• Journal of the Korean Institute of Electrical and Electronic Material Engineers
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• v.21 no.11
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• pp.995-999
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• 2008

ZnO nanowires with tetrapod shape were formed on the surface of the sample by direct melt oxidation of Al-Zn alloy at $1000^{\circ}C$ in air. X-ray diffraction (XRD) pattern revealed that the ZnO nanowires had wurtzite structure of hexagonal phase. Any other element except Zn and O was not detected in energy dispersive X-ray spectrum. The c- and a-axis lattice constants estimated from the XRD pattern were 0.520 and 0.325 nm, respectively. These are in well accordance with those of bulk ZnO single crystal, indicating high quality crystallinity. The green light emission at a wavelength of 510 nm was observed from the nanowires at room temperature, which was ascribed to high density of oxygen vacancies in nanowires.

• Korean Journal of Materials Research
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• v.2 no.4
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• pp.241-247
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• 1992

The direct bonding of Cu to $Al_2O_3$, employing the $Cu-Cu_2$O eutectic skin melt, is investigated. The bonding force and interface structure of samples prepared by oxidation at $1015^{\circ}C$ in $1.5{\times}10^{-1}$torr followed by bonding at 107$5^{\circ}C$ under $10_{-3}$ torr vacuum have been studied using peeling test, SEM, EDS and XRD. It has been found that the optimal strength is obtained for 3 minutes of oxidation while the adhesion force is decreased with oxidation shorter or longer than 3 minutes. The rupture occured at alumina-eutectic interface. Fractured surface of $Al_2O_3$covered with $Cu_2$O nodules pulled out of the Cu indicates that bonding strength is governed by $Cu-Cu_2$O interface and not by $Cu_2$O-A$l_2O_3$interface. The bonding force is slightly increased with bonding time and the reaction phases of CuA$l_2O_4$and $CuAlO_2$are formed at interface during the bonding.

• Nuclear Engineering and Technology
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• v.45 no.6
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• pp.767-790
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• 2013

MAAP4 is a computer code that can simulate the response of a light water reactor power plant during severe accident sequences, including actions taken as part of accident management. The code quantitatively predicts the evolution of a severe accident starting from full power conditions given a set of system faults and initiating events through events such as core melt, reactor vessel failure, and containment failure. Furthermore, models are included in the code to represent the actions that could mitigate the accident by in-vessel cooling, external cooling of the reactor pressure vessel, or cooling the debris in containment. A key element tied to using a code like MAAP4 is an uncertainty analysis. The purpose of this paper is to present a MAAP4 based analysis to examine the sensitivity of a key parameter, in this case hydrogen production, to a set of model parameters that are related to a Level 2 PRA analysis. The Level 2 analysis examines those sequences that result in core melting and subsequent reactor pressure vessel failure and its impact on the containment. This paper identifies individual contributors and MAAP4 model parameters that statistically influence hydrogen production. Hydrogen generation was chosen because of its direct relationship to oxidation. With greater oxidation, more heat is added to the core region and relocation (core slump) should occur faster. This, in theory, would lead to shorter failure times and subsequent "hotter" debris pool on the containment floor.

• Korean Chemical Engineering Research
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• v.46 no.6
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• pp.1142-1147
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• 2008

Nano-structured porous carbon fiber(PCF) for the catalyst supports of the direct methanol fuel cell (DMFC) were prepared from the mesophase pitch by using the nano-MgO powders. Specific surface area of the PCFs was $8{\sim}58m^2/g$ and surface pore structures had almost meso pore diameter of 10~20 nm which were depending on the amount of MgO spheres. Aqueous reduction method was used to load 60 wt% PtRu on the prepared PCF supports. The electro-oxidation activity and single cell performance of the 60 wt% Pt-Ru catalysts were measured by cyclic voltammetry and unit cell test. The performances of these catalysts increased by 5~10% compared with one of commercial catalyst.