• 한국세라믹학회지
• /
• 제32권11호
• /
• pp.1246-1254
• /
• 1995

A numerical model for fabrication and deposition of ultrafine SiO2 particles were proposed in the simplified horizontal MCVD apparatus using tube furnace reactor. The model equations such as energy and mass balance equations and the 0th, 1st and 2nd moment balance equations of aerosols were considered in the reactor. The phenomena of SiCl4 chemical reaction, SiO2 particle formation and coagulation, diffusion and thermophoresis of SiO2 particles were included in the aerosol dynamic equation. The profiles of gas temperature, SiCl4 concentration and SiO2 particle volume were calculated for standard conditions. The concentrations, sizes and deposition efficiencies of SiO2 particles were calculated, changing the process conditions such as tube furnace setting temperature, total gas flow rate and inlet SiCl4 concentration.

• 한국추진공학회:학술대회논문집
• /
• 한국추진공학회 2009년도 제33회 추계학술대회논문집
• /
• pp.93-96
• /
• 2009

고속 비행기술의 발전과 엔진효율의 향상은 비행체와 엔진의 열적부하를 증가시킨다. 극초음속까지 비행체의 속도가 빨라지면 공기흐름을 이용한 냉각이 어렵기 때문에 항공유를 주요 냉각제로서 사용하게 된다. 연료가 열 흡수원(Heat sink)으로서 사용될 때 열분해반응 또는 촉매분해반응과 같은 흡열반응(Endothermic reaction)을 거쳐 분해가 되는데 이러한 특성을 지닌 연료를 흡열연료(Endothermic fuels)라고 한다. 흡열반응은 촉매를 통해 개선될 수 있지만, 코킹침적이 형성되기 이전까지의 온도로 제한된다. 본 연구에서는 흡열연료에 관련된 주요 기술을 조사하여 기초연구에 활용하고자 하였다.

• 한국환경과학회지
• /
• 제22권9호
• /
• pp.1097-1103
• /
• 2013

Tetrafluoromethane($CF_4$) have been widely used as etching and chemical vapor deposition gases for semiconductor manufacturing processes. $CF_4$ decomposition efficiency using microwave system was carried out as a function of the microwave power, the reaction temperature, and the quantity of $Al_2O_3$ addition. High reaction temperature and addition of $Al_2O_3$ increased the $CF_4$ removal efficiencies and the $CO_2/CF_4$ ratio. When the SA30 (SiC+30wt%$Al_2O_3$) and SA50 (SiC+50wt%$Al_2O_3$) were used, complete $CF_4$ removal was achieved at $1000^{\circ}C$. The $CF_4$ was reacted with $Al_2O_3$ and by-products such as $CO_2/CF_4$ and $AlF_3$ were produced. Significant amount of by-product such as $AlF_3$ was identified by X-ray powder diffraction analysis. It also showed that the ${\gamma}-Al_2O_3$ was transformed to ${\alpha}-Al_2O_3$ after microwave thermal reaction.

• 청정기술
• /
• 제23권3호
• /
• pp.308-313
• /
• 2017

본 연구에서는 Graphite Felt (GF) 전극의 표면에 산소와 질소의 도핑을 통하여 전기화학적 특성을 개선하고, 이의 촉매화학적 효과를 바나듐 레독스 흐름전지의 양극과 음극의 특성비교를 통하여 관찰하였다. 탄소전극 표면의 산소와 질소 동시 도핑은 GF 샘플을 773 K에서 암모니아-공기 ($NH_3=50%$, $O_2=10%$) 혼합가스에 노출시켜 Chemical Vapor Deposition (CVD) 방법으로 제조하였다. 이러한 산소-질소 동시 도핑의 전기화학적 효과는 산소만으로 도핑 처리된 GF 샘플과 비교하여 분석, 평가하였다. 탄소전극 샘플들의 표면 구조와 화학적 조성은 Scanning Electron Microscopy (SEM)와 X-ray Photoelectron Spectroscopy (XPS) 방법을 통하여 분석하였다. 결과물로 얻어진 탄소전극은 바나듐 레독스-흐름전지의 양극과 음극에 동시 적용하여 충-방전 사이클을 진행하고, 각 전극이 흐름전지의 효율과 양극과 음극에서의 전기화학적 특성에 미치는 효과를 비교하여 분석하였다. 산소와 질소의 동시 도핑으로 처리된 GF 전극은 산소만으로 활성화된 전극에 비하여 흐름전지의 전압 및 에너지 효율에서 2% 이상의 향상 효과를 보여주었다. 특히, 탄소전극 표면의 산소-질소의 동시 도핑은 음극반응에서 우수한 전기화학적 특성을 유도하는 것을 확인하였다.

• International Journal of Automotive Technology
• /
• 제8권6호
• /
• pp.667-674
• /
• 2007

Various types of NOx storage catalysts for NGV's were designed, manufactured, and tested in this work on a model gas test bench. As in most of other studies on NOx storage catalyst, alkaline earth metal barium(Ba) was used as the NOx adsorbing substance. The barium-based experimental catalysts were designed to contain different amounts of Ba and precious metals at various ratios. Reaction tests were performed to investigate the NOx storage capacity and the NOx conversion efficiency of the experimental catalysts. From the results, it was found that when Ba loading of a catalyst was increased, the quantity of NOx stored in the catalyst increased in the high temperature range over 350. With more Ba deposition, the NOx conversion efficiency as well as its peak value increased in the high temperature range, but decreased in the low temperature range. The best of de-NOx catalyst tested in this study was catalyst B, which was loaded with 42.8 g/L of Ba in addition to Pt, Pd and Rh in the ratio of 7:7:1. In the low temperature range under $450^{\circ}C$, the NOx conversion efficiencies of the catalysts were lower when $CH_4$, instead of either $C_3H_6$ or $C_3H_8$, was used as the reductant.

• 한국방사성폐기물학회:학술대회논문집
• /
• 한국방사성폐기물학회 2017년도 추계학술논문요약집
• /
• pp.73-73
• /
• 2017

Pyroprocessing at KAERI (Korea Atomic Energy Research Institute) consists of pretreatment, electroreduction, electrorefining and electrowinning. SFR (Sodium Fast Reactor) fuel is prepared from the electrowinning process which is composed of LCC (Liquid Cadmium Process) and Cd distillation et al. LCC is an electrochemical process to obtain actinides from spent fuel. In order to recover actinides inert anodes such as carbon material are used, where chlorine gas ($Cl_2$) evolves on the surface of the carbon material. And, stainless steel (SUS) crucible should be installed in large-scale electrowinning system. Therefore, the effect of chlorine on the SUS material needs to be studied. LiCl-KCl-$UCl_3$-$NdCl_3$-$CeCl_3$-$LaCl_3$-$YCl_3$ salt was contained in 2 kinds of electrolytic crucible having an inner diameter of 5cm, made of an insulated alumina and an SUS, respectively. And, three kinds of electrodes such as cathode, anode, reference were used for the electrochemical experiments. Both solid tungsten (W) and LCC were used as cathodes. Cd of 45 g as the cathode material was contained in alumina crucibles for the deposition experiments, where the crucible has an inner diameter of 3 cm. Glassy carbon rod with the diameter of 0.3 cm was employed as an anode, where shroud was not used for the anode. A pyrex tube containing LiCl-KCl-1mol% AgCl and silver (Ag) wire having a diameter of 0.1cm was used as a reference electrode. Electrodeposition experiments were conducted at $500^{\circ}C$ at the current densities of $50{\sim}100mA/cm^2$. In conclusion, Fe ions were produced in the salt during the electrodeposition by the reaction of chlorine evolved from the anode and Fe of the SUS crucible and thereby LCC system using SUS crucible showed very low current efficiencies compared with the system using the insulated alumina crucible. Anode shroud needs to be installed around the glassy carbon not to influence surrounding SUS material.