• Applied Chemistry for Engineering
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• v.7 no.3
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• pp.473-480
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• 1996

Synthesis of n-perfluorooctanesulfonyl fluoride(n-PFOSF), which is valuable precursor perfluoro-chemicals, was studied by electrochemical fluorination(ECF). Of prime concern was to investigate the cyclic voltamograms of Ni electrode in anhydrous hydrogen fluoride(AHF) with and without the reactants and to measure fluorine evolution potential. In a batch cell, chronoampherometric electrolysis and various chemical analysis such as GC, GC/MS and IR were used to understand the amphere change of electrode and the reaction paths. Fluorine equilibrium potential was found to be about 2.8V(vs. $Cu/CuF_2$) from the cyclic voltammograms and decay curves of anode potential in AHF. In batch processes, the ECF proceeded in two distinguished steps. The first step proceeded electrochemically and the second one chemically. Under 7V(vs. $Cu/CuF_2$), amount of crude products was proportional to the applied anode potential. Above 7V(vs. $Cu/CuF_2$), it had a hundred percentage with weight ratio of reactants and productivity of PFOSF was almost constant.

• Journal of Korean Society of Archives and Records Management
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• v.2 no.2
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• pp.173-186
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• 2002

급변하는 정보화시대 속에서 우리가 잊고 있는 중대한 사실이 있다. 이는 우리가 많은 양의 정보를 가장 빠르고 작고 편리하게 담고자 치중하고 있는 지금, 그 주체가 되는 기록물, 즉 종이에 적혀있는 과거의 역사는 조금씩 우리 곁에서 사라져 가고 있다는 사실이다. 다시말하자면, 우리가 막대한 예산을 들여 이 기록물을 보존하는 목적으로 다른 매체로 전환시키는데 총력을 기울이면서도, 실제로 보존 대상인 이 기록물들에 대해서는 예산부족을 핑계로 삼아 등한시하고 있는 것이다. 기록물의 보존은 과거에도 중요하게 여겨졌고, 현재와 미래에도 계속 중요하게 여겨질 것이다. 그럼으로 우리는 과거의 기록이라는 메시지를 우리의 선조들로부터 전해 받아 우리의 다음세대에게 전해주는 메신저에 불과하므로 이 메신저의 역할에 대하여 정확하게 알아야 할 것이다. 또한 우리가 전해 받은 과거의 유물로 그대로 물어주기 위해서는 우리가 이 시대에 할 수 있는 최선의 일은 그 원형을 잘 보존시키는 일이다. 이러한 기록물의 소실은 그 기록물에 적혀 있는 과거 역사의 소실을 뜻한다. 따라서 앞으로의 보존과학은 과거에 대한 우리의 탐험을 뒷받침할 많은 정보들을 제시하여 줄 것이며 이러한 정보들이 체계적으로 분류되어 정리될 때 한국 종이 기록물의 보존 복원이 발전을 거듭할 것이다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2018.06a
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• pp.69.1-69.1
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• 2018

산업 현장에서 자주 사용되는 알루미늄 합금은 순도가 높은 알루미늄에 비해 경제성, 기계적 성질이 우수한 장점이 있다. 하지만 이런 합금들은 물리적, 화학적 성질이 순수 알루미늄과 달라 양극산화와 같은 표면처리가 쉽지 않다. 양극산화는 표면처리 기술의 대표적인 방법 중 하나로 인위적으로 산화피막을 형성하는 기술이다. 순도가 높은 알루미늄은 산성 전해질에서의 양극산화를 통해 다공성 산화피막을 형성할 수 있으며 그 구조로 인해 내식성, 내마모성 등 기계적, 화학적인 다양한 장점이 있다. 하지만, Mg, Si, Cr과 같은 성분이 함유된 알루미늄의 경우 산성 전해질에서 산화물을 형성되지 않는다. 본 연구에서 기존의 산성 전해질에서의 양극산화 방법이 아닌$K_2HPO_4$를 함유하는 고온의 글리세롤 전해질을 사용하여 양극산화를 진행하였다. 사용한 알루미늄은 산업용으로 자주 사용되는 3000계열의 알루미늄을 사용하였으며 균일한 양극산화를 위해 샌드페이퍼를 통한 연마과정을 통해 표면을 평탄화 하였다. 이후 전기화학적 에칭 과정을 거쳐 표면에 있는 자연산화막을 제거하여 표면 분석을 용이하게 하였다. 양극산화는 10wt%의 $K_2HPO_4$/글리세롤 전해질에서 전해질의 온도와 인가 전압을 달리 하여 진행하였다. 결과 $150^{\circ}C$ 이상의 온도에서 알루미늄 합금의 양극산화를 확인할 수 있었고 $170^{\circ}C$의 온도에서 인가 전압을 20V로 하였을 때 가장 정렬된 다공성 구조를 얻을 수 있었다. 본 연구 결과를 통해 산업용 알루미늄 합금의 양극산화를 통해 다공성 나노구조 산화물을 형성 시킬 수 있었다.

• Resources Recycling
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• v.10 no.4
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• pp.18-23
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• 2001

Air pollutants, phenol was generated in case of thermal regeneration of used activated carbon loaded with phenol and because of this problem, removal process of phenol were studied. Electrolytic oxidation of samples, used S.company granular activated carbon (WS-GAC), used C.company granular activated carbon (WC-GAC) and used L.company granular activated carbon (WL-GAC) loaded with phenol carried out by potentiostatic method in this study. In case of experiment was to come into operation in condition of samples containing 100 mg/g phenol, supporting electrolyte was 1.0% sodium chloride solution, Ti-Ir (10$\times$10$\textrm{cm}^2$) electrode and electrode distance was 2 cm, current density was $1.25 A/dm^2$, Obtained from the results of electrolytic oxidation experiments were not detected residual phenol. And then we knew about reaction time of electrolytic oxidation, current density, concentration of supporting electrolyte and electrode and electrode distance were 60 minutes, 1.25 A/dm$^2$, 1.0%, 2 cm.

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2004.06a
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• pp.236-236
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• 2004

삼중수소수 오염처리의 선행공정으로 적합한 전기분해-촉매교환 결합공정(CECE process)은 수소동위원소 산화물의 수소화 전환을 위한 전해셀과 다단 액상촉매 교환탑으로 이루어진 탈삼중수소 공정이다(그림 1). 촉매탑은 수소 흐름에 수증기를 동반하도록 하는 친수층과 수증기-수소간의 수소동위원소 교환반응을 유도하는 촉매층으로 구분되며, 탑 상부에는 수소의 산화 반응기 그리고 하부에는 물의 수소화 전해셀로 구성되어 있다(그림 2).(중략)

• Resources Recycling
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• v.25 no.4
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• pp.42-48
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• 2016

A research for the recovery of the metal with high purity from the waste tin plating solution was carried out. First, tin plating waste solution was tested to remove the organic substances and metallic impurities such as Fe, Zn, Na etc. using ion exchange resin having iminodiacetic functional groups (Lewatit TP 207). Second, the tin solution was purified to obtain the high purity tin solution using ion exchange resin having ethylhexyl-phosphate functional groups (Lewatit VPOC 1026). Finally, 99.98% of the high purity of tin metal can be recovered from the purified solution by cyclone type electrowinning method.

• Corrosion Science and Technology
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• v.11 no.6
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• pp.213-217
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• 2012

The amount of spent fuel from nuclear power plants has been increasing. An effective management plan of the spent fuel becomes a critical issue, because the storage capacity of each plant will reach its storage limit in a few years. The volume of high toxic spent fuel can be reduced through a fuel processing. Advanced Fuel Cycle (AFC) system is considered to be one of the options to reduce the toxicity and volume of the spent fuel. It is necessary to set up a test facility to demonstrate the feasibility of the process at the engineering scale. The objective of the work is a development of the safety evaluation technology for the AFC system. The evaluation technology of the AFC structural integrity and processes were surveyed and reviewed. Key evaluation parameters for the main processes such as electrolytic reduction, electrorefining, and electrowinning were obtained. The survey results may be used for the establishment of the AFC regulatory licensing procedure. The establishment of the licensing criteria minimizes the trials and errors of the AFC facility design. Issues taken from the survey on the regulatory procedure and design safety features for the AFC facility provide a chance to resolve potential issues in advance.

• Resources Recycling
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• v.30 no.6
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• pp.76-82
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• 2021

The separation of palladium from crude metal, which is obtained from electronic waste using pyrometallurgy was achieved through electrolysis. This was done to recover high-purity copper. The oxidation potentials of these metals are a fundamental part of the analysis of electrolytic separation of palladium and impurity metals. To achieve this, copper, iron, and nickel were dissolved in the electrolyte, and palladium and aluminum were found to be recoverable from anode slime. During the electrolysis for palladium separation, palladium was present in the anode slime and was obtained with a recovery of 97.46 % indicating almost no loss. 4N-grade copper was recovered from the electrodeposition layer at the cathode.

• Resources Recycling
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• v.27 no.6
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• pp.38-43
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• 2018

In this study, using electro-refining process and methane gas reduction, we performed studying the recovery of tin with high purity from waste tin oxide had used as a electrode rod of ceramic furnace which occurred during glass production process. We recovered the crude tin of 99% purity from a methane gas reduction process and controlled a little amount of impurities. When the electrolytic refining condition was a current density of $60A/dm^2$ and the sulfuric acid concentration of 0.75 mol, 96.8% of recovered tin (99.979% of purity) were recovered during the electrolytic refining. We confirmed that toxic impurities such as Pb, Sb included in electrode rod. could be controlled.

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2005.06a
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• pp.101-109
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• 2005

In order to produce only a pH-controlled solution without discharging any unused solution, this work has developed a continuous electrolytic system with a pH-adjustment reservoir being placed before an ion exchange membrane-equipped electrolyzer, where as a target solution was fed into the pH-adjustment reservoir, some portion of the solution in the pH-adjustment reservoir was circulated through the cathodic or anodic chamber of the electrolyzer depending on the type of the ion exchange membrane used, and some other portion of the solution in the pH-adjustment reservoir was discharged from the electrolytic system through other counter chamber with its pH being controlled as acid or base. The phenomena of the pH being controlled in the system could be explained by the electro-migration of the ion species in the solution through the ion exchange membrane under a cell potential difference between anode and cathode and its consequently-occurring non-charge equilibriums and electrolytic water- split reactions in the anodic and cathodic chambers.