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.
본 연구는 X-선관 각도 변경에 따른 경사효과(Anode Heel Effect)의 변화를 알아보고자 실시하였다. 실험조건은 70 kV, 30 mAs, 초점-검출기간의 거리 100 cm, 조사야는 35×43 ㎠, 측정점은 조사야의 정중앙점에서 좌우 3.5 cm 간격으로 나누어 양극쪽으로 A1, A2, A3, A4, A5, A6 점을 설정하고 음극쪽으로 C1, C2, C3, C4, C5, C6 점으로 설정하였다. X-선관을 수직으로 하여 측정점인 A6에서 C6까지 각각 입사표면선량을 측정하였다. 다음에 X-선관을 양극쪽으로 15도 30도로 변경 하면서 각각 측정하고 같은 방법으로 음극쪽으로 15도 30도로 변화시켜 측정하였다. 결과로 X-선관이 수직인 경우 A5보다 C5점이 3배정도 입사표면선량이 높게 나타나 수직 촬영 시 방사선감수성이 높은 장기가 위치해 있는 쪽으로 양극을 위치시키면 피폭을 줄일 수 있었다. X-선관의 각도를 주고 촬영할 경우에는 음극측으로 각도를 주는 것이 양극과 음극측의 입사표면선량 차이를 줄일 수 있으며 상, 하 두께 차이가 있는 부위를 촬영할 경우에는 음극측이 두꺼운 부위를 향하게 각도를 주는 것이 입사표면선량의 차이를 줄여 좀 더 균일한 영상을 만들 수 있었다.
함정에 사용되는 선체재료로는 연강, 고장력강, 고강도강, 알루미늄 합금 및 복합재료 등이 있다. 그 중 함정의 선체는 수밀과 강도 의 유지 및 탑재장비의 지지 등 기본적인 기능을 위하여 철강 재료를 주로 사용하고 있다. 함정의 주 임무는 해양에서 작전을 수행하는 것이 므로 해수에 의한 선체 부식이 필연적으로 발생하게 된다. 선체의 부식을 방지하기 위하여 도장 방법, 희생양극법 및 강제 전류 방식이 사용 되고 있다. 특히 Al 및 Zn을 활용한 희생양극법의 경우 부식특성 개선을 위하여 인듐(In), 카드뮴(Cd) 및 납(Pb) 등의 중금속이 첨가되어 있 다. 하지만 이러한 중금속은 인체 및 환경에 매우 유해하므로 전 세계적으로 사용이 점차 규제되고 있다. 이에 본 논문에서는 인체 및 환경에 무해한 미세원소(Ma, Ca, Ce 및 Sn)를 첨가하여 Al 및 Zn 합금을 제조하였다. 제조된 함정용 Al 및 Zn 희생양극의 효율 특성 측정을 위하여 SEM, XRD, 동전위 분극실험 및 전류효율 평가를 실시하였으며, 실험결과 Al-3Zn-0.6Sn 및 Zn-3Sn 합금의 양극 성능이 다른 합금 보다 효 율성이 우수하였다.
Electrochemical degradation of phenol was evaluated at DSA (dimensionally stable anode), JP202 (Ru, 25%; Ir, 25%; other, 50%) electrode for being a treatment method in non-biodegradable organic compounds such as phenol. Experiments were conducted to examine the effects of applied current (1.0~4.0 A), electrolyte type (NaCl, KCl, Na2SO4, H2SO4) and concentration (0.5~3.0 g/L), initial phenol concentration (12.5~100.0 mg/L) on phenol degradation and UV254 absorbance as indirect indicator of by-product degraded phenol. It was found that phenol concentration decreased from around 50 mg/L to zero after 10 min of electrolysis with 2.5 g/L NaCl as supporting electrolyte at the current of 3.5 A. Although phenol could be completely electrochemical degraded by JP202 anode, the degradation of phenol COD was required oxidation time over 60 min due to the generation of by-products. UV254 absorbance can see the impact of as an indirect indicator of the creation and destruction of by-product. The initial removal rate of phenol is 5.63 times faster than the initial COD removal rate.
Fabrication and oxidants production of 3 or 4 components metal oxide electrode, which is known to be so effective to destruct non-biodegradable organics in wastewater, were studied. Five electrode materials (Ru as main component and Pt, Sn, Sb and Gd as minor components) were used for the 3 or 4 components electrode. The metal oxide electrode was prepared by coating the electrode material on the surface of the titanium mesh and then thermal oxidation at 500℃ for 1 h. The removed RhB per 2 min and unit W of 3 components electrode was in the order: Ru:Sn:Sb=9:1:1 > Ru:Pt:Gd=5:5:1 > Ru:Sn=9:1 > Ru:Sn:Gd=9:1:1 > Ru:Sb:Gd=9:1:1. Although RhB decolorization of Ru:Sn:Sb:Gd electrode was the highest among the 4 components electrode, the RhB decolorization and oxidants formation of the Ru:Sn:Sb=9:1:1 electrode was higher than that of the 3 and 4 components electrode. Electrogenerated oxidants (free Cl and ClO2) of chlorine type in 3 and 4 components electrode were higher than other oxidants such as H2O2 and O3. It was assumed that electrode with high RhB decolorization showed high oxidant generation and COD removal efficiency. OH radical which is electrogenerated by the direct electrolysis was not generated the entire 3 and 4 components electrode, therefore main mechanism of RhB degradation by metal oxide electrode based Ru was considered indirect electrolysis using electrogenerated oxidants.
Fabrication and oxidants formation of 1 and 2 component metal oxide electrode, which is known to be so effective to destruct non-biodegradable organics in wastewater, were studied. Five electrode materials (Ru, Pt, Sn, Sb and Gd) were used for the 1 and 2 component electrode. The metal oxide electrode was prepared by coating the electrode material on the surface of the titanium mesh and then thermal oxidation at 500℃ for 1 h. The removed RhB per 2 min and unit W for one component electrode decreased in the following sequences: Ru/Ti > Sb/Ti > Pt/Ti > Gd/Ti > Sn/Ti. The concentration of oxidants generated in 1 and 2 component electrodes was in the order of: ClO2 > free Cl > H2O2 > O3. OH radical was not generated from in entire one and two component electrodes. RhB degradation rate and generated oxidants of the Ru-Sn=9:1 electrode was higher than that of the two component electrode. The exact relationship between the removal of RhB and the generated oxidants concentration was not obvious. However, it was assumed that electrode with high RhB decolorization had high oxidant concentration.
Small gas bubbles are used in many environmental and industrial processes for solid-liquid separations or to facilitate heat and mass transfer between phases. This study examines some of the factors that affect the bubble volume and size processed in the EF (electroflotation) process. The effect of electrode material, NaCl dosage, current and electrode distance were studied. The results showed that the generated bubble volume with electrode material lay in: Pt/Ti ≒ Ru/Ti ≒ Ir/Ti > Ti electrode. The more NaCl dosage was high, the smaller bubble was generated due to the low electric power. Bubble generation was increased with increase of current. With the increase of NaCl dosage, bubble generation was increased at same electric power (16.2 W). Generated bubble volume was not affected by electrode distance. However, no clear trends in bubble size as a function of these parameters were evident.