• 한국표면공학회지
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• 제52권3호
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• pp.150-155
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• 2019

The carbon electrode was modified through manganese-catalyzed hydrogenation method for high energy density vanadium redox flow battery (VRFB). During the catalytic hydrogenation, the manganese oxide deposited at the surface of the carbon electrode stimulated the conversion reaction from carbon to methane gas. This reaction causes the penetration of the manganese and excavates a number of cavities at electrode surface, which increases the electrochemical activity by inducing additional electrochemically active site. The formation of the porous surface was confirmed by the scanning electron microscopy (SEM) images. Finally, the electrochemical performance test of the electrode with the porous surface showed lower polarization and high reversibility in the cathodic reaction compared to the conventional electrode.

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 1997년도 춘계학술발표회논문집(2)
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• pp.159-164
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• 1997

Pyrolytic carbon layer was coated on A1203 balls by fluidized bed type chemical vapour deposition unit to develop the coating technology for the preparation of coated nuclear fuel. The deposition was carried out at the temperature ranges between 110$0^{\circ}C$ and 130$0^{\circ}C$ with various gas contents and flow rates. Source and carrier gas were propane and argon, respectively. X-ray analysis shows that the deposition layer was typical carbon spectra. The growth rate of carbon layer depended on the amount of source gas and the deposition temperature. For the alumina balls with 2mm in diameter, the deposition rate was 11${\mu}{\textrm}{m}$/hr in the flow gases containing 30% source gas at 130$0^{\circ}C$ with a total flow rate of 2.0$\ell$/min. Microstructural observation of the deposits with scanning electron microscope revealed that the deposits had relatively dense and isotropic structure. Chemical analysis by energy dispersive spectroscopy showed that the layer was pure carbon.

• 한국환경과학회지
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• 제21권11호
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• pp.1371-1377
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• 2012

The simulated dyes solution containing Basic Red 46(BR 46), Yellow 21(Y 21), and Maxilon Blue 30(MB 30) were electrochemically oxidized using carbon fiber as an anode. The electrolyses were performed in a electrolytic flow cell constructed by Vycor glass tube. The carbon fiber was positioned in the inside of Vycor glass tube and platinum wire coiled around outside of tube as a cathode. Several operating variables, such as current, time, pH and flow rate of solution were studied. Increasing current density would lead to a corresponding increase in the dye removal efficiency 99.2 % at a 200 mA. The electrolyses time could also improve and removal efficiency was about 99 % after 1.5 hours of electrolyses. The removal efficiency was increased with the increase of flow rate of solution and optimum flow rate was 5 mL/min. THe pHs of solution affect the removal efficiency. The removal efficiency was decreased with the increase of pH of solution and optimum pH was 5.05 (0.1 M $KNO_3$).

• 멤브레인
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• 제16권4호
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• pp.252-258
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• 2006

배기가스로부터 폴리이서술폰 분리막을 이용하여 이산화탄소 분리 특성을 수치해석 방법으로 분석하였다. 공급 기체와 투과 기체가 서로 다른 방향으로 흐르는 향류 흐름 시스템에 대한 분리막 공정 지배 방정식을 유한 차분법으로 전개하였으며 Compaq Visual Fortran 6.6 소프트웨어를 이용 공정 모사하였다. 개발된 프로그램을 사용하여 수치해석을 수행한 결과 이산화탄소 투과특성에 영향을 주는 가장 중요한 인자로는 이산화탄소 투과 구동력과 체류시간임을 알 수 있었다. 동일한 조건에서 향류 흐름 공정모사에 의한 투과 측 이산화탄소 농도와 투과량은 병류 흐름 공정모사 결과보다 소폭 증가함을 확인하였다.

• Spatial Information Research
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• 제20권5호
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• pp.1-13
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• 2012

본 연구는 그동안 이산화탄소의 유동 방향 연구에서 지적된 지상관측자료의 시 공간적 제약성을 극복하고자, 최초의 온실가스 측정 전용 위성인 GOSAT을 활용하여 동북아시아 지역의 계절별 이산화탄소의 유동 방향을 평가하고자 하였다. 이를 위해 크리깅 분석을 적용하여 결측값을 보완하고, 이방성 베리오그램을 통해 전체적인 이산화탄소의 유동 방향을 결정하였다. 그 결과 동북아시아의 이산화탄소 공간적 분포 양상은 위도대에 일치하는 변화추세를 확인할 수 있었으며, 계절별 유동성은 봄, 가을, 겨울의 경우 남동쪽 및 동쪽으로 유동되는 이산화탄소가 주를 이루어 나타났으며, 여름에 경우 북쪽 및 북동쪽으로 이동하는 흐름이 나타났다. 이러한 결과는 동북아시아 지역에서 나타나는 계절풍과 유사한 흐름으로 주로 서에서 동으로 이동되는 경우가 주를 이루고 있음을 알 수 있으며, 이는 중국에서 배출된 이산화탄소가 한반도와 일본까지 영향을 미치고 있음을 확인할 수 있다. 그러나 이산화탄소의 유동은 인위적 배출원과 식생의 호흡, 해양의 배출과 흡수 등의 다양한 요인과 결부되어 달라지기 때문에 이산화탄소 유동에 개입되는 다양한 변수와 상관성을 평가하는 후속연구가 필요할 것으로 사료된다.

• 한국추진공학회지
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• 제16권2호
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• pp.73-79
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• 2012

본 연구에서는 높은 강도의 가스흐름으로부터 연소실 내부를 보호하기 위하여 carbon fabric을 삽입한 EPDM계 내열재를 개발하였다. 연소관 내열재의 삭마 특성을 시험하기 위하여 6-inch 모사모타에 extension tube를 연결하였고, 모타와 extension tube 사이에 구멍이 있는 FRP를 삽입하여 추진제 연소 시 높은 강도의 가스흐름을 유도하였다. 결과적으로 연소시험후 carbon fabric/EPDM 연소관 내열재의 삭마량은 다른 연소관 내열재들에 비해 감소하는 것으로 확인되었다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2011년도 제37회 추계학술대회논문집
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• pp.85-91
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• 2011

본 연구에서는 높은 강도의 가스흐름으로부터 연소실 내부를 보호하기 위하여 carbon fabric을 삽입한 EPDM계 내열재를 개발하였다. 연소관 내열재의 삭마 특성을 시험하기 위하여 6-inch 모사모타에 extension tube를 연결하였고, 모타와 extension tube 사이에 구멍이 있는 FRP를 삽입하여 추진제 연소시 높은 강도의 가스흐름을 유도하였다. 결과적으로 연소시험후 carbon fabric/EPDM 연소관 내열재의 삭마량은 다른 연소관 내열재들에 비해 감소하는 것으로 확인되었다.

• 한국세라믹학회지
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• 제20권2호
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• pp.166-172
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• 1983

In this study the sillicon-alloyed isotropic pyrolytic carbon was deposited in the tumbling bed from the pyrolysis of propane and silicon tetrachloride and investigated whether the silicon-alloyed isotropic pyrolytic carbon deposited in this study was usable as bionaterial or not. The silicon-allyed isotropic pyrolytic carbon was varied by controlling the process variables such as propane con-concentration and the argon flow rate flowing in to the silicon tetrachloride bubbler at a fixed reaction bed tempera-ture of 120$0^{\circ}C$ a rotation of reaction tube of 40 rpm a bed particle weight of 7.5 g and a total flow rate of 21/min; the propane concentration was varied from 10 to 70 and the argon flow rate flowing into the silicon tetrachloride bubble from 0 to 1000 cc/min. The results show that the silicon-alloyed isotropic pyrolytic carbon was obtained at all conditions investigated, . And then the alloyed silicon content is rangion from 7 to 14.5 wt%. The density and deposition rate of deposited silicon-alloyed isotropic carbon increased axxording to silicon content and propane concentration. And the apparent crystal-size(Lc) of pyrolytic carbon is not changed with silicon content. The density and apparant crystallite size are respec-tively in the range of 1.94 to 2.06 and 20 to 25$\AA$ It is shown that the silicon-alloyed isotropic pyrolytic carbon ob-tained in this experiment is usable as biomaterial.

• 한국응용과학기술학회지
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• 제21권1호
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• pp.45-50
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• 2004

The effects of reaction temperature and flow rate of reactants on the methane conversion, product selectivity, product ratio, and carbon deposition were investigated with 13wt% Ni/MgO catalyst. Reaction temperatures were changed from 600 to $850^{\circ}C$, and reactants flow rates were changed from 100 to 200 mL/mim. There were no significant changes in the methane conversion observed in the range of temperatures used. It is possibly stemmed from the nearly total exhaustion of oxygen introduced. The selectiveties of hydrogen and carbon monoxide did not largely depend on the reaction temperature. The selectivities of hydrogen and carbon monoxide were 96 and 90%, respectively. Carbon deposition observed was the smallest at $750^{\circ}C$ and the largest at $850^{\circ}C$. It is found that the proper reaction temperature is $750^{\circ}C$. The best reactant flow rate was 150 ml/min.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.1979-1983
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• 2008

The effects of carbon dioxide addition to oxygen have been investigated with swirl-stabilized premixed methane flame in a laboratory-scale pre-mixed combustor. The methane fuel and oxydant mixture gas ($CO_2$ and $O_2$) were mixed in a pre-mixer and introduced to the combustor through different degrees of swirl vanes. The flame characteristics were examined for different amount of carbon dioxide addition to the methane fuel and different swirl strengths. The effects of carbon dioxide addition and swirl intensity on the combustion characteristics of pre-mixed methane flames were examined using chemiluminescence techniques to provide information about flow field. The results show that the flame area increases at upstream of reaction zone because of increase in recirculation flow for increase in swirl intensity. The flame area is also increased at the downstream zone by recirculation flow because of increase in swirl intensity which results in higher centrifugal force. The OH and CH radical intensity of reaction zone decrease with carbon dioxide addition because the carbon dioxide plays a role of dilution gas in the reaction zone.