강유전체 재료의 하부전극으로 사용되고 있는 Pt/Ti 박막의 접착력에 대한 열처리 분위기의 영향을 연구하였다. 시편의 접착력은 90˚ 필 테스트 방법을 사용하여 정량적으로 측정하였다. 열처리 후 사용된 분이기에 관계없이 모두 접착력이 감소하였는데 특히 산소분위기에서 열처리 한 시편의 접착력이 매우 크게 감소하였다. AES depth profile과 단면 TEM을 이용하여 계면반응을 관찰한 결과 산소열처리시에는 Ti가 외부에서 확산해 온 산소와 반응하여 rutile TiO2상이 형성됨을 알 수 있었다. 그러므로 산소열처리 후에 일어나는 접착력의 급격한 감소 원인은 열처리시 취약한 TiO2상이 형성되며 이로 인해 Ti 접착층이 고갈되기 때문임을 알 수 있었다.

An innovative batch electrolytic system consisted of electrolytic basin, which was equipped with DSA(Dimensionally Stable Anode) type insoluble electrode, Ti/IrO2 anode and H-C metal cathode, and flotation separator was developed for the efficient treatment of shipboard emulsified oily wastewater. The electorod cleance and current density of elecrolytic basin to ensure maximum treatment efficiency of oily wastewater was evaluated as 6 mm, 3 A/dm3, respectively. The electrolytic efficiency of oily wastewater was affected by the operationtemperature, and it means that the temperature controller to ensure the stabiity of the process is required. The conductivity in the electrolytic basin was increased with the percentage of sea water in the oily wastewater, and over 90% of treatment efficiency of oily wastewater could be obtained at 7% of sea water. The oil removal rate was increased according to the increase of the quantity of electricity, and the maximum value of electrilyic rate constant was 288 mgoil/A.min. The information obtained from this study might be used for development of an efficient continuous electrolytic system treating the emulsified oily wastewater.

감응물질로 제4급 암모늄염을 사용하여 PVC를 지지체로 과염소산이온의 농도 10-6M까지 측정가능한 이온 선택성 전극을 제작하였다. 감응물질의 화학적 구조와 함량, 가소제의 종류 및 막 두께에 따른 선형응답 범위와 Nernst의 기울기 등 전극특성을 검토하여, 최적 막조건을 구한 다음 측정가능 pH범위와 여러 방해이온에 대한 선택계수를 비교 검토하였다. 과염소산 이온선택성 전극에서 감응물질의 화학적 구조 즉, 알킬기의 탄소고리수가 증가할수록 선형응답 범위 등 전극 특성은 Aliquat 336P, TOAP, TDAP 및 TDDAP의 순서로 좋아졌다. 가소제는 DBP가 가장 좋았고, 감응물질의 양은 최적 함량 이상에서 적을수록 좋았다. 최적 막 조성은 TDDAP 9.09, PVC 30.3 및 DBP 60.61wt%이었고, 막두께 0.45mm이었다. 이 조건에서 선형응답 범위 10-1~1.2 × 10-6M, 검출한계 5.1×10-7M 및 Nernst기울기 57mV/pClO4이었다. 막전위는 pH 4~11 범위에서 pH의 영향을 받지 않았으며, 선택계수 서열은 다음과 같았다. SCN->I->NO3->Br->ClO3->F->Cl->SO42-

플라즈마 회전전극법으로 제조된 Ti-51at%Al 금속간화합물 분말에 함유된 불순물의 함량변화를 분석하였다. 산소와 탄소의 함량은 각각 600 및 200ppm 정도로 분말입도에 따라 변하였으며, 이는 주로 원재료에 포함된 불순물의 영향이었다. AES 분석에 의하면 분말표면 산화물은 주로 Ti 및 Al과 산소 및 탄소의 복합화합물로 구성되었으며, 그 두께는 약 100 및 200μm 크기의 분말에 대하여 각각 7 및 3.4nm 정도로 측정되었다. 분말의 제조로 산소와 탄소의 함량이 오히려 감소되는것의 구체적인 기구는 아직 확인되지 않았으나 플라즈마 고열에 의한 정련현상에 기인하는 것으로 생각된다.

Ta2O5 박막은 실리콘산화막, 실리콘질화막 박막에 비해 유전율은 높으나 누설전류밀도가 높고, 절연파괴강도가 낮아 DRAM의 커패시터용 재료로서 실용화가 되지 못하고 있다. 본 연구에서는 LPCVD법으로 형성시킨 300Å 두께의 Ta2O5 유전체박막에 대해 후속열처리 또는 전극재료를 변화시켜 열악한 전기적 특성의 원인을 규명하고자 하였다. 그 결과 다결정 실리콘 전극의 경우 성막상태의 Ta2O5 박막은 전극에 의한 환원반응에 의해 전기적 특성이 열화됨을 알 수 있었고, 이를 TiN 전극의 사용으로 억제시킬 수 있었다. 다결정 실리콘 전극의 경우 성막상태의 Ta2O5 유전체는 누설정류밀도가 10-1A/cm2, 절연파괴강도가 1.5MV/cm 정도였으며, 800˚C에서 O2열처리를 하면 전기적 특성은 개선되나, 유전율이 낮아진다 TiN 전극을 채용할 경우 누설전류밀도 10-6~10-7A/cm2, 절연파괴강도 7~12MV/cm 로 ONO(Oxide-Nitride-Oxide) 박막과 비슷한 Ta2O5 고유전막을 얻을 수 있었다.

The ammonium salt of N-Nitrosophenylhydroxiamine, namely Cupferron, is a well-known analytical reagent which precipitates a great number of metal ions in acid medium. Various structures of electrode reduction for N-Nitrosophenylhydroxiamine have been suggested in acid and alkaline media by many researchers, but not in neutral medium. So the mechanism of electrode reaction of Cupferron was investigated by both chronopotentiometric and polarographic methods. It was estimated that the reduction of Cupferron occurs in a three-step mechanism through which a chemical step is interposed between two charge transfer, the ECE (charge transfer-chemical reaction-charge transfer) mechanism, over a range of neutral and alkaline media. The chemical reaction of the process was assumed to be acid-base catalyzed from the fact that kapp (over all rate constant) of chemical reaction is pH dependent.

In this work, we prepared a heterojunction anode with a surface layer of SnO2-Sb-Ni (SSN) on a Ti/IrO2 electrode by thermal decomposition to improve the electrochemical activity of the Ti/IrO2 electrode. The Ti/IrO2-SSN electrode showed significantly improved electrochemical activity compared with Ti/IrO2. For the 0.1 M NaCl and 0.1 M Na2SO4 electrolytes, the onset potential of the Ti/IrO2-SSN electrode shifted in the positive direction by 0.1 VSCE and 0.4 VSCE, respectively. In 2.0-2.5 V voltages, the concentration in Ti/IrO2-SSN was 2.59-214.6 mg/L Cl2, and Ti/IrO2 was 0.55-49.21 mg/L Cl2. Moreover, the generation of the reactive chlorine species and degradation of Eosin-Y increased by 3.79-7.60 times and 1.06-2.15 times compared with that of Ti/IrO2. Among these voltages, the generation of the reactive chlorine species and degradation of Eosin-Y were the most improved at 2.25 V. Accordingly, in the Ti/IrO2-SSN electrode, it can be assumed that the competitive reaction between chlorine ion oxidation and water oxidation is minimized at an applied voltage of 2.25V.

The conventional development of multi-component electrodes is based on the researcher's experience and is based on trial and error. Therefore, there is a need for a scientific method to reduce the time and economic losses thereof and systematize the mixing of electrode components. In this study, we use design of mixture experiments (DOME)- in particular a simplex lattice design with Design Expert◯R program- to attempt to find an optimum mixing ratio for a three-component electrode for the high RNO degradation; RNO is an indictor of OH radical formation. The experiment included 12 experimental points with 2 center replicates for 3 different independent variables (with the molar ratio of Ru, Ti, Ir). As the Prob > F value of the ‘Quadratic’ model is 0.0026, the secondary model was found to be suitable. Applying the molar ratio of the electrode components to the corrected response model results is an RNO removal efficiency (%) = 59.89 × [Ru] + 9.78 × [Ti] + 67.03 × [Ir] + 66.38 × [Ru] × [Ir] + 132.86 × [Ti] × [Ir]. The R2 value of the equation is 0.9374 after the error term is excluded. The optimized formulation of the ternary electrode for an high RNO degradation was acquired when the molar ratio of Ru 0.100, Ti 0.200, Ir 0.700 (desirability d value, 1).

콘크리트 비저항에 대한 실험실 단위의 측정시, 실험체의 제한된 크기로 인해 겉보기 비저항은 측정위치에 따라 영향을 받게 된다. 콘크리트 실험체를 대상으로 한 비저항 측정에서 위치에 따른 영향을 분석하였으며 겉보기 비저항이 가장자리로 이동할수록 그 영향이 높게 나타난다는 것을 확인하였다. 콘크리트 비저항 추정의 정확성을 높이기 위해 이에 대한 사전 검토가 필요함을 알 수 있었다.

The lifetime of the electrode is one of the most important factors on the stability of the electrode. Since the lifetime of the DSA (Dimensionally stable anode) electrode is long, an accelerated lifetime test is required to reduce the test time. Beacuse there is no basis or standard method for accelerated lifetime testing, many researchers use different methods. Therefore, there is a need for basis and methods for accelerated lifetime testing that other researchers can follow. We designed a reactor system for accelerated lifetime testing and planned specific methods. Reactor system was circulating batch reactor. Reactor volume and cooling water tank were 12.5 L and 100 L, respectively. Electrode size was 2 cm x 3 cm (real electrolysis area, 5 cm2). In order to maintain the harsh conditions, accelerated lifetime test was carried out in a high current density (0.6 A/cm2) and low electrolyte concentration (NaCl, 0.068 mol/L). Maintaining a constant temperature was an important operation parameter for exact accelerated lifetime test. As the accelerated lifetime test progressed, the active component of electrode surface was consumed and desorption occurred. At the point of 5 V rise, corrosion of the surface of the base material(titanium) also started.

Recently, the evaluation of the grout chamber of PC bridges has been emphasized in order to prevent many problems in advance. This paper analyzes the electrical resistance of the MWCNT cement composites by electrode intervals in order to select the optimum electrode location for evaluation of grout chamber. It is concluded that the electrical resistance of the MWCNT cement composite specimens increase as the electrode interval is longer.

The mother machine makes the necessary shape by processing materials such as metal. The SCFs are applied to the processing surface when the mother machine processes the material, thereby improving the cutting conditions. SCFs contain high concentrations of organic components and nitrogen compounds, which can cause problems such as eutrophication and algae bloom. Therefore, proper treatment is required. Electrochemical treatment is expected to be an alternative to conventional processes, and to be useful in various wastewater treatments. Moreover, it is an efficient elimination technique for contaminants and has a simple equipment composition. In this study, the removal efficiency of the T-N contained in the waste SCF using electrochemical treatment is analyzed. The electrode was made of titanium and iridium, made into a perforated metal sheet to prevent an imbalance of the sample concentration in the reactor. Experiments were conducted to examine the effects of current density and the concentration of the supporting electrolyte (NaCl, Na2SO4) on removal efficiency. In the cases with 60 A/m2, 80 A/m2, and 100 A/m2 current densities, the removal efficiencies of the T-N contained in the waste SCF were 51.03%, 68.83%, and 79.58%. Comparing between the addition and non-addition of NaCl, the removal efficiency with the addition of NaCl (5 ~ 10 mM) was higher than for no addition at 60 min for all current densities. The addition of Na2SO4 increased the removal rate of the T-N, but it was less effective than NaCl addition.

As industry continues to develop, the amount of various recalcitrant substances that cannot be removed by conventional wastewater treatment has increased in modern society. The SCFs (Soluble Cutting Fluids) used in metalworking processes contain many chemical substances, such as mineral oils, anticorrosive agents, extreme-pressure additives and stabilizers, as well as high concentrations of organics. Recently, electrolysis has been expected to become an alternative to conventional processes and to be useful in various wastewater treatments. Electrolysis is a highly adaptable industrial wastewater treatment method, having a high efficiency, short processing time, and simple equipment composition, regardless of the biodegradable nature of the contaminants. The effects of operating time, current density, and electrolyte on COD removal of waste SCFs have been studied using the stainless steel (SUS316) electrode in a batch type reactor. The results were as follows. ① Without electrolytes, when the current density was adjusted to 40 A/m2, 60 A/m2, and 80 A/m2, the removal efficiencies of the COD were 25.0%, 37.7%, and 49.1% after 60 min, respectively. ② In the comparison between NaCl (5 ~ 10 mM) addition and non-addition, the removal efficiency with NaCl was higher than for without after 60 min for all current densities. ③ In the comparison between Na2SO4 (5 ~ 10 mM) addition and nonaddition, the removal efficiency with Na2SO4 showed no significant difference to that with NaCl at all current densities.

1970년대 수출주도 고도성장을 위해 정부는 조선･철강･기계 등의 중화학공업을 선택적으로 집중육성 하였다. 그 결과 일반기계산업은 1970년 수출 8백만불에서 2015년 현재 218,262백만불로 약 27,000배 이상 성장하였다. 일반기계산업에 있어 금속가공 공정은 필수적이며, 금속가공 공정에서 필요로 하는 것이 공작기계(Mother machine)와 절삭유(Soluble Cutting Fluids, SCF)이다. 절삭조건 개선에 사용되는 절삭유는 첨가제, 사용용도 등에 따라 원액으로 사용하는 비수용성과 물로 희석해서 사용하는 수용성으로 나뉜다. 국내 절삭유 이용량의 60%이상이 수용성 절삭유로 비수용성 절삭유의 오일미스트(Oil-mist), 폐유처리과정에서 유독성 물질 발생 등의 문제로 수용성 절삭유 사용량이 점차 증가하였다. 또한 절삭 성능 향상을 위한 방부제, 윤활제, 방청제, 부식방지제, 세정제, 극압 첨가제 등 각종 화학물질 첨가로 인해, 노출될 경우 췌장, 피부, 담낭, 방광, 소화기계 등 인체의 여러 조직에 암을 유발할 수 있으며, 각종 호흡기계 질환과 피부질환을 초래하는 것으로 알려져 있다. 인체에 미치는 영향 외에도 수용성 절삭유에는 고농도의 유기성분과 질소화합물 등이 함유되어 있어 적절한 처리 없이 수계로 유출시 부영양화, 녹조현상 등과 같은 문제를 일으킬 수 있으며 산화반응에 의해 수계의 용존산소를 감소시키므로 그 처리의 중요성이 부각되고 있다. 본 연구에서는 실공정에서 발생한 폐수용성절삭유를 원시료로 하여 대표적인 불용성 전극인 Ti/IrO2 전극을 이용하여 전기화학적 처리를 진행하였으며 연구에 사용한 장치의 모식도를 Fig. 1에, 시료의 성상을 Table 1에 나타내었다.

우리나라 경제의 성장을 이끈 기계산업은 2015년 현재 생산액 100조원, 사업체수 9,526개사, 종사자수 31만 5천명, 부가가치 39조원으로써 제조업 중 생산액 5위, 사업체수 2위, 종사자수 3위, 부가가치 4위에 위치하고 있다. 이러한 기계산업에 있어 공작기계를 이용해 금속을 원하는 모양으로 만드는 금속가공은 반드시 필요한 공정으로 금속가공 시 가공 장비의 수명 연장 및 가공물의 품질 향상을 위해 칩이 형성되는 영역에 적용되어 윤활 및 냉각작용을 하는 절삭유(Soluble Cutting Fluids, SCF)가 이용되고 있다. 절삭유는 수용성 및 비수용성으로 나뉘는데 비수용성 절삭유의 경우 윤활성은 우수하나 경제성 및 발연, 발화등의 문제점이 있으며, 수용성 절삭유는 윤활성은 비교적 떨어지나 냉각성과 경제성이 우수하다는 장점이 있다. 또한 절삭유는 기능 향상을 위해 PAH, 방부제, 파라핀계 염소, 아질산염 등 20~30개의 첨가제가 사용된다. 이는 중추신경계 장애, 이비인후 자극, 피부염 발생 등을 일으킬 위험성이 크다고 알려져 있으며, 고농도의 유기성분 및 질소화합물로 인해 수계에 유출시 부영양화, 녹조현상 등과 같은 문제를 일으킬 수 있다. 따라서 본 연구에서는 전기화학적 처리를 통해 반응시간에 따른 폐수용성 절삭유의 COD 및 T-N의 제거율 변화를 분석하였다. 전기화학적 처리의 중요 인자인 전극은 비교적 가격이 저렴하고 용출량이 낮은 것으로 알려져 있는 SUS316전극을 이용하였으며 자세한 실험 조건을 Table 1에, 연구에 사용한 장치의 모식도를 Fig. 1에 나타내었다.

Soluble Cutting Fluids (SCFs) have been used in metal machining processes to improve the quality of metal processing equipment and products. Although SCFs are useful and essential material, wasted soluble cutting fluids are harmful in hydroecological systems because of the high concentration of COD and nitrogen material. If discharged to hydroecological systems without specific treatment, they may cause eutrophication in rivers and lakes. Therefore, the removal efficiency of the COD contained in the SCFs is investigated in this study using electrochemical treatment with an insoluble electrode. The electrode was made of titanium with iridium plating, made from a perforated metal sheet to agitate the sample in the reactor. Cathode and anode electrodes were inserted into acrylic reactor alternately and the reaction time was one hour. The experimental results were as follows: First, for 60 A/m2, 80 A/m2, and 100 A/m2 current densities, the COD removal efficiencies were 42.0%, 63.9%, and 78.4%, respectively.

The Electrocoagulation-Flotation (ECF) process has great potential in wastewater treatment. ECF technology is effective in the removal of colloidal particles, oil-water emulsion, organic pollutants such as microalgae, and heavy metals. Numerous studies have been conducted on ECF; however, many of them used a conventional plate-type aluminum anode. In this study, we determined the effect of changing operational parameters such as power supply time, applied current, NaCl concentration, and pH on the turbidity removal efficiency of kaoline. We also determined the effects of different electrolyte types (NaCl, MgSO4, CaCl2, Na2SO4, and tap water), as well as the differences caused by using a plate-type and mesh-type aluminum anode, on the turbidity removal efficiency. The results showed that the optimal values of ECF time, applied current, NaCl concentration, and pH were 5 min, 0.35 A, 0.4 g/L NaCl in distilled water, and pH 7, respectively. The results also revealed that the turbidity removal efficiency of kaoline in different electrolytes decreased in the following sequence, given the same conductivity: tap water > CaCl2 > MgSO4 > NaCl > Na2SO4. The turbidity removal efficiency of the mesh-type aluminum anode was significantly greater than the plate-type aluminum anode.

상향류식 혐기성 생물전기화학 반응조(upflow anaerobic bioelectrochemical reactor, UABE)를 이용하여 주정폐수를 유기물부하율 16 g COD/L.d에서 처리하는 동안 pH, 알카리도, 유기산 등의 상태변수들의 변화와 COD 제거율, 비메탄발생량 및 메탄함량에 대한 전극배치의 영향을 평가하였으며, 그 성능을 UASB 반응조와 비교하였다. 면적이 27 m²/m³인 전극을 나선형으로 UABE 반응조 전체 공간에 고르게 배치하였을 때 비메탄발생율은 5.78 L/L.d로서, 전극을 설치하지 않은 UASB 반응조의 3.49 L/L.d보다 약 65.6%로 높았다. 이것은 UABE 반응조에 전기활성미생물이 성장하여 직접 종간전자전달(direct interspecies electron transfer, DIET) 반응이 활성화됨으로서 메탄생성반응이 크게 향상되었다는 것을 의미한다. UABE 반응조의 상부 1/3의 공간에 위치한 전극을 제거하였을 때, 비메탄발생율은 5.74 L/L.d로서 반응조 전체 공간에 전극을 설치한 경우와 큰 차이가 없으나, UABE 반응조 상부 2/3 공간에 설치한 전극을 제거한 경우 비메탄발생율은 5.34 L/L.d로 약 7.5% 감소하였다. 이 결과는 UABE 반응조에서 전극을 하부 1/3의 공간에만 설치한 경우 전기활성미생물도 감소하여 DIET 반응도 감소하였다는 것을 의미한다. 전극을 UABE 반응조 하부로부터 2/3 이상의 공간까지 설치하였을 때 COD 제거율은 약 91.5%이었으나 반응조 하부로부터 1/3의 공간에만 설치한 경우 COD 제거율은 88.9%로 약 2.6%로 감소하였다.

Rapid industrial development has led to a serious problem of pollution in the industrial sector. With the increasing social need for environmental protection, research on air pollution prevention equipment for reducing pollutants in industrial processes is actively being undertaken. The deterioration of existent, installed facilities, their increased emission rates, and the strengthening of the effluent quality standards make complying with permissible emission standards difficult. In fact, installing new electric precipitators or complementing existent facilities is inevitable. The expansion and complementation of the installed electrical precipitators have led to improvements in dust collection efficiency, shorter working times, and lower costs. Because of its easy installation and simple manufacturing process, the production method with the discharge electrode of an electric precipitator is widely used. The following conclusions were reached by classifying discharge electrodes into four types based on the production method and mutually comparing them by their dust collection efficiency. None of the four types used in this study were damaged by impact. However, we were able to confirm some strain from the compression sites of both type A and type B. Both type B and type C are expected to have greater dust collection efficiencies than the other models due to their large vibration transmissibility. Moreover, the high vibrational energy is expected to cause rapping damage during its operation. Particularly, in the case of type B, some of the strain was found at the end of the compression site. The coupling schemes of both type C and type D are out of vibration transmissibility. On the other hand, the ability to maintain straightness and solidity of the side is regarded as outstanding and stable. Type D has outstanding on-site workability, considering the presence of locking, structural stability, and work conditions. From these experiments, we determined that type C is the most ideal connection method of discharge electrode, considering its construction period of renovation. Type C is inferior to type D with regard to on-site workability. However, type C has outstanding dedusting transmission with regard to the straightness, solidity maintenance, and vibration of shearing stress.