• 분석과학
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• 제14권5호
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• pp.416-421
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• 2001

수소화물 발생 유도결합 플라스마 원자 방출 분광법으로 주석을 분석할 때 연속 흐름 수소화물 발생 장치에 사용되는 환원제 및 산의 농도에 대하여 최적조건을 확립하였다. 시료에 함유되어 있는 플루오르화 이온이 주석의 수소화물 발생을 방해하는 영향과 이러한 영향을 최소화하기 위한 여러 가지 예비환원제를 비교 실험하였다. 환원제 및 안정제의 농도가 $NaBH_4$ 1~2%/NaOH 1.0 M인 조건에서 우수한 수소화물을 발생시키는 산농도는 0.5~1.0 M 이었으며, 또한 플루오르화 이온의 방해영향이 매우 크게 관찰되었지만 boric acid 및 L-cysteine의 혼합용액은 이런 영향을 최소화하여 가장 효과적인 주석의 수소화물 발생 보조제로 확인되었다. 플루오르화 이온이 함유되어 있는 용액에서 미량의 주석을 분석하여 회수율이 100~108 %의 결과를 얻었다.

• 분석과학
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• 제8권2호
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• pp.187-193
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• 1995

N,N,N,N-Tetrabenzylethylenediamine 중성운반체를 이용하여 PVC 수소이온 선택성 막전극을 제조하였다. 가소제 종류(phthalates와 sebacate) 및 친지방성 첨가제(NaTPB)에 따른 막전극의 전기저항과 수소이온 감응범위 및 알칼리금속과 알칼리토금속의 존재하에서 방해효과를 조사하였다. 가소제 종류에 의한 전기저항은 영향을 거의 받지 않았고 NaTPB 0.7%의 경우 수소이온에 대한 Nernstian 기울기는 가장 이론값에 근접하였으며, 또한 알칼리금속 및 알칼리토금속에 의한 방해도 적게 받았다. pH-선택성 고분자 막전극은 pH 2~10 범위내에서 선형적이고, 산과 알칼리용액 중에서 안정성 및 재현성 시험 결과 매우 좋게 나타났다.

• 상하수도학회지
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• 제28권1호
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• pp.83-89
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• 2014

The aim of this study is to investigate the sorption/ion exchange of radioactive nuclides such as $Cs^+$ and $Sr^{2+}$ by synthetic Na-micas. In order to prepare Na-micas, two natural micas (phlogopite and biotite) were used as precursor materials. XRD, SEM, and EDS analyses were used to examine material characterization of synthetic Na-micas. Analyses of materials revealed that Na-micas were successfully obtained from natrual micas by K removal treatment. On the other hand, single solute (Cs or Sr) and bi-solute (Cs/Sr) sorption experiments were carried out to determine sorption capacity of Na-micas for Cs and Sr under different pH and ionic strength conditions. Uptake of Cs and Sr by micas in bi-solute system was lower than in single-solute system. Additionally, Langmuir and Langmuir competitive models were applied to describe sorption isotherm of Na-micas. bi-solute system was well described by Langmuir competitive models. For the results obtained in this study, Na-micas could be promising sorbents to treat multi-radioactive species from water and groundwater.

• 상하수도학회지
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• 제27권2호
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• pp.155-164
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• 2013

The main purpose of this research was to examine the adsorption/ion exchange characteristics of radioactive species such as cesium and strontium onto synthetic Na-birnessite (sodium-birnessite). As part of efforts to investigate the sorption behavior of cesium and strontium onto synthetic Na-birnessite, batch isotherm tests were performed under different experimental conditions. Na-birnessite was synthesized by the oxidation of $Mn^{2+}$ ions in sodium hydroxide solution. The synthetic Na-birnessite was characterized by powder x-ray diffraction (XRD), scanning electron microscopy (SEM), energy-dispersive x-ray spectroscopy (EDS), and Brunauer-Emmett-Teller (BET) surface area analysis. Cesium and strontium concentrations were determined by atomic absorption spectroscopy (AAS). The removal efficiency of strontium by Na-birnessite was around 95 % which was much higher than that of cesium (~ 32 %). The results imply that strontium has a higher affinity for Na-birnessite than cesium because strontium, divalent cation leads to larger electrostatic attraction than monovalent cesium.

• Bulletin of the Korean Chemical Society
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• 제13권3호
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• pp.317-324
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• 1992

Structure and dynamics of $Na^+$ ions are investigated by molecular dynamics simulations of rigid dehydrated zeolite-A at several temperatures using a simple Lennard-Jones potential plus Coulomb potential. A best-fitted set of electrostatic charges is chosen from the results of simulation at 298.15 K and Ewald summation technique is used for the long-ranged character of Coulomb interaction. The calculated x, y, and z coordinates of $Na^+$ ions are in good agreement with the positions determined by X-ray crystallography within statistical errors, their random movings in different types of closed cages are well described by time-correlation functions, and $Na_Ⅰ$ type ions are found to be less diffusive than $Na_Ⅱ$ and $Na_{III}$. At 600.0 K, the unstable $Na_{III}$ type ion pushes down one of nearest $Na_{I}$ ions into the $\beta-cage$ and sits on the stable site Ⅰ, and the captured ion in the $\beta-cage$ wanders over and attacks one of 8 $Na_{I}$ type ions.

• 멤브레인
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• 제34권1호
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• pp.58-69
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• 2024

역전기투석(reverse electrodialysis, RED)은 해수와 담수의 농도 차로부터 에너지를 얻는 이온교환막을 이용한 전기막 공정이다. 해수와 담수에 포함된 다가 이온은 이온교환막의 고정 전하 그룹에 강하게 결합하여 높은 저항을 유발하며 uphill transport를 통해 개방회로 전압과 전력 밀도를 저하시킬 수 있다. 본 연구에서는 RED 응용을 위해 1가 이온 선택성 및 전기화학적 특성이 우수한 세공충진 음이온교환막(pore-filled anion-exchange membrane, PFAEM)을 제조하였다. 제조된 막의 1가 이온 선택성은 3.65였으며 동일 조건에서 1.27의 선택성을 갖는 상용막(ASE, Astom Corp.)보다 우수한 수준을 나타내었다. 또한 제조된 막은 ASE 대비 낮은 전기적 저항 등 우수한 전기화학적 특성을 나타내었다. 0.459 M NaCl/0.0510 M Na₂SO₄의 해수와 0.0153 M NaCl/0.0017 M Na₂SO₄의 담수 조건에서 RED 성능을 평가한 결과 제조된 막을 적용하여 1.80 W/m²의 최대 전력 밀도를 얻었으며 이는 ASE 막 대비 40.6% 향상된 출력 성능이었다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제2권2호
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• pp.117-121
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• 1997

Glutamic acid can be crystallized inside cation exchange column when displacer NaOH concentration is high enough to concentrate displaced glutamic acid beyond its solubility limit. Resulting crystal layer of glutamic acid was moved with liquid phase through the column, and thus could be eluted from the column and recovered in fraction collector. For the purpose of enhancing crystal recovery, effects of operating parameters on the crystal formation were investigated. The increase in the degree of crosslinking of resin favored crystal recovery because of its low degree of swelling. Higher concentration of displacer NaOH was advantageous. If NaOH concentration is too high, however, crystal recovery was lowered due to the solubility-enhancing effects of high pH and ionic strength. The decrease of mobile phase flow rate enhanced crystal recovery because enough time to attain local equilibrium could be provided, but film diffusion would control the overall crystal formation with extremely low flow rate. Lower temperature reduced solubility of glutamic acid and thus favored crystal formation unless the rate of ion exchange was severely reduced. The ion exchange operated by displacement mode coupled with crystallization was advantageous in reducing the burden of further purification steps and in preventing purity-loss resulted from overlapping between adjacent bands.

• 한국표면공학회지
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• 제47권4호
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• pp.147-154
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• 2014

Formation behavior of PEO (Plasma Electrolytic Oxidation) films on AZ31 Mg alloy was studied in aqueous solutions containing various concentrations of hydroxide ion ($OH^-$) and silicate ion ($SiO_3{^{2-}}$) by voltage-time curves, and corrosion resistance of the PEO film-covered specimen was investigated by immersion test in 0.5 M NaCl solution. From the analyses of the voltage-time curves, it is suggested that two different types of anions are essentially needed for the formation of PEO films on AZ31 Mg alloy: film formation agent and local film breakdown agent. $SiO_3{^{2-}}$ ion acts only as a film formation agent but $OH^-$ ion acts not only as a film formation agent but also film breakdown agent. The PEO films prepared on AZ31 Mg alloy in alkaline silicate solution showed very good corrosion resistance without any pitting or filiform corrosions up to 480 h of immersion in 0.5 M NaCl.

• Bulletin of the Korean Chemical Society
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• 제12권3호
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• pp.265-270
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• 1991

Theoretical calculations on the stabilization energies of framework atoms in hydrolyses Co(Ⅱ )-exchanged zeolite A were made using some potential energy functions and optimization program. The protons which are produced by hydrolysis of $[Co(H_2O)_n]^{2+}$ ion in large cavity showed a tendency to attack the framework oxygen atom O(1) preferentially, and the oxygen atom O(4) within OH- ion was coordinated at Al atom. The weakness of bonds between T(Si, Al) and oxygen by attack of proton and too large coordination number around small aluminum atom will make the framework of Co(Ⅱ)-exchanged zeolite A more unstable. The stabilization energy of $Co_4Na_4$-A framework (- 361.57 kcal/mol) was less than that of thermally stable zeolite A($Na_{12-}$A: - 419.68 kcal/mol) and greater than that of extremely unstable Ba(Ⅱ)-exchanged zeolite A($Ba_{6-}$A: - 324.01 kcal/mol). All the data of powder X-ray diffraction, infrared and Raman spectroscopy of Co(Ⅱ)-exchanged zeolite A showed the evidence of instability of its framework in agreement with the theoretical calculation. Three different groups of water molecules are found in hydrated Co(Ⅱ )-exchanged zeolite A; W(Ⅰ) group of water molecules having only hydrogen-bonds, W(Ⅱ) group water coordinated to $Na^+$ ion, ans W(Ⅲ) group water coordinated to Co(Ⅱ) ion. The averaged interaction energy of each water group shows the decreasing order of W(Ⅲ)>W(Ⅱ)>W(Ⅰ).

• 한국환경과학회지
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• 제20권10호
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• pp.1337-1345
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• 2011

The removal performances of divalent heavy metal ions ($Pb^{2+}$, $Cu^{2+}$, $Cd^{2+}$, $Sr^{2+}$ and $Mn^{2+}$) were studied using the Na-P1 zeolite synthesized from Jeju scoria in the batch and continuous fixed column reactor. The uptakes of heavy metal ions by synthetic Na-P1 zeolite decreased in the order of $Pb^{2+}$ > $Cu2^{2+}$ > $Cd^{2+}$ > $Sr^{2+}$ > $Mn^{2+}$ based on the selectivity of each ion to ionic exchange site of Na-P1 zeolite for single and mixed solutions in batch or continuous fixed column reactor. For mixed solution, each heavy metal ion uptake was lower than that in single solution, and especially the uptake for $Mn^{2+}$ decreased greatly. In batch reactor, the uptakes of heavy metal ions by synthetic Na-P1 zeolite were described by Freundlich or Langmuir equation, but they followed the former better than the latter. In continuous fixed column reactor, the maximum ion exchange capacity obtained for each of heavy metal ions, was about 90----- of that in batch reactor. The uptakes of heavy metal ions by synthetic Na-P1 zeolite increased with the increase of initial heavy metal concentration and solution pH, and the decrease of the amount and particle size of synthetic zeolite.