• 환경위생공학
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• 제23권1호
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• pp.67-72
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• 2008

Ion exchange performance to remove Ammonium in water was studied using commercially available strong acidic cationic exchange resin of $Na^+$ type in the batch and continuous column reactors. The performance was tested using the effluent concentration histories for continuous column or equilibrium concentrations for batch reactor as a function of time until resins were exhausted or reached ionic equilibrium between resin and solution. The results shoed that cationic exchange resin used in this study was more effective than activated carbon or zeolite for ammonium removal. Ammonium removal with the ion exchange resin temperature to be high qualitative recording minuteness but increases about seasonal change of temperature was judged with the public law where the adaptability is excellent. When the pH comes to be high at 11 degree, the ammonium was not effectively removed.

• 공업화학
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• 제27권6호
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• pp.633-638
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• 2016

본 연구에서는 상용화된 양이온교환수지, 음이온교환수지, 혼합이온교환수지 각각 3종을 이용하여 Cs과 I 등의 방사성이온을 포함하고 있는 오염수 중 방사성 이온을 분리하는 연구를 하였다. 실험은 상온에서 회분식으로 진행하였으며, 이온교환수지의 양을 달리하여 각각의 이온교환수지에 대한 Cs와 I의 제염성능을 비교하였다. 이온크로마토그라피 기기로 농도분석을 한 결과, D사의 이온교환수지의 대체적으로 이온교환능력이 높은 결과 값을 가졌으며, 공통적으로 이온교환수지의 양이 적을 때, 이온교환수지 질량 대비 제염성능이 높은 것을 알 수 있었다. D사의 양이온교환수지의 질량이 적을 때, Cs 이온에 대한 이온교환용량은 0.199 meq/g, 음이온교환수지의 I 이온에 대한 이온교환용량은 0.344 meq/g의 결과 값을 확인할 수 있었으며, 혼합이온수지를 사용했을 때에는 I 이온에 대한 이온교환용량이 0.33 meq/g으로, D사의 이온교환수지가 다른 이온교환수지에 비해 특히 I에 대한 이온교환능력이 높은 것을 알 수 있었다.

• 한국세라믹학회지
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• 제25권3호
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• pp.237-242
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• 1988

Float 공법에 의한 국산 Soda-lime-silica 판유리를 대상으로하여 그의 이온교환 거동에 대하여 연구하였다. 효과 분석으로는 $K^+$ 이온의 침투깊이, 표면층에 형성된 압축응력의 크기, 압축응력층의 두께, $K^+$이온 교환량 및 밀도변화 등을 조사하였다. 본 연구에서 표면층의 최대 압축응력값은 43$0^{\circ}C$-8h 및 45$0^{\circ}C$-6h의 열처리 조건하에서 59.8kg/$Cm^2$이며, 확산을 위한 활성화 에너지는 17.0Kcal/mole이었다. 한편, 과도한 이온교환 열처리 조건하에서는 응력이완 현상을 나타냄을 알 수 있었다.

• E2M - 전기 전자와 첨단 소재
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• 제9권3호
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• pp.284-290
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• 1996

The electrical properties of bulk galsses in the system Na$_{2}$O-CaO-Al$_{2}$O$_{3}$-B$_{2}$O$_{3}$-SiO$_{2}$ containing 20 to 30mol% sodium which have been subjected to a sodium .tautm. silver ion exchange reaction for 24, 36 and 48 hrs. were analysed by impedance spectroscopy method. Ion exchanged glasses exhibit activation energy values lower than those of the untreated ones. The electrical conductivity increase with sodium content and ion exchanging time. In this experiment the electrical conductivity exhibits a manximum value of 1.78*10$^{-4}$ S/cm at 200.deg. C which contains 30mol% sodium and subjects ion exchange reaction for 48hrs.

• 한국세라믹학회지
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• 제26권4호
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• pp.499-504
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• 1989

Coloring effect, mechanical properties resulting from silver ions exchange of glasses immersed into the mixed molten salt of KNO3 and AgNO3 were investigated in this study. Ion exchange coloring of glasses made it possible to obtain glasses with a range from yellow to yellowish-brown, and spectral transmittance was investigated. The amount of ion exchange and peneration depth increased with treatment temperature and time. The activation energy decreased with mole fraction of AgNO3. It can be seem that the bending strength of ion exchanged glasses were 3~4 times higher than the parent glass and Ag+ colloids prevented from increasing surface microhardness.

• Membrane and Water Treatment
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• 제5권2호
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• pp.87-108
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• 2014

Electrodeionization (EDI), which combines electrodialysis (ED) and conventional ion-exchange (IX), is a mature process which has been applied since more than twenty years on commercial use for the production of ultrapure water (UPW). Eliminating chemical regeneration is the main reason for its commercial success. The increase in acceptance of EDI technology has led to an installation of very large plant as the commercial state of the art that produces $1,500m^3/h$ of water for high pressure steam boiler. More recently, EDI system has found a number of new interesting applications in wastewater treatment, biotechnology industry, and other potential field. Along with further growth and wider applications, the development of stack construction and configuration are also become a concern. In this paper, the principle of EDI process is described and its recent developments, commercial scale, and various applications are pointed out.

• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 2005년도 제13회 산화철워크샵
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• pp.3-14
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• 2005

We Investigated minutely how the biosorption technology using algal biomass is opened in Canadian technology society. Making comparative study for relative technologies in views of overall unit operation cost, we could grasp next facts. - Algal biomass plays the competitive performance for various metals. - Algal biomass biosorbent is regenerated. - Reactor system is not and involved one. This means that algal biomass occupies the strong position as biosorbent. Especially, in North America, for the purpose of metal bearing wastewater treatment, 20 hundred million US dollars was appropriated a sum for the purchase of ion exchange resin. But it is only thirty million US dollars if algal biomass biosorbent is used on behalf of ion exchange resin. Furthermore, the expenses for same treatment can be cut down additively through metal recovery.

• 멤브레인
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• 제30권4호
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• pp.276-281
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• 2020

알칼리 금속 이온과 염소 이온이 포함된 용액으로부터 이온교환수지를 이용한 이온 제거에 대한 연구를 진행하였다. 양이온인 금속이온(Na⁺와 K⁺)의 제거에는 양이온교환수지를, 음이온인 염소 이온(Cl^-)의 제거에는 음이온교환수지를 사용하였다. 용액 A (Na⁺를 36,633 ppm, Cl^-를 57,921 ppm 함유)의 경우, Na⁺ 이온과 Cl^- 이온은 20분 이내에 99% 이상 제거되었다. 용액 B (K⁺를 1,638 ppm 함유)의 경우, K⁺ 이온은 3분 이내에 99% 이상 제거되었다.

• 한국산림과학회지
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• 제79권3호
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• pp.285-289
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• 1990

산림토양내(山林土壤內) N 양료화(養料化)와 질산화(窒酸化)를 구명(究明)하기 위하여 최근(最近) 많이 사용하고 있는 ion 교환 (交換) 수지(樹脂) (Ion Exchange Resin : IER)의 방법(方法)을 구명(究明)하고 실험실(實驗室)과 토양(土壤)에 묻었던 IER의 재사용(再使用) 여부를 판단(判斷)하기 위하여 흡수율(吸收率)을 분석(分析)하였다. IER 20g을 나이론 스타킹에 넣고 무처리구, 2M NaCl에 진탕한 후 물에 씻은 처리구(處理區)(2M NaCl구(區), 4M NaCl에 진탕한 처리구(處理區)로서 N 흡수율(吸收率)을 분석(分析)한 결과(結果) 2M NaCl구(區)의 IER은 $NH_4$ 및 $NO_3$를 각각(各各) 70, 60% 흡수(吸收)하여 가장 높은 결과를 보였고 4M NaCl구(區)는 40%정도의 흡수율(吸收率)을 나타냈다. 무처리(無處理) IER은 $NO_3$ 흡수율에서 2M NaCl구(區)와 비슷하였으나 $NH_4$는 낮은 N 농도에서 과대치를 나타냈다. 재사용(再使用)한 IER의 흡수율은 60~80%로서 일정한 흡수율을 나타내지 않았지만 전처리(前處理)로서, 흡수율(吸收率)을 구명(究明)하여 N 농도별로 각각(各各) 흡수율(吸收率)을 적용하면 재사용이 가능할 것으로 판단(判斷)된다.

• 에너지공학
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• 제27권2호
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• pp.70-80
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• 2018

Natural organic matter (NOM) is among the most common pollutant in underground and surface waters. It comprises of humic substances which contains anionic macromolecules such as aliphatic and aromatic compounds of a wide range of molecular weights along with carboxylic, phenolic functional groups. Although the concentration of NOM in potable water usually lies in the range of 1-10 ppm. Conventional treatment technologies are facing challenge in removing NOM effectively. The main issues are concentrated to low efficiency, membrane fouling, and harmful by-product formation. Ion-exchangers can be considered as an efficient and economic pretreatment technology for the removal of NOM. It not only consumes less time for pretreatment but also resist formation of trihalomethanes (THMs), an unwanted harmful by-product. This article provides a comprehensive review of ion exchange processes for the removal of NOM.