• Bulletin of the Korean Chemical Society
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• 제9권2호
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• pp.81-84
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• 1988

The CO oxidation was performed on $H_2$-reduced NiO-${\alpha}-Fe_2O_3$ in the temperature range 150-$250^{\circ}C$. The kinetic study and the conductivity measurements indicate the oxidation reaction follows Langmuir-Rideal type process that is uncommon in heterogeneous catalyst$^1$. No active site is found on the catalyst surface for CO adsorption, but an oxygen vacancy adsorbs an oxygen, and this step is rate initiation. The partial orders are half for $O_2$ and first for CO, respectively. Apparent activation energy for over-all reaction is 9.05 kcal/mol.

• Journal of Industrial and Engineering Chemistry
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• 제67권
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• pp.448-460
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• 2018

Copper nanoparticle-doped and graphitic carbon nanofibers-covered porous carbon beads were used as an efficient catalyst for treating synthetic phenolic water by catalytic wet air oxidation (CWAO) in a packed bed reactor over 10-30 bar and $180-230^{\circ}C$, with air and water flowing co-currently. A mathematical model based on reaction kinetics assuming degradation in both heterogeneous and homogeneous phases was developed to predict reduction in chemical oxygen demand (COD) under a continuous operation with recycle. The catalyst and process also showed complete COD reduction (>99%) without leaching of Cu against a high COD (~120,000 mg/L) containing industrial wastewater.

• 한국입자에어로졸학회지
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• 제4권2호
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• pp.51-67
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• 2008

In this study, we devoted to kinetic measurement of the catalytic oxidation of iron-containing flame soot particles and better understanding the role of catalytic particles on carbon oxidation in particular at low temperature, targeting on autothermal regeneration of diesel particulate filter by diesel exhaust gas. Carbon-based Fe-containing particles generated by spraying ferrocene-doped diesel fuel in an oxy-hydrogen flame are tested and compared with a commercial carbon black powder for thermogravimetric analysis (TGA), secondary ion mass spectrometry (SIMS), Fourier-transform infrared spectroscopy (FTIR), Induced coupled plasma-Atomic emission spectroscopy (ICP-AES), and High-resolution transmission electron microscopy (HR-TEM). As a result, we found that a small amount of the ferrocene addition led to significant reductions in a on-set temperature and an activation energy of the carbon oxidation as well. An oxygenated surface complex forming at the particle surface could be thought as active species that would be readily consumed in particular at low temperature.

• 한국표면공학회:학술대회논문집
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• 한국표면공학회 2011년도 춘계학술대회 및 Fine pattern PCB 표면 처리 기술 워크샵
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• pp.96-97
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• 2011

The T23 steel, whose composition was Fe-2.3%Cr-1.6%W, was arc-melted, and oxidized between $600^{\circ}C$ and $900^{\circ}C$ in air for up to 7 months. The amount of precipitates in the arc-melted microstructure was as large as 11.4 vol.%. The precipitates increased the oxidation rate of the arc-melted T23 steel. Owing to the low amount of Cr in the T23 steel, breakaway oxidation occurred after a few hours during oxidation above $700^{\circ}C$ in both arc-melted and as-received T23 steels. The scales that formed on arc-melted and as-received T23 steels were similar to each other. They consisted primarily of the outer $Fe_2O_3$ layer and the inner ($Fe_2O_3$, $FeCr_2O_4$)-mixed layer. The precipitates increased the microhardness and the oxidation rates.

• 한국환경과학회지
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• 제29권12호
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• pp.1205-1211
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• 2020

In this study, the applicability of reduction-oxidation-linked treatment was evaluated for nitrobenzene and a by-product by analyzing the reaction kinetics. Nitrobenzene showed very low reactivity to persulfate that was activated using various methods. Nitrobenzene effectively reacted through the reduction process using Zero-Valent Iron (ZVI). However, aniline, a toxic substance, was produced as a by-product. Reduction-oxidation-linked treatment is a method that can allow the oxidative degradation of aniline after reducing nitrobenzene to aniline. The experimental results show improved reactivity and complete decomposition of the by-product. Improved reactivity and decomposition of the by-product were observed even under conditions in which the reduction-oxidation reaction was induced simultaneously. No activator was injected for persulfate activation in the process of reducing oxidant linkage, and the activation reaction was induced by ferrous iron eluted from the ZVI. This indicates that this method can be implemented relatively simply.

• 한국수소및신에너지학회논문집
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• 제33권2호
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• pp.148-157
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• 2022

Research on hydrogen storage is active to properly deal with hydrogen, which is considered a next-generation energy medium. In particular, research on metal hydride with excellent safety and energy efficiency has attracted attention, and among them, magnesium-based hydrogen storage alloys have been studied for a long time due to their high storage density, low cost, and abundance. However, Mg-based alloys require high temperature conditions due to strong binding enthalpy, and have many difficulties due to slow hydrogenation kinetics and reduction in hydrogen storage capacity due to oxidation, and various strategies have been proposed for this. This research manufactured Mg₂Ni to improve hydrogenation kinetics and synthesize about 5, 10, 20 wt% of CaF₂ as a catalyst for controlling oxidation. Mg₂NiHx-CaF₂ produced by hydrogen induced mechanical alloying analyzed hydrogenation kinetics through an automatic PCT measurement system under conditions of 423 K, 523 K, and 623 K. In addition, material life cycle assessment was conducted through Gabi software and CML 2001 and Eco-Indicator 99' methodology, and the environmental impact characteristics of the manufacturing process of the composites were analyzed. In conclusion, it was found that the effects of resource depletion (ARD) and fossil fuels had a higher burden than other impact categories.

• Bulletin of the Korean Chemical Society
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• 제35권5호
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• pp.1379-1384
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• 2014

${\alpha}-Fe_2O_3$ spherical particles having an average diameter of ca. 420 nm and ${\alpha}-Fe_2O_3$ fine particles (< 10 ${\mu}m$ particle size) were prepared to examine as catalysts for CO oxidation. Kinetic studies on the catalytic reactions were performed in a flow reactor using an on-line gas chromatography system operated at 1 atm. The apparent activation energies and the partial orders with respect to CO and $O_2$ were determined from the rates of CO disappearance in the reaction stage showing a constant catalytic activity. In the temperature range of $150-275^{\circ}C$, the apparent activation energies were calculated to be 13.7 kcal/mol on the ${\alpha}-Fe_2O_3$ spherical submicron clusters and 15.0 kcal/mol on the ${\alpha}-Fe_2O_3$ fine powder. The Pco and $Po_2$ dependencies of rate were investigated at various partial pressures of CO and $O_2$ at $250^{\circ}C$. Zero-order kinetics were observed for $O_2$ on both the catalysts, but the reaction order for CO was observed as first-order on the ${\alpha}-Fe_2O_3$ fine powder and 0.75-order on the ${\alpha}-Fe_2O_3$ spherical submicron clusters. The catalytic processes including the inhibition process by $CO_2$ on the ${\alpha}-Fe_2O_3$ spherical submicron powder are discussed according to the kinetic results. The catalysts were characterized using XRD (X-ray powder diffraction), FE-SEM (field emission-scanning electron microscopy), HR-TEM (high resolution-transmission electron microscopy), and $N_2$ sorption measurements.

• 대한환경공학회지
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• 제28권4호
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• pp.397-401
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• 2006

본 연구에서는 지하수내의 TCE 오염물질을 과망간산을 이용하여 산화분해할 경우의 반응율에 대하여 평가하였다. 또한 최적의 산화제 주입량 결정을 위하여 TCE뿐만 아니라 지하수 대수층 물질에 의한 과망간산의 소모율에 대한 실험을 수행하였다. 대수층 물질이 없는 경우에 과망간산에 의한 TCE의 분해는 효과적으로 이루어졌으며 500 mg/L의 과망간산 농도에서 $k_{obs}=5.24{\times}10^{-3}s^{-1}$의 유사 1차반응계수를 얻었다. TCE와 과망간산에 대하여 각각 1차반응, 전체적으로는 2차반응을 나타내었다. 이때의 반응계수는 $k=0.65{\pm}0.08M^{-1}s^{-1}$였다. 반면 대수층 물질 자체는 산화제인 과망간산과 활발한 반응을 하여 상당한 소모효과를 나타내었으며 이는 대수층 물질내에 존재하는 금속산화물에 의한 것이라 판단된다.

• 에너지공학
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• 제18권4호
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• pp.239-246
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• 2009

본 논문에서는 주위 가스 온도와 체류시간에 따른 아 역청탄 촤 입자의 연소 특성에 관한 기본적인 연구를 진행하였다. 실험용 장비로써 노 내 온도 범위가 $900^{\circ}C$에서 $1400^{\circ}C$까지 조절이 가능한 DTF(drop tube furnace)를 설치하였고, 온도가 보정된 two color pyrometer를 DTF의상부에 장착하여 촤가 산화할 때의 입자 온도를 측정할 수 있게 하였다. 촤 산화 시 반응한 총 질량을 구하기 위해 열중량 분석기를 사용하였으며, 회분 추적법을 통해분석하였다. 이를 통해대기압 조건에서 촤가산화 할때질량 및 면적 반응성, 반응속도 상수들을 결정하였다.

• 대한화학회지
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• 제18권2호
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• pp.117-125
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• 1974

반응온도 $40^{\circ}C∼95^{\circ}C$에서 일산화탄소를 여러가지 온도에서 처리한 산화니켈을 촉매로 하여 산화시켰다. 일산화탄소의 산화 속도는 낮은 온도에서 진공속에서 처리한 산화니켈상에서 제일 빠르다. 이때 반응속도는 일차 반응에 따르며 활성화 에너지는 이 반응온도 범위에서 4kcal정도이다. 공기중에서 $NiCO_3$를 분해하여 얻은 산화니켈촉매는 반응 온도가 $95^{\circ}C$이상에서도 활성이 없다. 그러나 이산화 니켈을 진공에서 처리했을 경우 이 반응온도 범위에서 활성이 있다. 이때 산화니켈의 비화학 양론적인 과량의 산소가 일산화탄소의 산화속도를 지배하는 것 같다.