과는 순수투과유량과 제거율에 상당한 영향을 미치고 있음을 알 수 있었다. MF막의 친수성을 개선하기 위해 소수성 PVDF와 상호 용해성 이 좋은 친수성 poly(methyl methacrylate) (PMMA)를 혼합하여 투과성능과 제거율을 개선한 우수한 친수성 MF막을 제조할 수 있었다.

Evidence for Existence of a Water-Extractable Anticoagulant in an Earthworm, Lumbricus rubellus

  • Woo, Jeong-Im;Bahk, Yun-Kyung;Yu, Kyoung-Hee;Paik, Seung-R.;Chang, Chung-Soon
    • BMB Reports
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    • 제29권6호
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    • pp.500-506
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    • 1996
  • We have isolated a water-extracted novel regulator for blood coagulation from an earthworm, Lumbricus rubellus. As a folk remedy, the earthworm has been known to facilitate blood circulation. After complete heat inactivation of endogenous proteases in the earthworm, an anticoagulant(s) was purified through ammonium sulfate fractionation and three consecutive gel permeation chromatography of Sephacryl S-300, Sephadex G-75, and G-150 by measuring activated partial thromboplastin time (APTT) The anticoagulant was further purified to 2,800 fold with a C4 reversed-phase HPLC This activity was stable under heat ($100^{\circ}C$ for 30 min) and acidic conditions (0.4 N HCl). The effects of this partially purified anticoagulant on thrombin were observed with various substrates such as N${\alpha}$-benzoyl-DL-arginine-p-nitroanilide (BApNA), H-D-phenylalanyl-L-pipecoyl-L-arginine-p-nitroanilide (S-2238), N${\alpha}$-p-tosyl-L-arginine methyl ester (TAME), and fibrinogen as a natural substrate. Only TAME hydrolysis, due to an esterase activity of the enzyme, was inhibited among the chromogenic substrates. In addition, the anticoagulant not only inhibited the conversion of fibrinogen to fibrin but also prolonged the fibrin clot formation monitored with the in vitro coagulation test. Based on these observations, we suggest the significance of measuring the ability of antithrombotic drugs to inhibit the esterase activity of thrombin. In this report, it was also shown that the earthworm indeed contained a water-extractable, heat- and acid-stable anticoagulant which could be used as a novel antithrombotic agent.

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Preparation of graphene oxide incorporated polyamide thin-film composite membranes for PPCPs removal

  • Wang, Xiaoping;Li, Nana;Zhao, Yu;Xia, Shengji
    • Membrane and Water Treatment
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    • 제9권4호
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    • pp.211-220
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    • 2018
  • Incorporating nano-materials in thin-film composite (TFC) membranes has been considered to be an approach to achieve higher membrane performance in various water treatment processes. This study investigated the rejection efficiency of three target compounds, i.e., reserpine, norfloxacin and tetracycline hydrochloride, by TFC membranes with different graphene oxide proportions. Graphene oxide (GO) was incorporated into the polyamide active layer of a TFC membrane via an interfacial polymerization (IP) reaction. The TFC membranes were characterized with FTIR, FE-SEM, AFM; in addition, the water contact angle measurements as well as the permeation and separation performance were evaluated. The prepared GO-TFC membranes exhibited a much higher flux ($3.11{\pm}0.04L/m2{\cdot}h{\cdot}bar$) than the pristine TFC membranes ($2.12{\pm}0.05L/m2{\cdot}h{\cdot}bar$) without sacrificing their foulant rejection abilities. At the same time, the GO-modified membrane appeared to be less sensitive to pH changes than the pure TFC membrane. A significant improvement in the anti-fouling property of the membrane was observed, which was ascribed to the favorable change in the membrane's hydrophilicity, surface morphology and surface charge through the addition of an appropriate amount of GO. This study predominantly improved the understanding of the different PA/GO membranes and outlined improved industrial applications of such membranes in the future.

Racemic and enantiomeric effect of tartaric acid on the hydrophilicity of polysulfone membrane

  • Sharma, Nilay;Purkait, Mihir Kumar
    • Membrane and Water Treatment
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    • 제7권3호
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    • pp.257-275
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    • 2016
  • The enantiomeric and racemic effects of tartaric acid (TA) on the properties of polysulfone (PSn) ultrafiltration membranes were studied in terms of morphology and hydrophilicity (HPCT) of membrane. Asymmetric membranes were prepared by direct blending of polyvinyl pyrrolidone (PVP) with D-TA and DL-TA in membrane casting solution. FTIR analysis was done for the confirmation of the reaction of PVP and TA in blended membranes and plain PSn membranes. Scanning electron microscope (SEM), field emission scanning electron microscope (FESEM) and atomic force microscopy (AFM) were used for analyzing the morphology and structure of the resulting membranes. The membranes were characterized in terms of pure water flux (PWF), hydraulic permeability and HPCT. PWF increased from $52L/m^2h$ to $79.9L/m^2h$ for plain and D-TA containing PSn membrane, respectively. Water contact angle also found to be decreased from $68^{\circ}$ to $55^{\circ}$. In Additionally, permeation and rejection behavior of prepared membranes was studied by bovine serum albumin (BSA) solution. A considerable increase in BSA flux (from $19.1L/m^2h$ for plain membrane to $32.1L/m^2h$ for D-TA containing membrane) was observed. FESEM images affirm that the pore size of the membranes decreases and the membrane permeability increases from 0.16 to 0.32 by the addition of D-TA in the membrane. D-TA increases the HPCT whereas; DL-TA decreases the HPCT of PSn membrane. PVP (average molecular weight of 40000 Da) with D-TA (1 wt%) gave best performance among all the membranes for each parameter.

Preparation of highly hydrophobic PVDF hollow fiber composite membrane with lotus leaf-like surface and its desalination properties

  • Li, Hongbin;Zi, Xingchen;Shi, Wenying;Qin, Longwei;Zhang, Haixia;Qin, Xiaohong
    • Membrane and Water Treatment
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    • 제10권4호
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    • pp.287-298
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    • 2019
  • Lotus leaf has a special dual micro and nano surface structure which gives its highly hydrophobic surface characteristics and so-called self cleaning effect. In order to endow PVDF hollow fiber membrane with this special structure and improve the hydrophobicity of membrane surface, PVDF hollow fiber composite membranes was obtained through the immersion coating of poly(vinylidene fluoride-co-hexafluoropropylene) (PVDF-HFP) dilute solution on the outside surface of PVDF support membrane. The prepared PVDF composite membranes were used in the vacuum membrane distillation (VMD) for the desalination. The effects of PVDF-HFP dilute solution concentration in the dope solution and coating time on VMD separation performance was studied. Membranes were characterized by SEM, WCA measurement, porosity, and liquid entry pressure of water. VMD test was carried out using $35g{\cdot}L^{-1}$ NaCl aqueous solution as the feed solution at feed temperature of $30^{\circ}C$ and the permeate pressure of 31.3 kPa. The vapour flux reached a maximum when PVDF-HFP concentration in the dilute solution was 5 wt% and the coating time was kept in the range of 10-60 s. This was attributed to the well configuration of micro-nano rods which was similar with the dual micro-nano structure on the lotus leaf. Compared with the original PVDF membrane, the salt rejection can be well maintained which was greater than 99.99 % meanwhile permeation water conductivity was kept at a low value of $7-9{\mu}S{\cdot}cm^{-1}$ during the continuous testing for 360 h.

PEBAX/PVDF 복합막 제조 및 투과증발을 통한 에탄올/물 분리 연구 (Preparation of PEBAX/PVDF Composite Membrane and Separaration of Ethanol/Water Mixtures by Pervaporation)

  • 정예원;나해은;조세욱;손민영
    • 멤브레인
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    • 제33권6호
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    • pp.377-382
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    • 2023
  • 본 연구는 PEBAX/PVDF 복합막을 제조하고 에탄올/물 혼합액에 대한 투과증발 성능을 평가하였다. 또한 PVDF 지지체 표면에 ZIF-8 층을 형성하여 복합막의 투과증발 성능을 향상시키고자 하였고, PEBAX 선택층 두께에 따른 성능 비교를 통해 최적의 막을 선정하였다. 제작된 복합막을 물과 에탄올이 95/5 중량비로 혼합된 공급액에 대하여 투과증발 실험을 수행하였다. 그 결과 ZIF-8 충이 형성된 PVDF 지지체를 사용한 복합막의 경우 플럭스 1.98 kg/m2h, 분리 계수 3.88로 일반 PVDF 지지체를 사용한 복합막보다 투과량과 선택도가 모두 높은 값을 나타내었다.

Hydrophobic modification conditions of Al2O3 ceramic membrane and application in seawater desalination

  • Lian li;Zhongcao Yang;Lufen Li
    • Membrane and Water Treatment
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    • 제15권1호
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    • pp.21-29
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    • 2024
  • 1H,1H,2H,2H-perfluorodecytriethoxysilane (C16H19F17O3Si) be successfully applied to the hydrophobic modification of Al2O3 tubular ceramic membrane. Taking the concentration of modification solution, modification time, and modification temperature as factors, orthogonal experiments were designed to study the hydrophobicity of the composite membranes. The experiments showed that the modification time had the greatest impact on the experimental results, followed by the modification temperature, and the modification solution concentration had the smallest impact. Concentration of the modified solution 0.012 mol·L-1, modification temperature 30 ℃ and modification time 24 h were considered optimal hydrophobic modification conditions. And the pure water flux reached 274.80 kg·m-2·h-1 at 0.1MPa before hydrophobic modification, whereas the modified membrane completely blocked liquid water permeation at pressures less than 0.1MPa. Air gap membrane distillation experiments were conducted for NaCl (2wt%) solution, and the maximum flux reached 4.20 kg·m-2·h-1, while the retention rate remained above 99.8%. Given the scarcity of freshwater resources in coastal areas, the article proposed a system for seawater desalination using air conditioning waste heat, and conducted preliminary research on its freshwater production performance using Aspen Plus. Finally, the proposed system achieved a freshwater production capacity of 0.61 kg·m-2·h-1.

Coagulant bath medium effect towards polylactic acid membranes structure and methylene blue dye removal

  • Amira M. Nasib;Stephen Simon;Syahmie M. Rasidi;Siti Kartini E. Ab. Rahim;Hoo Peng Yong;Ng Qi Hwa;Khairiraihanna Johari
    • Advances in materials Research
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    • 제13권3호
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    • pp.243-251
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    • 2024
  • The asymmetric polylactic acid (PLA) membrane was prepared via phase inversion method using non-solvent induced separation (NIPS) technique. This study aims to synthesized as well as to characterize the PLA membrane and evaluating the membrane performance on water flux and permeability. In addition, this research also studied the removal performance of methylene blue dye. The polymer solution has been prepared using 12 wt.% of PLA and dissolved in 88 wt.% of Dimethylacetamide (DMAc) as a solvent. Then, the cast film was immersed in different ratio of coagulant bath medium (distilled water: methanol: ethanol) ranging from 100:0:0, 75:25:0, 75:0:25 and 75:12.5:12.5, respectively). Several characterizations were performed which include, membrane contact angle and membrane porosity. Performance PLA membranes were determined in terms of water flux and permeability at 1 bar transmembrane pressure using dead-end permeation cell. Finally, methylene blue (MB) removal efficiency was tested at the same transmembrane pressure. The findings revealed that the increase of alcohol concentration in coagulant bath resulted in higher porosity and lower contact angle. In short, MB dye rejection efficiency is also closely related to the amount of alcohol ratio used in coagulant baths. Increases in concentration of methanol and ethanol in coagulant bath medium increases the membrane porosity thus increased in efficiency of methylene blue rejection.

다공성 실관막을 이용한 투과추출 공정에 관한 연구 -PP 및 PTFE실관막을 이용한 에탄올의 투과추출 특성에 관한 연구- (A Study on the Perstraction Process Using Microporous Hollow Fiber -The Characteristics of Perstraction Using PP and Hollow Fiber-)

  • 정원;황의윤;이호원;김우식
    • 멤브레인
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    • 제1권1호
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    • pp.65-77
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    • 1991
  • PP 및 PTFE 실관막을 이용하여 xylene-HAc(acetic acid)-water계, MIBK-ethanol-water계 및 TBP-ethanol-water계에서의 압력차 변화, 수용상 및 유기상 유속 변화에 따른 아세트산 및 에탄올의 투과추출 실험을 행하였다. xylene-HAc-water계에서 구한 막상에서의 물질전달계수로 부터 실관막의 굴곡률을 구할 수 있었는바, PP 재질의 Celgard X10-400 및 PTFE 재질의 Tex TA001실관막의 굴곡률은 각각 1.82 및 1.43이었다. 에탄올의 투과추출시 투과 flux 및 총괄물질전달계수는 추출 용매로서 MIBK를 사용한 경우가 TBP를 사용한 경우보다 큰 것으로 나타났으며 이러한 경향은 유기상 유속이 증가함에 따라 뚜렷이 나타났다. 또한 총괄물질전달계수는 유기상 유속의 증가에 따라 비선형적으로 증가하였는 바, 이들 사이에 $K_o {\propto} V_{or}^{-0.35}$인 관계가 있음을 확인하였다. 에탄올의 투과추출에 있어서 Gore Tex TA001실관막을 사용한 경우 율속단계는 막상에서의 물질전달이었다.

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