• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2009년도 하계학술대회 논문집
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• pp.209-209
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• 2009

Fabrication of p-type ZnO has already proven difficult and usually inconsistent despite numerous worldwide efforts. Many research groups studied electrical and optical properties P, Li, As, N single doped ZnO thin film. In P-doped ZnO thin film, the reproducibility of p-type conduction with $P_2O_5$ as a dopant source was shown to be relatively poor. In this study, we made P single doped and Li & P co-doped ZnO target. To investigate electrical and optical properties of P single doped and Li & P co-doped ZnO thin film using $P_2O_5$ and $Li_3PO_4$ dopant source respectively was deposited by PLD. The growth temperature was changed 500, $700^{\circ}C$ and various oxygen partial pressure and post-annealing conditions was changed temperature, different gas ambient($O_2,N_2$). We investigate that how to change electrical and optical properties as function of growth temperature, oxygen partial pressure and post-annealing(RTA).

• 센서학회지
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• 제10권4호
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• pp.222-231
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• 2001

$SnO_2$의 물성을 $Fe_2O_3$ 첨가량, 산소분압, CO 기체농도, 그리고 온도의 함수로서 관찰하였다. 시편은 후막인쇄 기법으로 알루미나 기판 위에 제조하였다. $700^{\circ}C$/6h 소성한 시편들의 $Fe_2O_3$첨가량에 따른 미세구조와 입자분포의 차이는 거의 없었다. $Fe_2O_3$를 첨가하지 않은 $SnO_2$의 전기적 성질은 소성온도가 낮은 경우와 산소분압이 낮은 경우에 전도성이 높게 측정되었다. $Fe_2O_3$를 첨가한 $SnO_2$의 전도성은 측정온도 증가로 증가하지만 $Fe_2O_3$ 첨가량 증가로 전도성은 감소하였다. 산소분압 의존성은 $Fe_2O_3$ 첨가로 감소하였다. CO 가스에 대한 기체 센서 특성 중 감도는 $350^{\circ}C$, 0.1 mol% $Fe_2O_3$를 첨가한 경우에 가장 높았고, 재현성 및 응답성도 양호하게 나타났다.

• The Korean Journal of Ceramics
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• 제4권2호
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• pp.114-121
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• 1998

Using Hebb-Wagner's asymmetric cell, partial conductivities of holes and electrons in yttria stabilized zirconia doped with 10 mol% TiO2 have been estimated by a dc polarization measurement. The current interrruption method and ac impedance measurements have been also made to evaluate the ionic conductivity and to examine the consistency of the partial conductivities. Partial conductivities of electrons(σn) and holes (σp) were found to be pro-peortional to -1/4 and 1/4 power of partial pressure of oxygen gas, respectively, except for σn at reducing conditions. In comparison with 5 mol% doped YSZ, σn was found to increase with the increase of TiO2 concentration, but σp stayed at almost a constant value.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제4권2호
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• pp.95-102
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• 2000

Methane combustion over perovskite-type oxides prepared using the malic acid method was investigated. To enhance the catalytic activity, the perovskite oxides were modified by the substitution of metal into their A or B site. In addition, the reaction conditions, such as the temperature, space velocity, and partial pressure of the methane were varied to understand their effect on the catalytic performance. With the LaCoO3-type catalyst, the partial substitution of Sr or Ba into site A enhanced the catalytic activity in the methane combustion. With the LaBO3(B=Co, Fe, Mn, Cu)-type catalyst, the catalytic activities were exhibited in the order of Co>Fe Mn>Cu. Futhermore, the partial substitution of Co into site B enhanced the catalytic activity, whereas an excess amount of Co decreased the activity. The surface area and catalytic activity of the perovskite catalysts prepared using the malic acid method showed higher values than those prepared using the solid reaction method. The catalytic activity was enhanced with decreased methane concentration and with a decrease in the space velocity.

• 한국재료학회지
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• 제24권2호
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• pp.81-86
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• 2014

The nitrogen solubility and nitride capacity of $CaO-SiO_2-Al_2O_3-MgO-CaF_2$ slag systems were measured by using gas-liquid equilibration at 1773K. The nitrogen solubility of this slag system decreased with increasing CO partial pressure, with the linear relationship between nitrogen contents and oxygen partial pressure being -3/4. This system was expected to show two types of nitride solution behavior. First, the nitrogen solubility decreased to a minimum value and then increased with the increase of CaO contents. These mechanisms were explained by considering that nitrogen can dissolve into slags as "free nitride" at high basicities and as "incorporated nitride" within the network at low basicities. Also, the basicity of slag and nitride capacity were explained by using optical basicity. The nitrogen contents exhibited temperature dependence, showing an increase in nitrogen contents with increasing temperature.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 1999년도 춘계 학술발표회 논문집
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• pp.225-228
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• 1999

MCFC의 장수명화를 위해 기존의 Li$_2$CO$_3$-K$_2$CO$_3$계 전해질을 Li$_2$CO$_3$-$Na_2$CO$_3$계 용융탄산염으로 대체함으로써, 전지 수명을 단축시키는 NiO의 용출을 억제하고자하는 연구가 진행중에 있다. 이러한 대체 Li$_2$CO$_3$-$Na_2$CO$_3$ 전해질은 실제 전지에서 사용되고 있는 분리판 재료인 스테인레스강의 안정성에도 기존의 Li$_2$CO$_3$-K$_2$CO$_3$ 혼합염과는 다른 경향을 보이는 것으로 알려져 있다.(중략)

• 에너지공학
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• 제12권3호
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• pp.231-240
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• 2003

국내 발전용으로 수입되는 5개 석탄 촤의 이산화탄소 가스화 반응성을 전압력 0.5∼2.0 MPa, 반응온도 850∼100$0^{\circ}C$의 범위에서 가압열중량분석기를 사용하여 고찰하였다. 석탄 등급, 촤의 초기 물성, 그리고 압력이 반응속도에 미치는 영향을 평가하였다. 낮은 등급의 석탄 촤의 반응성이 높은 등급의 석탄 촤보다 좋았으며 이는 촤의 기공구조와 반응 표면적의 항으로 설명되었다. 기공특성 데이터중 대/중간 기공이 반응성에 미치는 영향이 켰으며 이는 반응가스가 촤 표면적으로 확산하는 통로를 제공하기 때문인 것으로 보인다. $CO_2$ 분압 0.18∼0.495 MPa 범위에서 촤의 반응속도는 분압에 비례하였으며 반응 차수는 약 0.4∼0.7의 범위에 있었다. 반응속도에 대한 전압력의 영향은 작은 것으로 나타났으며 미반응핵 모델에 근거한 5개 촤의 반응성 지수를 구하였다.

• 한국포장학회지
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• 제26권2호
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• pp.105-112
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• 2020

어린 싹을 길러 이용하는 채소에 대한 관심이 커지고 있어, 무 싹채소의 생육 증진과 유통 중 나타나는 영향을 검토하고자 CO₂처리 효과를 검토하였다. 본 실험에서는 재배 중 CO₂ 처리를 가스나 탄산수 형태로 하여, 생육뿐만 아니라 수확후 모의유통 중 포장 내의 생체중량 감소, 선도와 hue angle 등 수확후 변화 정도를 조사하였다. 재배 후 수확 시 생육에서 처리 여부에 따라서는 CO₂ 처리가 무처리보다 경장이 약간 길어지는 효과가 있었으며, 엽록소형광이나 SOD 값에서 무처리와 CO₂ 처리가 다소 다른 경향을 보였다. 그러나 CO₂ 처리 방법 간의 차이를 언급하기는 어려워 탄산가스 대신 탄산수 이용의 가능성을 보였다. 수확 후 포장 내의 CO₂ 처리로 인해 무 싹채소의 O₂ 소모가 크고 CO₂ 축적 정도가 다소 높아졌으며, 모의유통 중에 수확전 CO₂ 처리가 hue angle 값을 비롯하여 SPAD, 외관 등에서 낮은 수치를 보여주었다. 그러나 CO₂ 처리 방법 간에는 큰 차이를 보이지 않은 것으로 나타났다. 무 싹채소의 재배 중 CO₂ 처리에 의한 처리가 경경 등의 생육량을 증가시키나, 모의유통 시 수확후 선도 유지의 효과가 크지 않아, 재배 중 다른 방법을 통한 품질을 개선할 수 있도록 연구가 더 필요한 것으로 생각된다.

• Bulletin of the Korean Chemical Society
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• 제31권5호
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• pp.1295-1300
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• 2010

The $CO_2-CH_4$ reaction catalyzed by Ni/silicon wafers was kinetically studied by using a photoacoustic technique. The catalytic reaction was performed at various partial pressures of $CO_2$ and $CH_4$ (50 Torr total pressure of $CO_2/CH_4/N_2$) in the temperature range of 500 - $650^{\circ}C$ in a static reactor system. The photoacoustic signal that varied with the $CO_2$ concentration during the catalytic reaction was recorded as a function of time. Under the reaction conditions, the $CO_2$ photoacoustic measurements showed the as-prepared Ni thin film sample to be inactive for the reaction, while the $CO_2/CH_4$ reactions carried out in the presence of the sample pre-treated in $H_2$ at $600^{\circ}C$ were associated with significant time-dependent changes in the $CO_2$ photoacoustic signal. The rate of $CO_2$ disappearance was measured from the $CO_2$ photoacoustic signal data in the early reaction period of 50 - 150 sec to obtain precise kinetic data. The apparent activation energy for $CO_2$ consumption was determined to be 6.9 kcal/mol from the $CO_2$ disappearance rates. The partial reaction orders, determined from the $CO_2$ disappearance rates measured at various $PCO{_2}'S$ and $PCH{_4}'S$ at $600^{\circ}C$, were determined to be 0.33 for $CH_4$ and 0.63 for $CO_2$, respectively. Kinetic data obtained in these measurements were compared with previous works and were discussed to construct a catalytic reaction mechanism for the $CO_2-CH_4$ reaction over Ni/silicon wafer at low pressures.

• 한국연소학회지
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• 제22권4호
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• pp.19-26
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• 2017

This study investigates the gasification of coal char by $CO_2$ under high pressures in a drop tube furnace(DTF). The rate constants are derived for the shrinking core model using the conventional method based on the set reactor conditions. The computational fluid dynamic(CFD) simulations adopting the rate constants revealed that the carbon conversion was much slower than the experimental results, especially under high temperature and high partial pressure of reactants. Three reasons were identified for the discrepancy: i) shorter reaction time because of the entry region for heating, ii) lower particle temperature by the endothermic reaction, and iii) lower partial pressure of $CO_2$ by its consumption. Therefore, the rate constants were corrected based on the actual reaction conditions of the char. The CFD results updated using the corrected rate constants well matched with the measured values. Such correction of reaction conditions in a DTF is essential in deriving rate constants for any char conversion models by $H_2O$ and $O_2$ as well as $CO_2$.