• 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.

• 한국방사성폐기물학회:학술대회논문집
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• 한국방사성폐기물학회 2005년도 Proceedings of The 6th korea-china joint workshop on nuclear waste management
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• pp.165-175
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• 2005

Measurement of spent resin activity was initiated in 2004 in order to develop the C-14 removal technology for safe disposal. As part of this program, spent resins were sampled and measured in the in-station resin storage tank 2 at Wolsong Nuclear Power Plant Unit 1. At the time of sampling, the resins had been in storage tank from 3 to 23 years. Total 72 resin samples were sampled, which were collected from both man-hole (68 samples) and test-hole (4 samples) in the in-station resin storage tank 2. They were separated into liquid, activated carbon, zeolite, and spent resin. The spent resins were oxidized with sample oxidizer and analyzed for C-14. Ten of collected mixed resin samples were separated by density into cation and anion resins using a sugar solution. The C-14 concentration in anion exchange resin was approximately 2 times higher than in the mixed resin. The average concentration of C-14 in the cation/anion mixed exchange resin was $460\;GBq/m^3$ from test-hole and $53.1\;GBq/m^3$ from man-hole. We have found that concentration of C-14 in the spent resin is about from 0.4 to $1,321\;GBq/m^3$. So it could be a problem, when dispose of at a repository, since there is a disposal limit of $222\;GBq/m^3$. This means we should develop the C-14 removal technology.

• 한국물환경학회지
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• 제30권5호
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• pp.517-523
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• 2014

In order to remove both nitrate and sulfate present in the concentrate of RO(reverse osmosis) process, a combined bio-regeneration and ion-exchange(IX) system was studied. For this purpose, both denitrifying bacteria(DNB) and sulfate reducing bacteria(SRB) were simultaneously cultivated in a bio-reactor under anaerobic conditions. When the IX column containing a nitrate-selective A520E resin was fully exhausted by nitrate and sulfate, the IX column was bio-regenerated by pumping the supernatant of the bio-reactor, which contains MLSS concentration of $125{\pm}25mg/L$, at the flowrate of 360 BV/hr. Even though the nitrate-selective A520E resin was used, the breakthrough curves of ionic species showed that sulfate was exhausted earlier than nitrate. The reason for this result is due to the fact that the concentration of sulfate in RO concentrate was 36 to 48 times higher than nitrate. The bio-reactor was successfully operated at a volumetric loading rate of 0.6 g $COD/l{\cdot}d$, nitrate-N loading rate of 0.13 g $NO_3{^-}-N/l{\cdot}d$, and sulfate loading rate of 0.08 g $SO_4{^{2-}}/l{\cdot}d$. The removal rate of SCOD, nitrate-N, sulfate was 90, 100, and 85%, respectively. When the virgin resin was fully exhausted and consecutively bio-regenerated for 2 days, 81% of nitrate and 93% of sulfate were reduced. When the virgin resin was repeatedly used up to 4 cycles of service and bio-regeneration, the ion-exchange capacity of bio-regenerated resin decreased to 95, 91, 88, and 81% of virgin resin.

• 분석과학
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• 제18권6호
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• pp.469-474
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• 2005

본 연구에서는 음이온 교환수지와 Sr-Spec 수지를 사용하여 토양중 $^{90}Sr$, $^{241}Am$ 및 Pu 동위원소들에 대하여 축차적으로 분리하는 정량법을 제시하였다. 플루토늄은 음이온 교환수지를 이용하여 분리하였고, 아메리슘 및 스트론튬은 옥살산 공침법 및 Sr-Spec 수지를 사용하여 순수 분리하였다. Pu 및 Am 동위원소는 알파 스펙트로메트리법으로 정량하였고, Sr-90은 액체섬광계수기를 사용하여 정량하였다. 본 연구에서 고찰된 $^{90}Sr$, $^{241}Am$ 및 Pu 동위원소 분석법을 IAEA 기준시료에 적용하여 분석법의 타당성을 검증하였다.

• Bulletin of the Korean Chemical Society
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• 제14권6호
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• pp.749-752
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• 1993

Borohydride exchange resin $(BER)-CuSO_4$ system readily reduces {\alpha},{\beta}$-unsaturated ketones to the corresponding saturated alcohols quantitatively. This reduction tolerates many functional groups such as carbon-carbon multiple bonds, chlorides, epoxides, esters, amides and nitriles.

• 한국방사성폐기물학회:학술대회논문집
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• 한국방사성폐기물학회 2005년도 추계 학술대회 논문집
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• pp.79-86
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• 2005

In PSR on the Kori 3&4 NPP, The low level radioactive waste resin from SGBD demineralizer is more than $65\%$ of total waste resin in NPP So, it needs to be improved. The secondary cooling water pH control methods are used ammonia-AVT from the first. According to changing ETA which is better than ammonia, SGBD cation load is increased about 2-3 times. Waste resin product is also increased in proportion to the SGBD cation load. To reduce the waste volume, new cation resin exchange criteria is confirmed that demineralizer is almost saturated.

• 한국환경과학회지
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• 제14권10호
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• pp.919-928
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• 2005

This study introduces the development of new supercritical water oxidation(SCW)(multiple step oxidation) to destruct recalcitrant organic substances totally and safely by using sodium nitrate as an oxidant. This method has solved the problems of conventional SCW, such as precipitation of salt due to lowered permittivity, pressure increase following rapid rise of reaction temperature, and corrosion of reactor due to the generation of strong acid. Destruction condition and rate in the supercritical water were examined using Polyvinyl Chloride(PVC) and ion exchange resins as organic substances. The experiment was carried out at $450^{\circ}C$ for 30min, which is relatively lower than the temperature for supercritical water oxidation $(600-650^{\circ}C)$. The decomposition rates of various incombustible organic substances were very high [PVC$(87.5\%)$, Anion exchange resin$(98.6\%)$, Cationexchange resin$(98.0\%)$]. It was observed that hetero atoms existed in organic compounds and chlorine was neutralized by sodium (salt formation). However, relatively large amount of sodium nitrate (4 equivalent) was required to raise the decomposition ratio. For complete oxidation of PCB was intended, the amount of oxidizer was an important parameter.

• 한국유체기계학회 논문집
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• 제17권2호
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• pp.35-40
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• 2014

The optimal removal efficiency to develop wastewater treatment system using the magnetic ion exchange resin. The secondary sedimentation effluent of wastewater in W wastewater treatment plant located in Gyeong-gi Province was used as the influent. To compare the sedimentation effluent reacted with the magnetic ion exchange resin to the influent, the concentrations of CODmm, TN, $NO{_3}^-$-N and TP were measured. The flux of the influent and HRT were set to 250 mL/min, 10 min, respectively, and BVTR has adjusted to 200, 150, 100. The removal efficiency of CODmn, TN, $NO{_3}^-$-N and TP in the 200 BVTR from 71%, 40.37%, 46.34%, 42.03%, 150 BVTR from 55.22%, 37.83%, 50.38% 41.6% and 100 BVTR from 74%, 59.15%, 79.94%, 79.16%, respectively. The results on 200 BVTR, 150 BVTR, 100 BVTR tests show that 100 BVTR is the optimal factor capable of the highest rate of rejection of the organic material.

• 한국식품과학회지
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• 제27권3호
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• pp.313-317
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• 1995

대두침출액으로부터 대두올리고당을 생산하기 위하여 한외여과한 대두침출액의 정제를 목적으로 이온교환공정을 검토하였다. 차단분자량 20,000인 막을 사용하여 한외여과한 대두침출액을 이온교환처리할 경우 회분은 양이온교환수지에 의하여 대부분 제거되었으며 단백질 및 색소제거에는 음이온교환수지의 효과가 높았다. 회분 및 단백질 제거효과가 높은 수지는 각각 양이온교환수지 SK1B 및 음이온교환수지 WA30이었다. 이온교환시 ERR이 낮을 경우 단백질과 회분의 제거는 효과적이었으나 상당량의 올리고당이 수지에 흡착되어 소실되었다. 차단분자량 20,000인 막을 사용하여 한외여과한 대두침출액을 차단분자량 5,000인 막으로 2차 한외여과하여 단백질을 추가로 제거하고 혼합수지를 사용하여 ERR 5.0으로 이온교환처리한 결과, 단백질, 회분, 색소가 거의 전량 제거되었고 올리고당의 회수율도 높아 적정 이온 교환조건으로 결정되었다.

• 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.