• Proceedings of the Optical Society of Korea Conference
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• 2000.08a
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• pp.160-161
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• 2000

BK7 glass 기판에 Ag$^{+}$-$Na^{+}$ 이온교환법을 이용하여 Y-분리기를 제작하였다. Y-분리기는 하나의 입력으로 입사되는 광파워를 두 개의 출력단으로 분리하거나 합하는 기능을 수행하는 가장 기본적인 소자로서 이온 교환법을 이용하여 0.2dB/cm 이하의 전송손실을 유지할 수 있다. 또한 MMI (multimode interference)가 갖는 파장에 의존적인 동작 특성과는 달리 사용 파장에 덜 의존적으로 광 신호를 분기시킬 수 있다$^{(1-3)}$ . (중략)

• Journal of the Korea Convergence Society
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• v.7 no.1
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• pp.155-160
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• 2016

The convergence process utilized both leaching and ion exchange techniques has been investigated for the heavy metals removal in the abandoned mine of Chungyang Province, Korea. The contaminated soil samples by heavy metals from Samkwang mine were analysed by statistical analyses. The highly contaminated soils was initially separated by the flotation process. The selectivity indices were increased with increasing flotation reagents. The selectivity of separation was then improved by the use of both leaching and ion exchange processes in order to extract the heavy metals. The results of this study showed that the higher the sulfuric acid concentration, the leaching rate of heavy metals was increased. The lecheate then was removed by the ion exchange method. The anticipating results might imply that convergence process utilized both leaching and ion exchange techniques would somehow apply for the removal of heavy metals in the abandoned mine.

• Journal of Radiation Protection and Research
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• v.13 no.2
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• pp.52-56
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• 1988

An ion-exchange method for the detection of radioactivity in water using ion-exchange resin in concentrating radioactive nuclides was compared with an evaporation method. The loss of the radioactive materials in the sample treated by the ion-exchange method was less by about 20% than that by the evaporation method. In addition, the evaporation method needed about 20 hours for evaporating one liter of the sample at $70^{\circ}C$, while the ion-exchange method spent 6 hours to adsorb and adsorb the same amount of the sample on the resin. Consequently, the ion-exchange method is more effective than the evaporation method for the treatment of the radioactively contaminated water and is especially suitable for detecting the low-level radioactivity in water.

• Proceedings of the Korean Nuclear Society Conference
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• 1996.05d
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• pp.121-126
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• 1996

수소동위원소 교환반응에 이용될 수 있는 소수성 백금촉매를 개발하기 위하여, 담체로서 실리카라이트를 합성하였으며, 합성된 실리카라이트가 활성탄이나 ZSM-5보다 더 강한 소수성을 가지는 것을 보였다. 또한, 일반적인 함침법과 이온교환법을 이용하여 백금을 담지시켰으며, 여러가지 방법으로 처리하여 제조한 백금담지 실리카라이트 촉매의 백금분산도를 수소흡착법을 이용하여 측정하였다. 함침법에 의해 제조된 촉매의 백금분산도는 매우 낮았으며, 이온교환법에의해 제조된 촉매는 백금담지량은 적으나 분산도는 높음을 확인하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.10a
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• pp.130-132
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• 1998

정밀여과막(MF)막은 $0.1~1\mum$정도의 공경을 가지고 있는 막으로 산업이나 생활분야에서 널리 사용되고 있다. 이러한 정밀여과막에 이온교환기를 부여 시키므로써, 필요로하는 금속이온이나 단백질을 흡착할 수 있는 기능성 분리막이 제조 가능하다. 방사선프라프트 중합법은 고분자를 개질, 수식 또는 기능화시키는 수법으로 사용되고 있다. 본 실험에서는 방사선그라프트중합법을 사용하여 폴리에틸렌 정밀여과막에 에폭시기를 가지는 glycidyl methacrylate(GMA)를 그라프트 중합시킨 후 이온 교환기를 도입하여, 얻어진 막의 특성에 대해 고찰하였다. 본실험의 목적은 다음과 같다. (1) 폴리에틸렌 정밀여과 막에 방사선그라프트 중합법을 사용하여 이온교환기를 도입시키는 반응조건을 검토한다. (2) 도입된 이온교환기에 다른 막의 투과 성능을 조사한다. (3) 투과법에 의한 금속이온의 흡착성능을 조사한다. 여기서, 이온교환기로서는 술폰산(sodium sulfite:$SO_3H$)을 사용하였다.

• Proceedings of the Korean Vacuum Society Conference
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• 2013.02a
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• pp.285-285
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• 2013

수산화인회석(Hydroxyapatite, HAP)은 인체 내 뼈와 치아의 주성분으로서 칼슘과 인산염으로 구성된 물질이다. 암모늄을 이용하여 pH를 조절함으로서 hexagonal 형태의 HAP를 수열합성법으로 합성하였다. XRD pattern을 통하여 수산화인회석의 결정구조를 확인하였으며, 전이금속 중의 하나인 Fe(III) 이온을 이온교환반응을 통하여 수산화인회석 표면에 도입하였다. ICP 측정을 통해 Fe 함량을 정량하였고 SEM과 TEM image를 통하여 크기와 형태를 관찰하였다.

• Clean Technology
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• v.3 no.2
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• pp.28-30
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• 1997

발효 아미노산을 분리하는 기존의 공정인 이온교환법에서 폐액 및 폐수처리에 따른 문제점을 해결하기 위한 새로운 분리공정으로 탈염 전기투석과 Water-splitting Electrodiaysis를 이용한 발효 아미노산의 분리 가능성 및 다양한 cell configuration과 막에 대한 성능 실험을 실시하였다. 실험결과 전기투석에 의해 경도물질을 제거한 후 양이온교환막과 bipolar 막으로 구성된 2-compartment WSED로 효과적으로 발효액에서 아미노산을 분리 할 수 있었으나 1가 양이온에 선택성을 지닌 양이온교환막으로는 아미노산의 분리가 어려움을 알 수 있었다.

• Journal of Radiation Protection and Research
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• v.24 no.2
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• pp.73-86
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• 1999

The ion-exchange method for the purification of primary coolant has been used broadly in PWR(pressurized water reactor)-type nuclear power plants due to its high decontamination efficiency, simple system, and easy operation. However, its non-selective removal of metal and non-radionuclides shortens its life, resulting in the generation of a large amount of waste ion-exchange resin. In this study, the feasibility of electrodeionization (EDI) was investigated for the purification of primary cooling water using synthetic solutions under various experimental conditions as an alternative method for the ion exchange. The results shows that as the feed flow-rate increased, the removal efficiency increased and the power consumption decreased. The removal rate was observed as a 1000 decontamination factor(DF) at a nearly constant level. For the synthetic solution of 3 ppm TDS (Total Dissolved Solid), the power consumption was 40.3 mWh/L at 2.0 L/min of feed flow rate. The higher removal rate of metal species and lower power consumption were obtained with greater resin volume per diluting compartment. However, the flow rate of the EDI process decreased with the elapsed time because of the hydrodynamic resistivity of resin itself and resin fouling by suspended solids. Thus, the ion-exchange resin was replaced by an ion-conducting spacer in order to overcome the drawback. The system equipped with the ion-conducting spacer resolved the problem of the decreasing flow rate but showed a lower efficiency in terms of the power consumption, the removal rate of metal species and current efficiency. In the repeated batch operation, it was found that the removal efficiency of metal species was stably maintained at DF 1000.

• Polymer(Korea)
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• v.27 no.1
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• pp.61-68
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• 2003

In this study, we have investigated the preparation of mixed bead and fiber type hybrid ion-exchanger for recovering nickel ion from plating rinse water. There was little dependence of adsorption capacity for nickel ion on the mixing ratio of resin type and fiber type of ion exchangers. However, it increased with increasing the resin content in the mixed bed. It was shown that the data Langmuir and Freundlich's adsorption isotherm model were well fitted to the linear. Affinity between the functional groups in the ion exchanger and nickel ion in the process was confirmed. The pressure drop decreased with increasing the number of stage in the multistage bed, but it increased with increasing the resin content in the mixing bed. The initial breakthrough time in the multistage bed was short due to the increase of number of stage in the continuous process. It was found that the final breakthrough time of the multistage bed was little changed. The breakthrough time decreased with increasing the amount of fibrous ion exchanger in the mixed bed. The maximum adsorption capacities of the mixed and multistage beds were 2.51 meq/g and 2.69 meq/g, respectively. The desorption time for the nickel ion with $1N H_2SO_4$ solution was lower than 10 minutes and the yield of desorption was greater than 98 percent.

• Applied Chemistry for Engineering
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• v.21 no.1
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• pp.52-57
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• 2010

Although chemical sedimentation and ion exchange are usually applied to the treatment of heavy metal ions and radioactive cations, they have some serious disadvantages like a great consumption of chemicals, the disposal of valuable metals, and the secondary pollution of soil by the solid-waste. The advanced countries recently have studied the electrochemical ion exchange, combined electrochemical reduction and ion exchange, for the development of the alternative technique. This study has been performed to investigate the optimum condition for the preparation of the nickel hexacyanoferrate (NiHCNFe) which is an electrochemical ion exchanger. NiHCNFe film was deposited on the surface of nickel plate by chemical method or electrochemical method. The morphology and composition of NiHCNFe were observed by SEM and EDS, respectively. The peak current density of NiHCNFe was measured from the cyclic voltammograms of the continuous oxidation-reduction reaction in a parallel plane ion exchange electrode reactor. It was found that the chemical preparation method was better than the electrochemical method. The concentrated NiHCNFe was apparently deposited on nickel plate when dipping in the preparing solution for 118 h, especially. It also had a best durable performance as an ion exchange electrode.