• 제목/요약/키워드: Ion Exchange Resin

검색결과 368건 처리시간 0.145초

Advances in electrodeionization technology for ionic separation - A review

  • Khoiruddin, Khoiruddin;Hakim, A.N.;Wenten, I.G.
    • Membrane and Water Treatment
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    • 제5권2호
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    • pp.87-108
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    • 2014
  • Electrodeionization (EDI), which combines electrodialysis (ED) and conventional ion-exchange (IX), is a mature process which has been applied since more than twenty years on commercial use for the production of ultrapure water (UPW). Eliminating chemical regeneration is the main reason for its commercial success. The increase in acceptance of EDI technology has led to an installation of very large plant as the commercial state of the art that produces $1,500m^3/h$ of water for high pressure steam boiler. More recently, EDI system has found a number of new interesting applications in wastewater treatment, biotechnology industry, and other potential field. Along with further growth and wider applications, the development of stack construction and configuration are also become a concern. In this paper, the principle of EDI process is described and its recent developments, commercial scale, and various applications are pointed out.

Decolorization of Aqueous Caprolactam Solution by Anion-exchange Resins

  • Yuan Zhen;Yu Ping;Luo Yunbai
    • Fibers and Polymers
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    • 제7권2호
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    • pp.112-116
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    • 2006
  • Caprolactam is the most important raw material for making Nylon 6 fibers and its quality directly determines the quality of Nylon. So it is necessary to study the techniques and methods to remove the colorful impurities from caprolactam. In this paper, the decolorization of caprolactam aqueous solution by anion exchange resins was studied and the decoloring abilities of five commercial resins were investigated. The regeneration of the resins was also studied, too. This study shows that the resin AMTX202 have excellent decoloring ability in the column experiment and that the decoloring efficiency is correlated with the volume of resins packed and is slightly affected by the flow rate and regenerating times. The fact that the resins can be regenerated and reused without affecting the efficiency of decolorization will decrease the cost of the treatment and operation in the industry. The adsorption of colored compounds with anion exchange resins in the packed columns seems to be technically feasible.

캐스팅법에 의한 전기투석용 고내구성 Polyvinylidene Fluoride (PVDF)계 양이온 불균질 이온교환막 제조 및 탈염특성 (Preparation and Desalination Characteristics of Highly Durable Heterogeneous Cation-exchange Membrane Based on Polyvinylidene Fluoride (PVDF) by Casting Method for Electrodialysis)

  • 고대영;김인식;황택성
    • 멤브레인
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    • 제26권2호
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    • pp.97-107
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    • 2016
  • 본 연구는 양이온 불균질막을 제조하기 위해 PVDF matrix에 상용 양이온교환수지와 sulfonated poly(phenylene oxide)(SPPO)를 배합하여 제조, 이온 흡착 특성에 관하여 연구하였다. 연구결과 PVDF-IER 불균질막과 PVDF-SPPO 불균질막 PVDF-SPPO-IER과 비교하였을 때 고분자 매트릭스의 비율이 30% 이하일 경우 이온교환용량, 전기저항에서 우수한 물성을 가지고 있는 것을 확인할 수 있었다. 인장강도의 경우 PVDF resin의 약한 내구성에도 불구하고 상용화 불균질막과 비교하여 최대 5배 이상의 강인한 모습을 보이고 있는 것으로 확인할 수 있었다. 따라서 화학적 특성과 기계적 특성을 고려했을 때 PVDF와 이온교환분말과 SPPO의 혼합 최적 비율은 30 : 70이며 이때의 전기저항은 $3{\sim}5{\Omega}{\cdot}cm^2$, 이온교환 용량은 0.6~1.0 meq/g으로 측정되었고 기계적 강도는 $12{\sim}15kgf/cm^2$으로 측정되었다.

Measurement of Carbon-14 Activity in Spent Ion-exchange Resin of Wolsong Nuclear Power Plant

  • Kim Kyoung-Doek;Choi Young-Ku;Kang Ki-Du;Yang Ho-Yeon
    • 한국방사성폐기물학회:학술대회논문집
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    • 한국방사성폐기물학회 2005년도 Proceedings of The 6th korea-china joint workshop on nuclear waste management
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    • pp.165-175
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    • 2005
  • Measurement of spent resin activity was initiated in 2004 in order to develop the C-14 removal technology for safe disposal. As part of this program, spent resins were sampled and measured in the in-station resin storage tank 2 at Wolsong Nuclear Power Plant Unit 1. At the time of sampling, the resins had been in storage tank from 3 to 23 years. Total 72 resin samples were sampled, which were collected from both man-hole (68 samples) and test-hole (4 samples) in the in-station resin storage tank 2. They were separated into liquid, activated carbon, zeolite, and spent resin. The spent resins were oxidized with sample oxidizer and analyzed for C-14. Ten of collected mixed resin samples were separated by density into cation and anion resins using a sugar solution. The C-14 concentration in anion exchange resin was approximately 2 times higher than in the mixed resin. The average concentration of C-14 in the cation/anion mixed exchange resin was $460\;GBq/m^3$ from test-hole and $53.1\;GBq/m^3$ from man-hole. We have found that concentration of C-14 in the spent resin is about from 0.4 to $1,321\;GBq/m^3$. So it could be a problem, when dispose of at a repository, since there is a disposal limit of $222\;GBq/m^3$. This means we should develop the C-14 removal technology.

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자성체 이온교환 수지와 PACI 응집에 의한 국내 주요 수계 내 자연유기물 제거 특성 및 막오염 저감 효과 (Effects of magnetic ion exchange resin with PACI coagulation on removal of natural organic matter and MF fouling)

  • 최양훈;정영미;김영삼;이승렬;권지향;권순범
    • 상하수도학회지
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    • 제22권1호
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    • pp.131-140
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    • 2008
  • The application of magnetic ion exchange resin($MIEX^{(R)}$) is effective for natural organic matter(NOM) removal and for control of the formation of disinfection byproducts(DBPs). NOM removal is also enhanced by adding $MIEX^{(R)}$ with coagulant such as polyaluminium chloride(PACl) in conventional drinking water treatment systems. In the application of $MIEX^{(R)}$, it is important to understand changes of NOM characteristics such as hydrophobicity and molecular weight distributions with $MIEX^{(R)}$ or $MIEX^{(R)}$+coagulant treatment.To observe characteristics of NOM by treatment with $MIEX^{(R)}$ or $MIEX^{(R)}$+coagulant, four major drinking water sources were employed. Results showed that the addition of $MIEX^{(R)}$ to coagulation significantly reduced the amount of coagulant required for the optimum removal of dissolved organic matter(DOC) and turbidity in the all four waters. The DOC removal was also increased approximately 20%, compared to coagulant treatment alone. The process with $MIEX^{(R)}$ and coagulant showed that complementary removal of hydrophobic and hydrophilic fraction of DOC. The combined processes preferentially removed the fractions of intermediate (3,000-10,000 Da) and low (< 500 Da) molecular weight. The microfiltration test showed that membrane cake resistance was decreased for waters with flocs from $MIEX^{(R)}$+coagulant. A porous layer was formed to $MIEX^{(R)}$ on the membrane surface and the layer consequently inhibited settling of coagulant flocs, which could act on a foulant.

2-비닐피리딘계 이온교환수지의 합성과 그의 이온교환능 (Synthesis and Ion Exchange Capacity of 2-Vinylpyridine Series Ion Exchange Resins)

  • 김동원;송해영
    • 대한화학회지
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    • 제25권3호
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    • pp.160-165
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    • 1981
  • 2-비닐피리딘계의 세가지 종류의 고분자물질을 합성하여 그들의 구조를 적외선 흡수 스펙트럼으로 확인한 결과, 2-비닐피리딘-디비닐벤젠의 삼중합체임을 알 수 있었다. 또한 2-비닐피리딘-아세트산비닐-디비닐벤젠의 삼중합체는 $98{\circ}C$에서 50분간 반응시킬 때 가장좋은 수율을 나타냈다. 특히 합성된 삼중합체중, 2-비닐피리딘-비닐알코올-디비닐벤젠과, 2-비닐피리딘-인산비닐-디비닐벤젠은 2-비닐피리딘-아세트산비닐-디비닐벤젠보다 큰 이온교환용량을 가지며, 2-비닐피리딘-비닐알코올-디비닐벤젠과 2-비닐피리딘-인산비닐-디비닐벤젠의 이온교환용량은 각각, 3.69 meq/g 및 5.38 meq/g이었다. 마지막으로 Mg(Ⅱ), Co(Ⅱ) 및 Cd(Ⅱ)금속이온에 대한 흡착능을 알아보았다.

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이온교환수지를 이용한 식물유지의 전처리 및 바이오디젤 생산 (Pretreatment of Vegetable Oil Using Ion-exchange Resin and Biodiesel Production)

  • 홍연기;허윤석;홍원희;오성우
    • 청정기술
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    • 제13권2호
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    • pp.104-108
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    • 2007
  • 바이오디젤은 식물성 또는 동물성 유지를 알콜과 화학적으로 반응하여 얻어진 지방산 알킬에스터로서 친환경적인 대체에너지로 주목받고 있다. 본 연구에서 폐식용유와 유채유에 대한 전처리 공정에 고체 산(acid)이온 교환수지를 도입하여 자유지방산을 제거함으로써 바이오디젤로의 전환율을 높이고자 하였다. 이온교환수지를 이용한 전처리를 통해 자유지방산의 90%이상을 제거할 수 있었으며 젖은 상태의 수지보다 건조 상태의 수지의 자유지방산 제거효율이 높은 것으로 나타났다. 전이에스테르화를 통해 최대 98%의 수율로 지방산 메틸에스터를 얻을 수 있었으며 본 연구 결과는 자유지방산의 제거가 필요한 바이오디젤 원료유의 전처리에 효과적으로 적용될 수 있다.

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이온교환수지탑을 이용한 Fructo-oligosaccharides의 분리 및 정제 (Separation and Purification of Fructo-oligosaccharides by an Ion-Exchange Resin Column)

  • 윤종원;송승구
    • KSBB Journal
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    • 제9권1호
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    • pp.35-39
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    • 1994
  • 강산성 양이온 교환수지를 이용하여 설탕, 포도당이 혼존되어 있는 fructo-oligosaccharides 시럽으로부터 순수한 fructo-oligosaccharides를 분리정제하였다. 분리 조건을 최적화한 결과, 수지탑 운전온도 $80^{\circ}C$, 유속 $0.25h^{-1}$이었으며, 수지탑의 높이와 직경의 비율은 25 이상에서 효과적이었다. 최적 조건에서 4회 분리를 수행한 결과, 분리율은 66%이었으며, 제품의 순도는 96%이었다. 분리된 fructo-oligosaccharides 용액은 양이온 교환수지와 음이온 교환수지가 함께 충전된 혼상 수지탑을 이용하여 염과 색소를 동시에 제거한 후 농축하여 최종제품을 제조하였다.

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