• Bulletin of the Korean Chemical Society
• /
• 제22권6호
• /
• pp.559-564
• /
• 2001

A method for calculating the main characteristics of a potentiometric titration curve in a carboxylic ion exchanger has been investigated. The potentiometric titration curves of simple electrolyte and ion exchangers (polyelectrolytes) showed a great difference between them. The acidity parameters of the ion exchangers, the thermodynamic constant (pK0), apparent equilibrium constant (K), and correction for the apparent equilibrium constant (b), were introduced and used to express the characteristics of the carboxylic ion exchanger. A characteristic equation related to the acidity parameters of the ion exchangers systems was derived. A fibrous carboxylic cation exchanger was used and potentiometric titration curves at different concentrations of the supporting electrolyte were obtained . To prove the validity of the characteristic equation, the concentration of the supporting electroyte was varied. In the present study, good agreement between the data points and the fitted curves was found in all the cases. The g (number of moles of alkali to 1 g of ion exchanger) of carboxylic ion exchanger was calculated from the concentration of supporting electrolyte (C), pH of the solution, and degree of neutralization of ion exchanger (x).

• 폴리머
• /
• 제26권5호
• /
• pp.575-581
• /
• 2002

본 연구는 폴리에틸렌 기재에 비드와 섬유상 이온교환체의 배합비를 달리하여 불균질 이온 교환막을 제조하였다. PE 불균질 이온교환막의 이온교환능은 섬유강 이온교환체의 양이 증가할수록 선형적으로 증가하였으며 30 wt%에서 최대 1.86 meq/g 이었다. 불균질 이온교환막의 함수율, 고정이온농도 및 이온운반율도 섬유상 이온교환체의 양이 증가할수록 증가하였나. 반면 불균질 이온교환막의 전기저항은 섬유상 이온교환체의 양이 증가할수록 감소하였으며, IXF (ion exchange fiber)의 혼합량이 30 wt%에서 5$\Omega$/$\textrm{cm}^2$으로 전기저항 값이 가장낮았다.

• 한국환경과학회지
• /
• 제11권9호
• /
• pp.993-999
• /
• 2002

Waste paper cup was sulfonated to be used as ion exchanger. Removal characteristic of copper and lead ion by prepared ion exchanger was investigated. The sulfonation was conformed by the high intensity band of $SO_3H$ group around 1100~$1160cm^{-1}$. The synthesized ion exchanger had greater removal ability for copper and lead ion than the original waste paper cup. Ion exchange system reached the final equilibrium plateau within 30min. The maximum removal capacities $q_{max}$ were calculated as 9.79mg/g fur copper and 15.95mg/g for lead, respectively. The affinity of lead based on a weight was higher than that of copper. The ion exchange phenomena appeared to follow a typical Freundlich isotherm.

• Bulletin of the Korean Chemical Society
• /
• 제22권5호
• /
• pp.503-506
• /
• 2001

Separation of lithium isotopes was investigated by chemical ion exchange with a hydrous manganese(IV) oxide ion exchanger using an elution chromatography. The capacity of manganese(IV) oxide ion exchanger was 0.5 meq/g. One molar CH3COO Na solution was used as an eluent. The heavier isotope of lithium was enriched in the solution phase, while the lighter isotope was enriched in the ion exchanger phase. The separation factor was calculated according to the method of Glueckauf from the elution curve and isotopic assays. The single stage separation factor of lithium isotope pair fractionation was 1.021.

• 한국유체기계학회 논문집
• /
• 제2권4호
• /
• pp.40-47
• /
• 1999

A hot water layer (HWL hereinafter) was installed at the depth of 1.2 m from the pool surface to reduce the radiation level at the pool top. After the HWL system was improved by the replacement of the filter with the Ion Exchanger to capture the Na-24, to purify the pool water of HWL and finally to reduce the radiation at the pool top. It was confirmed by the performance test of the pump and the measurement of the pressure difference through the Ion Exchanger and the strainer, that the flow characteristics of HWL system was not adversely affected after the system modification. Also the flow analysis using the pressure loss coefficients of the Ion Exchanger and strainer, calculated by the Darcy formula, could predict the flow variations by pressure changes within $10\%$ error in comparison with the field test results. It was also confirmed that HWL was maintained with the depth of 1.2 m from the pool surface because each electric water heater was electrically and thermodynamically maintained at 30 kW and the temperature of HWL was maintained with $5^{\circ}C$ higher temperature than that of pool water. Finally, it was confirmed that the pool top radiation was saturated and stabilized below 10000 nG/hr within 24 hours as the ion exchanger captured the main nucleus, Na-24 and purified the pool water of HWL.

• 대한화학회지
• /
• 제37권9호
• /
• pp.820-825
• /
• 1993

새로운 HDBPDA 이온교환체, {(4,5) : (13,14)-dibenzo-6,9,12-trioxa-3,15,21-triazabicyclo[15.3.l]heneicosa-(1,17,19)(18,20,21) triene ion exchanger: HDBPDA ion exchanger}의 이온교환용량은 3.8 meq/g이었다. 그리고 이 이온교환체에 대한 알칼리 및 알칼리토금속 이온들의 분포계수를 물과, 여러 농도의 염산용액중에서 측정하였다. 금속이온들의 분포계수는 염산농도의 영향을 거의 받지 않았으나, 대체적으로 염산의 농도가 감소할수록 점진적으로 약간 증가하는 경향을 보였다. 그리고 물속에서의 분포계수가 가장 컸다. HDBPDA 이온교환체를 사용하여 알칼리 및 알칼리토금속 이온들을 컬럼이온교환크로마토그래피로 분리하였으며, 이때 용리액으로 물을 사용하였다. 또한 알칼리 및 알칼리토금속 이온들의 분포계수는 그들 이온들의 이온반경이 증가함에 따라 증가하였다.

• 분석과학
• /
• 제6권3호
• /
• pp.261-265
• /
• 1993

새로운 DBPDA이온교체, {(4,5):(13,14)-dibenzo-6, 9, 12-trioxa-3, 15, 21-triazabicyclo [15.3.1] heneicosa-1(21), 17, 19-triene-2, 16-dione : DBPDA 이온교환체}의 이온교환용량은 4.2meq/g이었다. 그리고 이 이온교환체에 대한 알칼리 및 알칼리 토금속 이온들의 분배계수를 여러 농도의 염산용액 중에서 측정하였다. 또한 DBPDA 이온교환체를 사용하여 알칼리 및 알칼리 토금속 이온들을 이온교환 컬럼 크로마토그라피로 분리하였다. 이러한 결과로부터 알칼리 및 알칼리 토금속 이온들의 분배계수에 미치는 용액의 pH와 금속 이온들의 이온반경 효과를 고찰하였다.

• 한국연초학회지
• /
• 제26권2호
• /
• pp.159-167
• /
• 2004

This work has been conducted to select appropriate filter materials for removing carbonyl compounds in mainstream tobacco smoke. To investigate of the usability of this filter materials, two types of bead ion exchangers were synthesized and their adsorption characteristics for carbonyl compounds were investigated. Sulfonic acid group-containing cation exchanger and ammonium group-containing anion exchanger were synthesized by the suspension polymerization of glycidylmethacrylate(GMA) and divinylbenzene(DVB) followed by the subsequent functionalization, respectively. The removal efficiency of carbonyl compounds by these two ion exchangers increased in the presence of moisture. However, the amount of carbonyl compounds adsorbed on the anion exchanger was larger than that on the cation exchanger under two levels of water contents tested. This phenomenon seems to arise from the electron delocalization in carbonyl group of the anion exchangers. There was not any significant relationship between the amount of carbonyl compounds adsorbed on ion exchangers and the length of adsorption column. From the large ion exchange capacity and rapid ion exchange reaction rate of the anion exchanger, it is suggested that the anion exchanger may be a good filter material for removing carbonyl compounds in the mainstream tobacco smoke.

• 상하수도학회지
• /
• 제27권1호
• /
• pp.121-128
• /
• 2013

The concern for dissolved phosphate in water/wastewater has been increasing because of the risk for eutrophication. A variety of conventional and advanced technologies were applied to meet the enforced new regulation of phosphate around the world. However, there still remained a lot of challenge because most introduced/developed method, for example, biological and physic-chemical treatment is not easy to satisfy the new regulation of phosphate in water. In order to meet the new regulation, the application of ion exchanger has been tried which showed that the removal efficiency for phosphate was strongly determined by in the presence of the competing ion, especially sulfate. As results, a new class of ion exchanger governed by ligand exchange was developed and investigated to increase the selectivity for phosphate. The current study using organic/inorganic anion exchanger developed with Lewis acid-base interaction confirms the selectivity for phosphate over sulfate. According to isotherm test and column test, the value of the maximum phosphate uptake (Q) showed 64 mg/g as $po{_4}^{3-}$ and the breakthrough for phosphate occurs after 1000 min and completely finishes at 2500 min, respectively.

• 전기화학회지
• /
• 제15권4호
• /
• pp.256-263
• /
• 2012

본 연구에서는 전기화학적 이온교환체 중의 하나인 nickel hexacyanoferrate($KNiFe(CN)_6$) 막 전극을 사용하여 세슘 양이온을 분리하는 실험을 수행하였다. 1.0M $NaNO_3$와 1.0M $CsNO_3$의 단일성분계 및 이성분계 수용액에서 순환전위곡선을 측정하여 전극전위, 전류, 전기량의 변화 거동을 조사하였으며, 실험 전과 후에 $KNiFe(CN)_6$ 막의 구조 형태와 원자조성의 변화를 각각 SEM과 EDS 분석을 통하여 조사하였다. 또한 나트륨과 세슘 용액에서 교대로 이온교환 반응을 수행하여 측정한 순환전위곡선과 원자조성으로부터 $KNiFe(CN)_6$의 이온 선택성을 조사하였다. 본 연구의 실험 결과에 의하면, 전기를 인가한 $KNiFe(CN)_6$ 이온교환체는 화학적 유 무기물 이온교환체에 비해 약 40배 이상의 우수한 내구성을 가짐을 알 수 있었다. 또한 $KNiFe(CN)_6$ 이온교환체는 나트륨보다 세슘에 대해 보다 높은 선택도를 가짐을 확인할 수 있었다.