• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2001년도 하계학술대회 논문집
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• pp.275-278
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• 2001

Ferroelectric PZT thin films were fabricated on the RuO$_2$/Pt, Pt bottom electrode with a PZT(53/47) metal alkoxide solutions. All PZT thin films showed a uniform grain structure without the presence of rosette structure. The PZT thin films were etched as a function of Cl$_2$/Ar and additive CF$_4$ into Cl$_2$(80%)/Ar(20%). The etch rates of PZT thin films were 1970 ${\AA}$/min at 30 % additive CF$_4$ into Cl$_2$(80%)/Ar(20%). The remanent polarization and leakage current density in PZT thin film on the RuO$_2$/Pt were 64.2 ${\mu}$C/cm$^2$, 1.4${\times}$10$\^$-6/ respectively.

• 한국재료학회지
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• 제29권1호
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• pp.16-22
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• 2019

Indirect oxidation using chlorine species oxidizing agents is often effective in wastewater treatment using an electrochemical oxidation process. When chlorine ions are contained in the wastewater, oxidizing agents of various chlorine species are produced during electrolysis. In a ballast water management system, it is also used to treat ballast water by electrolyzing seawater to produce a chlorine species oxidizer. However, ballast water in the brackish zone and some wastewater has a low chlorine ion concentration. Therefore, it is necessary to study the chlorine generation current efficiency at various chlorine concentration conditions. In this study, the chlorine generating current efficiency of a boron-doped diamond(BDD) electrode and insoluble electrodes are compared with various chloride ion concentrations. The results of this study show that the current efficiency of the BDD electrode is better than that of the insoluble electrodes. The chlorine generation current efficiency is better in the order of BDD, MMO(mixed metal oxide), $Ti/RuO_2$, and $Ti/IrO_2$ electrodes. In particular, when the concentration of sodium chloride is 10 g/L or less, the current efficiency of the BDD electrode is excellent.

• 공업화학
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• 제18권4호
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• pp.356-360
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• 2007

나노 다공질 $TiO_2$ 전극막, 광 감응형 염료, 전해질 그리고 상대전극으로 구성된 염료감응형 태양전지(Dye-Sensitized Solar Cells, DSSCs)는 최근에 많은 관심을 받아오고 있다. 염료감응형 태양전지에서 $TiO_2$ 전극막은 태양광의 흡수량을 증가시키기 위해 가능한 많은 양의 Ru 착물을 표면에 흡착시켜야 하는데 이를 위해 높은 비표면적과 나노 다공성 입자로 구성된 광전극이 요구된다. 또한 에너지 전환 효율을 증가시키기 위한 방법으로 $TiO_2$ 페이스트의 제작시 산을 첨가 후 열처리하는 방법이 보고되고 있다. 이 논문에서는 산이 첨가된 페이스트로 제조한 $TiO_2$ 광전극이 염료감응형 태양전지의 에너지 변환 효율에 미치는 영향을 체계적으로 이해하기 위해 FE-SEM, XPS, EXAFS 그리고 AFM 등을 이용하여 제조된 광전극의 물리적 화학적 특성을 조사하였다. 또한 광전류-전압 곡선으로부터 산처리된 페이스트를 이용하여 제조한 염료감응형 태양전지의 에너지 전환효율을 평가하였다. 산처리된 페이스는 염료감응형 태양전지의 에너지 전환효율에 크게 영향을 미침을 알 수 있었다.

• 마이크로전자및패키징학회지
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• 제6권2호
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• pp.63-68
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• 1999

가스 감지막의 미세구조와 비화학량론 구조의 변화에 따른 응답특성의 거동을 고찰하기 위하여 소성 조건을 변화시키면서 $WO_3$후막형 가스센서를 제조하였다. 소자는 감지물질인 $WO_3$분말과 유기 용제를 균일하게 혼합한 페이스트를 Au전극과 $RuO_2$발열체가 입혀진 알루미나 기판 위에 스크린 프린팅 방법으로 제조하였다. 소성 조건을 변화시키기 위하여 600-$800^{\circ}C$ 온도범위하에서 1시간 동안 열처리 하였고, Ar과 $O_2$가스의 비율을 변화시키면서 $700^{\circ}C$에서 1시간 재열처리하였다. 열처리 결과, 소성 온도 $700^{\circ}C$에서 제조된 $WO_3$가스센서 소자가 가스감도 210, 응답속도 2초로 가장 좋은 특성을 보였으며 Ar과 $O_2$가스의 비율이 40-50%의 소성 분위기에서 가스 감도가 가장 높게 나타났다.

• 한국수소및신에너지학회논문집
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• 제11권1호
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• pp.19-27
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• 2000

The polymer electrolyte membrane fuel cell (PEMFC) system was developed. In order to enhance the performance of membrane electrode assembly (MEA), the transfer printing method of the electrocatalyst layer on membrane was developed. The $H_2/O_2$ single cell with an electrode area of $50cm^2$ was fabricated and tested using 20 wt.% Pt/C as an electrocatalyst and the commercial and hand-made MEA such as Nafion 115, Hanwha, Dow, Flemion T and Gore Select. The 100-cell PEMFC stack with an active electrode area of $300cm^2$ was designed and fabricated using 40 wt.% Pt/C and 30 wt.% Pt-Ru/C as a cathode and anode electrocatalysts, respectively. The performance of PEMFC system was obtained to be 7kW (250A at 28V) and 3.5kW (70A at 50V) at $80^{\circ}C$ by flowing $H_2/air$ and methanol reformed fuel gas/air, respectively.

• 공업화학
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• 제23권1호
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• pp.86-92
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• 2012

이온교환수지(ion exchange resin; IER)를 이용하여 이산화염소($ClO_2$)의 전구체 용액인 아염소산나트륨($NaClO_2$) 용액으로부터 아염소산이온($ClO_2^-$)을 흡착시킨 후 전기분해장치(electrolysis system)에 의한 이산화염소 가스 발생 특성을 조사하였다. 이온교환수지는 강염기성 음이온교환수지를 사용하였으며, 전극으로는 Ru, Ir이 코팅된 Ti plate를 사용하였다. 반응조의 교반속도, 온도, 아염소산 제조농도, 이온교환수지의 투입량과 형태에 따라 이온교환수지의 아염소산이온($ClO_2^-$) 흡착량에 미치는 영향을 조사하고 최대 흡착량을 나타내는 이온교환수지를 도출하였다. 전기분해장치에 의한 이산화염소의 발생 추이를 관찰하고 발생 목표값에 최적화된 조건을 실험계획법인 반응표면분석(response surface design)으로 선정하였다. 최대 흡착량을 나타내는 강염기성 음이온교환수지는 SAR-20 (TRILITE Gel type II형)이며 그 흡착량은 약 110 mg/IER (g)으로 관찰되었으며, 전기분해장치의 이산화염소 발생 최적조건은 멸균 목표값인 900~1000 ppm, 1 h에서 정전류는 전류인가 전극의 면적을 기준으로 $A/dm^2$, $N_2$ gas 유량은 4.7 L/min이었다.

• 한국재료학회지
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• 제20권5호
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• pp.257-261
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• 2010

A non-volatile resistive random access memory (RRAM) device with a Cr-doped $SrZrO_3/SrRuO_3$ bottom electrode heterostructure was fabricated on $SrTiO_3$ substrates using pulsed laser deposition. During the deposition process, the substrate temperature was $650^{\circ}C$ and the variable ambient oxygen pressure had a range of 50-250 mTorr. The sensitive dependences of the film structure on the processing oxygen pressure are important in controlling the bistable resistive switching of the Cr-doped $SrZrO_3$ film. Therefore, oxygen pressure plays a crucial role in determining electrical properties and film growth characteristics such as various microstructural defects and crystallization. Inside, the microstructure and crystallinity of the Cr-doped $SrZrO_3$ film by oxygen pressure were strong effects on the set, reset switching voltage of the Cr-doped $SrZrO_3$. The bistable switching is related to the defects and controls their number and structure. Therefore, the relation of defects generated and resistive switching behavior by oxygen pressure change will be discussed. We found that deposition conditions and ambient oxygen pressure highly affect the switching behavior. It is suggested that the interface between the top electrode and Cr-doped $SrZrO_3$ perovskite plays an important role in the resistive switching behavior. From I-V characteristics, a typical ON state resistance of $100-200\;{\Omega}$ and a typical OFF state resistance of $1-2\;k{\Omega}$, were observed. These transition metal-doped perovskite thin films can be used for memory device applications due to their high ON/OFF ratio, simple device structure, and non-volatility.

• Carbon letters
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• 제9권4호
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• pp.303-307
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• 2008

The studies on integrated operation of fuel cell with fuel processor are very essential prior to its commercialization. In this study, Polymer Electrolyte Membrane Fuel Cell (PEMFC) was operated with a fuel processor, which is mainly composed of two parts, methanol steam reforming reaction and preferential oxidation (PROX). In fuel processor, ICI 33-5 (CuO 50%, ZnO 33%, $Al_2O_3$ 8%, BET surface area: $66\;m^2g^{-1}$) catalyst and CuO-$CeO_2$ catalyst were used for methanol steam reforming, preferential oxidation (PROX) respectively. PEMFC was operated by hydrogen fuel generated from fuel processor. The resulting gas from PROX reactor is used to operate PEMFC equipped with our prepared anode and cathode catalyst. PtRu/C catalyst gives more tolerance to CO.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 춘계학술대회 초록집
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• pp.87-87
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• 2010

Photoelectrochemical (PEC) systems are promising methods of producing H2 gas using solar energy in an aqueous solution. The photoelectrochemical properties of numerous metal oxides have been studied. Among them, the PEC systems based on TiO2 have been extensively studied. However, the drawback of a PEC system with TiO2 is that only ultraviolet (UV) light can be absorbed because of its large band gap (3.2 - 3.4 eV). Two approaches have been introduced in order to use PEC cells in the visible light region. The first method includes doping impurities, such as nitrogen, into TiO2, and this technique has been extensively studied in an attempt to narrow the band gap. In comparison, research on the second method, which includes visible light water splitting in molecular photosystems, has been slow. Mallouk et al. recently developed electrochemical water-splitting cells using the Ru(II) complex as the visible light photosensitizer. the dye-sensitized PEC cell consisted of a dye-sensitized TiO2 layer, a Pt counter electrode, and an aqueous solution between them. Under a visible light (< 3 eV) illumination, only the dye molecule absorbed the light and became excited because TiO2 had the wide band gap. The light absorption of the dye was followed by the transfer of an electron from the excited state (S*) of the dye to the conduction band (CB) of TiO2 and its subsequent transfer to the transparent conducting oxide (TCO). The electrons moved through the wire to the Pt, where the water reduction (or H2 evolution) occurred. The oxidized dye molecules caused the water oxidation because their HOMO level was below the H2O/O2 level. Organic dyes have been developed as metal-free alternatives to the Ru(II) complexes because of their tunable optical and electronic properties and low-cost manufacturing. Recently, organic dye molecules containing multi-branched, multi-anchoring groups have received a great deal of interest. In this work, tri-branched tri-anchoring organic dyes (Dye 2) were designed and applied to visible light water-splitting cells based on dye-sensitized TiO2 electrodes. Dye 2 had a molecular structure containing one donor (D) and three acceptor (A) groups, and each ended with an anchoring functionality. In comparison, mono-anchoring dyes (Dye 1) were also synthesized. The PEC response of the Dye 2-sensitized TiO2 film was much better than the Dye 1-sensitized or unsensitized TiO2 films.

• 한국환경보건학회지
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• 제35권3호
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• pp.201-208
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• 2009

Oxidation of phenol in aqueous media by electro-Fenton process using Ru-Sn-Sb/graphite electrode has been studied. Hydrogen peroxide was electrically generated by reaction of dissolved oxygen in acidic solutions containing supporting electrolyte and $Fe^{2+}$ was added in aqueous media. Phenol degradation experiments were performed in the presence of electrolyte media at pH 3. Effect of operating parameters such as current, electrolyte type (NaCl, KCl and $Na_2SO_4$) and concentration, $Fe^{2+}$ concentration, air flow rate and phenol concentration were investigated to find the best experimental conditions for achieving overall phenol removal. Results showed that current of 2 A, NaCl electrolyte concentration of 2g/l, 0.5M concentration of $Fe^{2+}$, air flow rate of 1l/min were the best conditions for mineralization of the phenol by electro-Fenton.