• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.7 no.4
• /
• pp.727-732
• /
• 2006

The object of this study was to investigate the influence of composition and concentration of electrolyte, ratio of cation to anion exchange resin of mixed ion exchange column in the performance of ion exchange. Also this work examined the removal capability of suspended solids by ion exchange resin and the effect of particule on the characteristics of ion exchange. Breakthrough time was extended as the amount of ions and particles present in liquid was decreased. The case of anion, the breakthrough sequence is $Cl^{-}, but the case of cation, the breakthrough sequence is $Na^{+}. As for the ratio of cation to anion exchange resin of 1:2, the breakthrough time was prolonged compared with that of 1:1 and 1:3. For the electrolyte of equal concentration containing suspended solid, breakthrough time was contracted less than 20%. It results in the increase in the removal capacity of cation exchange resin. For the higher ratio of cation exchange resin, suspended solids are shorten the cation's breakthrough time so that the runtime of ion exchange resin tower is increased.

• Applied Chemistry for Engineering
• /
• v.27 no.6
• /
• pp.633-638
• /
• 2016

In this study, we used three kinds of commercially available cation, anion, and mixed-ion exchange resins to separate radioactive ions from a polluted water containing Cs, I, and other radioactive ions. The experiment was conducted at a room temperature with a batch method, and a comparative analysis on the decontamination ability of each resin for the removal of Cs and I was performed by using different quantities of resins. The concentration was analyzed using ion chromatography and the ion exchange resin product from company D showed an overall high ion exchange ability. However, for most of the experiments when the amount of ion exchange resin was decreased, the decontamination ability of the resins against mass increased. When the mass of company D's cation exchange resin was small, the ion exchange ability against Cs and I ions were measured as 0.199 and 0.344 meq/g, respectively. When the mixed ion exchange resin was used, the ion exchange ability against I ions was measured as 0.33 meq/g. All in all, company D's ion exchange resins exhibited a relatively higher ion exchange ability particularly against I ions than that of other companies' exchange ions.

• Proceedings of the KAIS Fall Conference
• /
• 2006.05a
• /
• pp.599-601
• /
• 2006

본 논문에서는 용액의 농도가 이온교환 특성에 미치는 영향을 조사하기 위하여 농도는 $Na^+\;50$, 125, 250ppm, $Cl^-\;165$, 315, 610ppm, 입자성 물질의 유입 농도 0ppm, 유속 500ml/min, 이온교환 수지는 ROHM&HAAS IR 120 양이온 수지와 ROHM&HAAS IRA 402 음이온 수지를 사용하였다. 수지탑 배열은 혼상-혼상-음이온 수지탑 순으로, 이온교환 수지탑의 양 음이온교환 수지의 조성 비율은 1:2 로 실험한 결과 이온교환 수지탑 성능은 유입 용액 성분 및 농도에 영향을 받는 것으로 나타났다. 이온교환 수지탑 배열 순서에 따라 파과시점이 연장되며, 파과순서는 음이온의 경우 $Cl^-\;<\;NO_3\;^-\;<\;F^-$, 양이온의 경우 $Na^+\;<\;K^+\;<\;Ca^{2+}$ 순 이였으며, 용액의 농도가 증가할수록 파과시간이 단축되었다.

• Proceedings of the Korean Environmental Sciences Society Conference
• /
• 2006.05a
• /
• pp.278-279
• /
• 2006

본 연구에서는 수중 silica 제거에 이온교환수지의 성능이 실험되었다. 음이온 단일수지에 비해 양이온/음이온 혼합수지가 silica제거에 효과적이었고, 혼합수지에서 온도가 높을수록 교환반응속도는 빨랐다. 음이온과 양이온교환능은 용액의 pH를 변화를 측정하여 해석할 수 있었다. 용액에 공존하는 양이온인 $Na^+$는 혼합수지에서 pH변화에 영향을 주는 물질이었고, 이러한 pH의 변화는 silica의 제거능에 영향을 주었다. 각 온도에서 도달된 평형농도로부터 각 수지에 대한 silica의 선택도계수가 측정되었다.

• Proceedings of the KAIS Fall Conference
• /
• 2006.05a
• /
• pp.596-598
• /
• 2006

본 논문에서는 수지 조성비 및 수지탑 배열이 이온교환 특성에 미치는 영향을 조사하기 위하여 전해질 농도는 $Na^+\;125ppm$, $Cl^-\;315ppm$ 유속은 500ml/min, 이온교환 수지는 ROHM&HAAS IR 120 양이온 수지와 ROHM&HAAS IRA 402 음이온 수지를 사용하였고, 수지탑 배열은 혼상-혼상-음이온, 혼상-음이온-혼상, 음이온-혼상-혼상 수지탑 순으로, 이온교환 수지탑의 양 음이온교환 수지의 조성 비율은 1:1, 1:2, 1:3 로 변화하여 실험한 결과 이온교환 수지의 조성비 변화에서는 양 음이온교환 수지 조성비 1:2의 경우 1:1, 1:3의 경우보다 파과시간이 연장되었다. 수지탑 배열이 음이온-혼상-혼상 수지탑인 경우 혼상-혼상-음이온 수지탑 배열과 파과시간을 비교해보면 약 60% 파과시간이 연장되었다. 따라서 수지탑 배열은 음이온-혼상-혼상 수지탑 순으로, 수지 조성비는 1:2일 때 가장 효율적인 것으로 나타났다.

• Applied Chemistry for Engineering
• /
• v.10 no.2
• /
• pp.206-211
• /
• 1999

Mixed-bed ion exchange performance was studied experimentally with variations of cation to anion resin ratio, resin weight and temperature at ultralow sodium chloride solution concentrations of less than $1.0{\times}10^{-4}M$. Analyzing the effluent concentration histories the performance test was examined as a function of tested solution volume for a laboratory-scale continuous flow column until both the cation and anion-exchange resins were exhausted. Initial leakage was observed for both cation and anion breakthrough curves, but serious at cation breakthrough curve because of low selectivity coefficient. The slope of breakthrough curve was affected by selectivity coefficient and temperature. The slope of anion breakthrough curve was steep because of the large selectivity coefficient, and ion exchange rates increased as temperature increased. The temperature effect decreased as the total volume was increased or as the resins were exhausted.

• Proceedings of the KAIS Fall Conference
• /
• 2002.05a
• /
• pp.137-139
• /
• 2002

이온교환은 액체상 이온과 고체상 이온간의 화학반응이며 연수 및 탈염공정, 특정물질의 제거 및 회수, 토양을 통한 이온성 물질의 이동에서 널리 이용되고 있다. 이온교환수지는 이온교환시 원자가가 높을수록, 수화반경이 작을수록, 이온농도가 낮을수록 증가한다. 본 연구는 이온교환수지에 대한 평형실험을 선택도가 칼럼실험에 적용되는지 조사하였다. 이 실험치 결과에서 음이온 교환수지의 선택도 순서는 OH/sup -/ < F/sup -/ < HCO₃/sup -/ < Cl/sup -/ < Br/sup -/ ≤ No₃/sup -/ < So₄/sup 2-/ 이였으며, 음이온 칼럼 교환도 동일하였다. 또한 바탕 양이온의 가수가 높을수록 이온교환이 빠르게 진행됨을 알 수 있다.

• Korean Journal of Food Science and Technology
• /
• v.27 no.3
• /
• pp.313-317
• /
• 1995

Ion exchange process was optimized to purify ultrafiltrated bean cooking water(BCW) for the production of soy-oligosaccharides. The ultrafiltrated BCW with cutoff MW(COMW) 20,000 membrane was treated with various ion exchange resins. Protein and ash were mostly removed by anion and cation exchange resins, respectively. Based upon removing capabilities for ash and protein, a cation exchange resin(SK1B) and an anion exchange resin(WA30) were selected. Protein and ash were more efficiently removed at low extract/resin ratios(ERR), but part of the oligosaccharides were concomitantly lost. When 2-step-ultrafiltrated BCW first with COMW 20,000 membrane and successively with COMW 5,000 membrane was treated with a mixed resin(SK1B : WA30 =1 : 2) at ERR 5.0, most oligosaccharides were recovered in a clear protein- and ash-free liquid.

• Journal of the Korea Academia-Industrial cooperation Society
• /
• v.4 no.3
• /
• pp.307-311
• /
• 2003

The test did for the determine the optimized ratio of cation to anion in mixed ion exchange demineralizers. Binary, ternary, quaternary, and quinary cation and anion adsorption was performed to develop a comprehensive experimental data set from small-volume batch tests to obtain the selectivity coefficients of many cations and anions. The quantitative run time might be estimated by such ion exchange models as semi-empirical mass action and surface complexation models. The demineralizer can be used longer by increasing the ratios of cation to anion exchange resins in the bed.

• Applied Chemistry for Engineering
• /
• v.10 no.1
• /
• pp.51-57
• /
• 1999

Adsorption characteristics of Ni(II), Co(II) and Ag(I) ions on the Amberite IRN 77 cation exchange resin have been studied to suggest the guide-line for the optimum operation of demineralization process in primary coolant system during the shut-down period of pressurized water reactor(PWR). The adsorption mechanism of each metal ion, Ni(II), Co(II) or Ag(I) ion, on a cation exchange resin was well coincided with Langmuir isotherm. The adsorption and treatment capacities of $H^+$-form resin were higher than those of $Li^+$-form resin. In the continuous ion exchange process for the solution of multi-component system, the selectivity of the resin was in increasing order of Ni(II)${\approx}$Co(II)>Ag(I). In addition, the increase of the flow rate decreased the treatment capacity of the resin as well as the slope of the breakthrough curve.