• Proceedings of the Materials Research Society of Korea Conference
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• 2011.10a
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• pp.29.2-29.2
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• 2011

수용액 상에서 유기물이나 무기물의 전해산화에는 높은 산소과전압과 그 화학종에 대한 화학적, 물리적 안정성이 요구되며, 이러한 요구 조건을 만족하는 소재로써 백금족의 원소가 통상 사용되고 있으나, 가격이 매우 비싸다는 단점을 가지고 있다. 특히 고전류밀도 폐수처리 불용성 전극은 수용액을 전기분해할 때 높은 전류밀도를 낼 수 있으며, 폐수에 혼합되어 있는 각종 화학적 성분에 대한 화학적, 물리적 내구성이 있는 전극으로서, 현재 기존의 수처리용 전극은 금속 Ti을 기판으로 하여 그 위에 불용성 촉매로써 전도성 금속염을 도포, 열처리를 반복하여 산화물의 형태로 수 ${\mu}m$의 두께로 코팅하는 이른바, DSA (Dimensionally Stable Anodes) 전극을 사용하고 있는데, 이는 제조 단가의 상승과 금속 Ti 기판 상에 코팅된 전도성 금속산화물의 미약한 접착력으로 인한 탈리로 전극 전체의 성능 저하 및 수명 단축을 초래하는 문제점이 있다. 본 연구에서는 상기의 문제점을 개선하고자 대표적 불용성 촉매 물질인 백금을 RF magnetron 스퍼터링방식으로 100~300 nm 두께로 성막하여 Ti 기판에 대한 불용성 촉매 물질의 부착력과 내구성 및 모의 해수에 대한 해수전해 특성 등을 평가하였다.

• Clean Technology
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• v.9 no.3
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• pp.133-144
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• 2003

In this study, Insoluble catalyst electrode for oxide systems were manufactured, by using of them, carried out experiments on electrolytic treatment of dyeing wastewater containing persistent organic compounds, and then made a comparative study of the efficiency of treatment for environmental pollutants and whether each of them is valuable of not as an electrode for soluble electrode(Fe, Al) and insoluble electrode(SUS, R.C.E; Replaced Catalyst Electrode) which were used in the electrolytic system. Besides, it was investigated the conditions for electrolytic treatment to find the maximum efficiency of electrolytic treatment. As the result of this study, by using of insoluble catalyst electrode for oxide can solved the stability of electrode that is one of the greatest problems in order to put to practical use of electrolysis process in the treatment of the sewage and wastewater and the result runs as follows; 1. The durability of insoluble catalyst electrode(R.C.E) can be verified the most favorable when the molar ratio of $RuO_2-SnO_2-IrO_2-TiO_2$(4 compounds system) is 70/20/5/5. 2. The efficiency of treatment was obtained a more than 90% goodness for CODMn and also a good results for T-N removal in the experimental conditions of the distance of electrode 5 mm, time of electrolysis 60 minutes, permissible voltage 10V, processing capacity $0.5{\ell}$.

• Applied Chemistry for Engineering
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• v.32 no.4
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• pp.409-416
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• 2021

Dimensionally stable electrodes are one of the important components in electrochemical water treatment processes. In the manufacturing of the dimensionally stable electrodes, the type of metal catalyst coated on the surface of the metal substrate, the coating and sintering methods substantially influence their performance and durability. In this study, using Ir-Ru-Ta ternary metal coating, various electrodes were prepared depending on the coating method under the same pre-treatment and sintering conditions, and its performance and durability were studied. As a coating method, brush and spray coating were used. As a result, the reduction in the amount of catalyst ink was achieved because more amount of metal could be coated for the electrode using spraying with the same amount of catalyst ink. In addition, the spray_2.0_3.0 electrode prepared by a specific spray coating method shows the phenomenon of cracking and the uniform coating of the ternary metal on the surface of the coating layer, and results in a high electrochemically active specific surface area, and the decomposition performance of 4-chlorophenol was superior to the other electrodes. However, it was found that there was no significant difference in durability depending on the coating method.

• Journal of Korean Society of Environmental Engineers
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• v.38 no.6
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• pp.291-298
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• 2016

Electrochemical water treatment process as a useful treatment method for the removal of non-degradable matter has been consistently studied for several decades. Key process of electrochemical water treatment are oxidation reaction from an anode and reduction from a cathode. In this study, the effect of pre-treatment methods in the insoluble electrode manufacturing process for the water treatment has been evaluated for the life time of electrode The results of this study showed that pre-treatment methods of a base metal such as surface roughness, clean method and interlayer formation influenced to life time of electrode when the same condition (catalyst electrode layer coating method and material system) was applied for pre-treatment methods. This study was conducted by using $IrO_2/Ti$ electrode In the test of sand-blasting process, an electrode manufactured by using sanding media of different sizes resulted in the most effective electrode life time when the size of alumina was used for $212{\sim}180{\mu}m$ praticle size (#80). The most effective method was considered using arc plasma in the additional roughness control and cleaning process, sputtering method to form Ta type interlayer formation process.

• Journal of the Korean Applied Science and Technology
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• v.33 no.2
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• pp.352-360
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• 2016

The purpose of this study was to determine the electrochemical properties develop DSA electrode for sewage sludge solubilization. Using Ir as a main catalyst, the catalyst selected for the sewage sludge solubilization durability and proceeds to functional electrode suitable for sewage sludge electrolysis experiment were obtained the following results. Less mass reduction of the sintering temperature of the main catalyst, Ir coated electrodes, the endothermic reaction zone $300^{\circ}C$ to $500^{\circ}C$, which was selected from a range of experiments. The efficiency of the catalyst results came up to $350^{\circ}C$ best. Each Binder stars (Ta, Sn, W) in this experiment was the biggest catalyst efficiency at $350^{\circ}C$. Used as a binder, $TaCl_5$, $SnCl_4$, $WCl_6$ of the Ta and without affecting the other characteristics of the main catalyst than Sn, W. For the 50% $IrO_2$ electrode is 1.4 V (vs. Ag / AgCl) in a current of about $29mA/cm^2$ was caused to evaluate the effectiveness of the electrode.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2017.05a
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• pp.99.1-99.1
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• 2017

$TiO_2$는 기계적, 화학적 안정성이 높아 가혹한 화학적 환경 또는 고온 운전 조건에서 훌륭한 내구성을 보여주어 산업적으로 일찍이 널리 이용되어 왔다. 예를 들어, 염소발생 (chlorine evolution reaction) 또는 산소발생반응은 (oxygen evolution reaction) 염소 또는 산소 라디칼에 전극이 지속적으로 노출되기에 강한 내부식성을 지닌 전극재가 요구되었고, 그 결과 $TiO_2$를 골조로 한 불용성전극 (dimensionally stable anode)이 개발되어 이용되고 있다. 그러나, $TiO_2$는 절연성이 높은 금속 산화물 재료이기 때문에 넓은 표면적 획득 및 촉매제 사용을 통해 소재의 단점을 극복해야만 한다. 넓은 반응 표면적 획득의 한 방법으로써 전기화학적 양극산화 (electrochemical anodization)를 통한 $TiO_2$ 나노튜브 제조법은 경제적이면서도 구조 제어도 간편한 방법이다. $TiO_2$ 나노튜브는 100nm 전후의 기공 크기를 가짐과 동시에 매우 높은 종횡비를 지니고 있어 넓은 반응 표면적 획득에 특히 유리하다. 그러나, 이 높은 종횡비는 촉매 도입을 어렵게 하는 저해요소가 되기도 한다. 이러한 문제를 해결하기 위하여 다양한 방법들이 연구되었으나 대부분이 번거롭거나 비싼 후단공정을 필요로 한다. 본 연구에서는 $TiO_2$ 나노튜브에 촉매를 도핑하기 위한 간단한 전기화학적 방법으로, 단일공정 양극산화법 (single-step anodization)과 전압충격법 (potential shock), 그리고 저전압충격법 (under potential shock)을 연구하였으며 이에 적용 가능한 촉매제의 종류를 소개한다. 또한, 촉매의 성질에 따른 응용분야와 그 성능평가 결과를 제시한다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2018.06a
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• pp.28-28
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• 2018

수전해(electrochemical water splitting)는 연료전지의 가역적 역반응을 이용하여 물로부터 수소와 산소를 발생시키는 기술이다. 산소는 음극에서 발생하는데, 이 때 음극 표면은 고농도의 산소 음이온 및 라디칼에 장시간 노출된다. 때문에 기계적, 화학적 내구성이 우수한 전극재를 사용할 필요가 있다. 불용성 전극 (dimensionally stable anode, DSA)은 이러한 기술적 요구사항을 잘 만족하는 상용화 된 전극이다. 티타늄이나 티타늄 합금 표면에 촉매를 미량 반복 살포하여 산화물 형태의 매우 견고한 표면을 형성함으로서 내구성을 확보한다. 그러나, 보통 DSA 제조 기법의 특징에 따라 다공성 표면 구조를 사용하지는 않기 때문에 생산 과정이 복잡하고 비용이 많이 발생하는 문제를 여전히 나타내고 있다. 본 연구는 상기 문제를 개선하기 위한 수전해용 음극 제조 기술에 관한 연구이다. 티타늄과 티타늄 합금은 동일한 양극산화 기술 적용이 가능하다는 점을 이용하여 티타늄 기판으로부터 다공성 구조를 형성함으로써 바인더의 사용을 배제하였다. 단일공정양극산화기법 (single-step anodization)을 이용하여 $IrO_2$와 $RuO_2$를 도핑함으로써 TiO2에 촉매능을 부여하였다. 제조된 나노튜브들의 구조적 특징을 HR-TEM (High-resolution transmission electron microscope)과 FE-SEM (Field-emission scanning electron microscope)으로 분석하고 SAED (selective area electron diffraction) 패턴을 분석하여 전극재의 결정성을 확인하였다. 알칼라인 분위기에서 일으킨 산소발생반응 (oxygen evolution reaction, OER)의 LSV (linear sweep voltammetry) 결과를 XPS (X-ray photoelectron microscoscopy) 결과와 연관지어 촉매 표면 구조와 과전압의 관계를 해석하였다. LSV 결과로부터 Tafel 분석을 연달아 수행함으로써 전극의 속도결정단계를 정의하였다. 최종적으로 사이클 테스트 통하여 DSA로써의 성능을 평가하였다.

• Korean Journal of Materials Research
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• v.22 no.2
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• pp.86-90
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• 2012

Insoluble catalytic electrodes were fabricated by RF magnetron sputtering of Pt on Ti substrates and the performance of seawater electrolysis was compared in these electrodes to that is DSA electrodes. The Pt-sputtered insoluble catalytic electrodes were nearly 150 nm-thick with a roughness of $0.18{\mu}m$, which is 1/660 and 1/12 of these values for the DSA (dimensionally stable anodes) electrodes. The seawater electrolysis performance levels were determined through measurements of the NaOCl concentration, which was the main reaction product after electrolysis using artificial seawater. The NaOCl concentration after 2 h of electrolysis with artificial seawater, which has 3.5% NaCl normally, at current densities of 50, 80 and 140 mA/$cm^2$ were 0.76%, 1.06%, and 2.03%, respectively. A higher current density applied through the electrodes led to higher electrolysis efficiency. The efficiency reached nearly 58% in the Pt-sputtered samples after 2 h of electrolysis. The reaction efficiency of DSA showed higher values than that of the Pt-sputtered insoluble catalytic electrodes. One plausible reason for this is the higher specific surface area of the DSA electrodes; the surface cracks of the DSAs resulted in a higher specific surface area and higher reaction sites. Upon the electrolysis process, some Mg- and Ca-hydroxides, which were minor components in the artificial seawater, were deposited onto the surface of the electrodes, resulting in an increase in the electrical resistances of the electrodes. However, the extent of the increase ranged from 4% to 7% within an electrolysis time of 720 h.

• Journal of the Korean Society for Environmental Technology
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• v.19 no.6
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• pp.536-542
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• 2018

A system combining an electrochemical method and an adsorption system using activated carbon was assessed to facilitate the reuse of cabbage-salting brine. IrOx/Ti insoluble catalyst electrodes were used in the experiment. The results were analyzed to identify any changes in the residual chlorine concentration according to variations in the current density at a salinity of 10 %, as well as the capacity of the activated carbon to adsorb the residual chlorine and organic matter. For current densities of $500A/m^2$ and $1,000A/m^2$, the residual chlorine concentration did not increase, instead stabilizing once the current reached 0.33 Ah/L. To assess the adsorption efficiency according to the residual chlorine concentration, the unit amount of the adsorption can be estimated from $Y=0.0066+2.087{\times}10^{-4}b$. For both residual chlorine generation using an electrochemical method and chlorine removal through activated-carbon adsorption, the unit amount of adsorption was 0.33 g/g. The maximum amount of $COD_{Cr}$ organic matter adsorbed by the activated carbon was 0.021 g/g, while for $COD_{Mn}$, the value was 0.004 g/g.