• 한국환경과학회지
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• 제18권12호
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• pp.1411-1416
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• 2009

Several adsorbents were tried to remove the selenium ions from industrial wastewater and the following ascending order of the adsorption performance for the selenium at pH 9 was observed: cation exchange resin < chelate resin < zeolite < brown marine algae < granular activated carbon < anion exchange resin. Initial concentration of selenium(146 mg/L) in industrial wastewater was reduced to 63 mg/L of selenium at pH 9 by neutralization process. The maximum uptake of Se calculated from the Langmuir isotherm with anion exchange resin was 0.091 mmol/g at pH 10 and that with granular activated carbon was 0.083 mmol/g at pH 6. The affinity coefficients of Se ion towards anion exchange resin and granular activated carbon were 3.263 L/mmol at pH 10 and 0.873 L/mmol at pH 6, respectively. The sorption performance of anion exchange resin at the low concentration of Se, namely, was much better than that of granular activated carbon. The Se ions from industrial wastewater throughout neutralization process and two steps of adsorption using anion exchange resin was removed to 97.7%.

• 한국건축시공학회:학술대회논문집
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• 한국건축시공학회 2018년도 추계 학술논문 발표대회
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• pp.23-24
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• 2018

Reinforced concrete is a building material that is generally used in modern society. Also, reinforced concrete structures in high salinity environments have low durability due to corrosion of reinforcing bars due to infiltrated chlorine ions. Anion exchange resins have an ability to immobilize chlorine ions in the resin while releasing their anions. As a material, it has already been shown that it is possible to fix the chloride ion inside the cementitious material through the cement mortar experiment. The purpose of this study is to confirm the compressive strength of cement mortar using powdered anion exchange resin after powdering an anion exchange resin. In order to confirm the chloride ion fixation ability of the powder anion exchange resin, chlorine ion penetration resistance test was carried out.

• 한국환경과학회지
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• 제7권1호
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• pp.89-95
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• 1998

Ion exchange performance to remove nitrate in water was studied using commercially available strong base anion exchange resin of Cl- type in the batch and continuous column reactors. The performance was tested using the effluent concentration histories for continuous column or equilibrium conquilibrium between resin and solution. Anion exchange resin used in this study was more effective than activated carbon or zeolite for nitrate removal. With large resin amount or low initial concentration, nitrate removal characteristics for a typical gel-type resin was Increased. On considering the relation between the breakthrough capacity and nitrate concentration of the influent, the use of anion exchange resin were suitable for the hi선or order water treatment. The nitrate removal of above 90% could be possible until the effluent of above 650 BV was passed to the column. Thus, the commercially available strong base anion exchange resin of $Cl^-$ type used in thins study could be effectively used as economic material for treatment of the groundwater. The breakthrough curves showed the sequence of resin selectivity as $SO_4^{2-}$ > $NO_3$ > $NO^{2-}$ > $HCO_3^-$. The results of this study could be scaled up and used as a design tool for the water purification system of the real groundwater and surface water treatment processes.

• 환경위생공학
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• 제12권1호
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• pp.15-23
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• 1997

The anionic exchange resins with the Dowex-1 and Amberlite CG-400 form were transformed into resin of sulfate and acetate acid form, respectively. The uranyl complex ions with SO$_{4}$$^{2-}$ and CH$_{3}$COO$^{-}$ were adsorbed on the anion exchange resion mentioned above, and these complex ions were eluted as mixture eluents of 0.7M HNO$_{3}$ - 0.5M NH$_{4}$NO$_{3}$ by anion exchange chromatography. The optimum adsorption conditions of uranyl anion complex ions adsorbed on the upper of the resin colmun were 1.5-2.0 ml/min of flow rates at pH 2.0 and adsorptive power of uranyl complex ion of sulfuric acid type were nearly consistent with the Caussion normal distribution curve, whereas the elution state of UO$_{2}$(Ac)$_{2}$$^{4-}$ with acetic acid type was departed. The weighing form obtained from resin of sulfuric acid and aceric acid type was U$_{3}$O$_{8}$ whose recovery was 91.7%. The possibility of recovering uranium from the monazite sulfate solution using a strong base anion resin, Amberlite CG-400(sulfate form), was successfully recovered more than 90%.

• 한국환경과학회지
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• 제18권6호
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• pp.595-601
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• 2009

The effects of the cation-to-anion resin ratio and bed depth on ion exchange performance of mixed-bed were studied at ultralow solution concentration. Breakthrough curves were experimentally obtained for NaCI solution as functions of resin ratio and bed depth. The bed depth affects the pattern of the sodium breakthrough curve but not the chloride breakthrough curve in beds because of the selectivity difference. Resin selectivity determines the shape of breakthrough curves, Some sodium and chloride breakthrough curves crossed at a point as a function of resin ratio. The lower cation-to-anion resin ratio showed the higher effluent concentration or treated volume of the crossover point regardless of the total resin weight.

• Nuclear Engineering and Technology
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• 제40권6호
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• pp.489-496
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• 2008

Ferrocyanide-anion exchange resin was prepared and the prepared ion exchange resins were tested on the ability to uptake $Cs^+$ ion. The prepared ion exchange resins were resin-KCoFC, resin-KNiFC, and resin-KCuFC. The three tested ion exchange resins showed ion exchange selectivity on the $Cs^+$ ion of the surrogate soil decontamination solution, and resin-KCoFC showed the best $Cs^+$ ion uptake capability among the tested ion exchange resins. The ion exchange behaviors were explained well by the modified Dubinin-Polanyi equation. A regeneration feasibility study of the spent ion exchange resins was also performed by the successive application of hydrogen peroxide and hydrazine. The desorption of the $Cs^+$ ion from the ion exchange resin satisfied the electroneutrality condition in the oxidation step; the desorption of the $Fe^{2+}$ ion in the reduction step could also be reduced by adding the $K^+$ ion.

• 한국산학기술학회논문지
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• 제7권4호
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• pp.727-732
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• 2006

본 연구에서는 전해질 성분 및 농도, 이온교환 수지 조성비율을 통해 이온교환 수지탑의 성능을 평가하고, 이온교환 수지에 의한 입자성 물질 제거의 능력과 입자성 물질이 이온교환 특성에 미치는 영향을 조사하였다. 이온교환 수지탑 배열 순서에 따라 파과(돌파)시점이 연장되며, 파과(돌파)순서는 음이온의 경우 $Cl^{-}, 양이온의 경우 $Na^{+} 순 이였으며, 전해질의 농도가 증가할수록 파과시간이 단축되었다. 이온교환 수지의 조성비 변화에서는 양음이온교환 수지 조성비가 1:2의 경우 1:1및 1:3의 경우보다 파과(돌파)시간이 연장되었으며 동일한 전해질 농도에서 입자 농도가 증가하면 20% 미만으로 파과(돌파)시간이 단축되었다. 양이온 교환수지 비율이 높으면 양이온의 파과(돌파)시점이 늦어져 이온교환 수지탑의 수명이 연장되고, 입자성 물질은 전해질 농도와 무관하게 이온교환 수지의 세공을 막아 이온교환 용량을 감소시켜 파과(돌파)시간을 단축시키는 것으로 조사되었다.

• Bulletin of the Korean Chemical Society
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• 제23권12호
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• pp.1819-1822
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• 2002

• 분석과학
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• 제18권6호
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• pp.469-474
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• 2005

본 연구에서는 음이온 교환수지와 Sr-Spec 수지를 사용하여 토양중 $^{90}Sr$, $^{241}Am$ 및 Pu 동위원소들에 대하여 축차적으로 분리하는 정량법을 제시하였다. 플루토늄은 음이온 교환수지를 이용하여 분리하였고, 아메리슘 및 스트론튬은 옥살산 공침법 및 Sr-Spec 수지를 사용하여 순수 분리하였다. Pu 및 Am 동위원소는 알파 스펙트로메트리법으로 정량하였고, Sr-90은 액체섬광계수기를 사용하여 정량하였다. 본 연구에서 고찰된 $^{90}Sr$, $^{241}Am$ 및 Pu 동위원소 분석법을 IAEA 기준시료에 적용하여 분석법의 타당성을 검증하였다.

• 대한환경공학회지
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• 제34권3호
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• pp.162-167
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• 2012

$Cl^-$ 형태의 음이온 교환 수지를 이용하여 오쏘인산 이온의 제거에 관한 연구를 수행하여, 오쏘인산의 형태에 따른 이온 교환 메커니즘을 살펴보았다. 또한, 알칼리도의 영향 및 타 이온의 영향을 조사하였다. 유입수에 포함된 오쏘인산 이온의 산화수가 2와 3인 화학종($HPO{_4}^{2-}$ and $PO{_4}^{3-}$)의 경우, 이온 교환 반응을 통해 완전히 제거되었으나, 1가 화학종($H_2PO_4{^-}$)인 경우는 음이온 교환 수지에 대한 친화도가 $Cl^-$ 이온과 경쟁적으로 작용하여 부분적인 제거만 이루어졌다. 이온 교환 반응을 거친 유출수의 pH는 유입수에 포함된 오쏘인산 이온의 당량에 해당하는 $Cl^-$ 이온이 유출수에 포함된 것을 근거로 계산한 수치에 비해 상당히 낮은 pH 값을 나타내었다. 이는 1가 이온은 2가 이온으로, 2가 이온은 3가 이온으로 변환되어 이온 교환되었기 때문으로 해석할 수 있었다. 알칼리도가 증가할 경우, pH 강하는 최소화되었다, 알칼리도가 100 mg/L ($CaCO_3$) 이상일 경우, 100 mg/L의 오쏘인산 이온($H_2PO_4{^-}$ 이온 포함)을 용액에서 모든 오쏘인산 이온이 제거되었다. 수용액에 포함된 $SO{_4}^{2-}$와 $NO_3{^-}$ 이온은 오쏘인산 이온과 함께 제거가 되었으며, 이에 해당하는 만큼 이온 교환 용량이 감소되었다.