• Journal of the Korean Chemical Society
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• v.48 no.6
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• pp.590-598
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• 2004

The preconcentration and determination of trace Cu(II) and Pb(II) on calcium alginate beads in aqueous solution were studied. A calcium alginate beads were prepared by adding an alginic acid to sample solution contained Ca(II). Some following conditions were optimized: the pH of sample solution, amount of alginic acid, and stirring time for effective adsorption; the type and concentration of acid, and sonication time in an ultrasonic vibrator for the perfect de-sorption. A sample solution was prepared with Cu(II) and Pb(II) in DI water. And Ca(II) and ethanol was added into the sample solution. The pH of the final sample solution was controlled with buffer solution. The alginic acid were dispersed in the sample solution by a magnetic stirrer. This mixture was stored in room temperature for 30 min to form a calcium alginate. After the beads were filtered and washed on a membrane filter, the analytes were redissolved from the beads by an ultrasonic vibration of 10 minutes in 1.0M $HNO_3$ solution. The effect of diverse ions on the adsorption of analytes were studied. This procedure was applied for the analysis of two real samples. The recoveries in spiked samples were $90.4{\sim}104.3%$ for analytes.

• Membrane Journal
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• v.19 no.4
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• pp.317-323
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• 2009

In this study the nanofiltration (NF) membrane treatment of a nitric acid waste solutions containing $Pb^{+2}$ heavy metal ion discharging from the etching processes of an electronics and semiconductors industry has been studied for the purpose of recycling of nitric acid etching solutions. Three kinds of NF membranes (General Electric Co. Duraslick NF-4040 membrane, Dow Co. Filmtec LP-4040 membrane and Koch Co. SelRO MPS-34 4040 membrane) were tested for their separation efficiency (total rejection) of $Pb^{+2}$ ion and membrane stability in nitric acid solution. NF experiments were carried out with a dead-end membrane filtration laboratory system. The membrane permeate flux was increased with the increasing storage time in nitric acid solution and lowering pH of acid solution because of the enhancing of NF membrane damage by nitric acid. The membrane stability in nitric acid solution was more superior in the order of Filmtec LP-4040 < Duraslick NF-4040 < SelRO MPS-34 4040 membrane. The total rejection of Pb+2 ion was decreased with the increasing storage time in nitric acid solution and lowering the pH of acid solution. The total rejection of $Pb^{+2}$ ion after 4 months NF treatment was decreased from 95% initial value to 20% in the case of Duraslick NF-4040 membrane, from 85% initial value to 65% in the case of SelRO MPS-34 4040 membrane and from 90% initial value to 10% in the case of Filmtec LP-4040 membrane. These results showed that SelRO MPS-34 4040 NF membrane was more suitable for the treatment of an acidic etching waste solutions containing heavy metal ions.

• Korean Journal of Soil Science and Fertilizer
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• v.44 no.3
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• pp.387-393
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• 2011

We analyzed the particle size distributions of three commercially available Devarda's alloy (DA) products, tested the nitrate recoveries of each particle size category, and examined the amounts of DA required for 100% recovery by varying $NO_3$-N concentration from 0.5 to 10 mg. We observed that use of DA coarser than 200 mesh resulted in poor analytical recovery (<80%). While the tested alloys were considered to be fine enough (>90% of the particles were less than 100 mesh), the recovery dramatically declined from 80% to 10% in a high concentration range (4 to 10 mg N). Satisfactory recovery was obtained by increasing the amount of finer DA (less than 300 or 450 mesh). However, there was no quantitative relationship between the amount of fine DA and nitrate recovered. Generally, the amount of nitrate reduced per unit DA decreased as the recovery efficiency declined. These results suggest that a sufficient amount of DA must be determined based on particle size distribution, and that treatment of at least two levels of DA and comparison of the subsequent change in nitrate recovery is required for soils containing high levels of nitrate. In addition, further studies are encouraged to account for the observed stoichiometric dis-equivalence of recovered nitrate N per unit mass of DA.

• The Korean Nurse
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• v.7 no.6 s.38
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• pp.70-73
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• 1968

심한 화상환자를 치료하는 동안이나 피부이식을 하는 동안에 어떻게하면 환자를 따뜻하고 안전하게 보호할 수 있을까? 사용할 용액들, 홑이불, 수술대, 회복실 침대를 따뜻하게 준비해 놓고 에어컨을 끈다. 너풀거리는 꺼즈를 잘 다듬어 놓고 stockinette도 준비한다. 피부이식을 위하여 피부를 떼어낸 부위에도 화상부위와 마찬가지로 질산은 드레싱을 하며 피부에 식염수나 기름종류는 사용하지 말아야 한다.

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2004.06a
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• pp.232-232
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• 2004

우라늄 변환시설 내의 라군 슬러지의 처리를 위해 슬러지의 물 첨가 용해를 실시하고, 여과후 발생한 질산염의 안정적 처리를 위한 열분해를 실시하였다. 라군 슬러지의 질산염 및 우라늄 제거공정은 후속처리공정에서의 부담을 최소화 할 수 있도록 1.5배의 물을 첨가 용해하였으며, 두 개의 라군에 저장된 슬러지 처리방법의 효율성 평가를 위하여 각 라군의 개별적, 혹은 혼합하여 실험을 실시하였다.(중략)

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2012.05a
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• pp.303-304
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• 2012

공업적으로 널리 사용되는 내식강의 전해연마는 주로 고농도의 인산염 전해액 기반에 황산과 질산 첨가된 용액에서 $70^{\circ}C$ 이상의 고온에서 행해지다 보니 폐액 처리와 작업 환경이 좋지 않아 기피 기술로 인식 되어 있다. 본 연구에서는 환경 친화적인 상온 공정을 개발 하고자 에틸렌 글리콜 용액에 여러 가지 첨가제를 첨가하여 그 효과를 살펴보고 최적 조성과 공정 조건을 확립 하고자 하였다. 틸렌 글리콜에 물과 질산 암모니움을 첨가하여 점도와 pH, 전류 전압 특성을 구하고 여기에 첨가제인 설파메이트와 암모니움 클로라이드 첨가량을 정하고 각각의 효과를 확인 하였다. 이러한 결과를 바탕으로 SUS 316 재질에 대한 최적 연마조건을 설정하기 위해 조도 변화, 광택도 및 표면 조직 변화와 전해연마기구를 비교 검토하였다.

• Resources Recycling
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• v.26 no.1
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• pp.30-36
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• 2017

Leaching experiments of anode slime were performed with several inorganic acids (HCl, $HNO_3$ and $H_2SO_4$) together with thiourea and thiosulfate solution to recover gold and silver. Gold was not dissolved at all into these inorganic acids in the absence of any oxidizing agents. At the same concentration of inorganic acid, the leaching of percentage of Ag was the highest in the sulfuric acid solution. The leaching percentage of silver increased with the increase of HCl concentration owing to the formation of $AgCl_2{^-}$. Copper, nickel and zinc except tin was almost dissolved in these inorganic acids but no tin was dissolved in nitric acid solution. Most of Au and Ag were dissolved into the mixture of sulfuric acid and thiourea solution. Thiosulfate could dissolve some silver from the anode slime but no gold was dissolved by this agent.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.76.2-76.2
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• 2010

질산 용액을 이용한 처리를 통해서 실리콘 웨이퍼 위에 누설 전류가 thermal oxidation 방법과 비슷한 수준의 얇은 실리콘 산화막을 형성할 수 있다. 이러한 처리 방법은 thermal oxidation에 비해서 낮은 온도에서 공정이 가능하다는 장점을 가진다. 이 때 질산 용액으로 68 wt% $HNO_3$을 쓰는데, 이 용액에만 넣었을 때에는 실리콘 산화막이 어느 정도 두께 이상은 성장하지 않는 단점이 있다. 그렇기 때문에 실리콘 웨이퍼를 68 wt% $HNO_3$에 넣기 전에 seed layer 산화막을 형성 시킨다. 본 연구에서는 p-type 웨이퍼를 phosphorus로 도핑해서 에미터를 형성 시킨 후에 seed layer를 형성 시키고 68 wt% $HNO_3$를 이용해서 에미터 위의 실리콘 산화막을 성장 시켰다. 이 때 보다 더 효과적인 seed layer를 형성 시키는 용액을 찾아서 실험하였다. 40 wt% $HNO_3$, $H_2SO_4-H_2O_2$, HCl-$H_2O_2$ 용액에 웨이퍼를 10분 동안 담그는 것을 통해서 seed layer를 형성하고, 이를 $121^{\circ}C$인 68 wt% $HNO_3$에 넣어서 실리콘 산화막을 성장시켰다. 이렇게 형성된 실리콘 산화막의 특성은 엘립소미터, I-V 측정 장치, QSSPC를 통해서 알아보았다.

• Applied Chemistry for Engineering
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• v.7 no.4
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• pp.707-714
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• 1996

Extraction behaviour of Np with DEHPA(di-(2-ethyhexyl)Phosphoric acid) from the low nitric acid solution(below 1M $HNO_3$) containing $H_2O_2$ as a reducing agent was studied at a batch system in order to establish the conditions of extraction and stripping and to enhance the extraction rate. As results, it was confirmed that the Np was mainly the pentavalent oxidation state in the low nitric acid solution. The extraction yield of Np was increased with increasing the concentration of DEHPA and $H_2O_2$ and decreased more rapidly with the increase of $HNO_3$ concentration. It was also found that the Np could be extracted into DEHPA even without the addiction any redox agents, although the extraction yield is rather low as about 70%. The extraction rate was proportional to the 0.516 power of $H_2O_2$ concentration and inversely proportional to 0.483 power of $HNO_3$ concentration as follows. $d[Np(V)]/dt=-1.391{\times}10^{-2}[H_2O_2]^{0.516}[HNO_3]^{-0.483}[Np(V)]$ Regardless of the $H_2O_2$, the Np extracted in the organic phase was effectively stripped to the aqueous phase with $H_2C_2O_4$. The Np could be stripped more than 92 % with 0.5M $H_2C_2O_4$.

• Proceedings of the Korean Nuclear Society Conference
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• 2002.10a
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• pp.342.2-342
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• 2002