• 대한화학회지
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• 제38권10호
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• pp.705-709
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• 1994

1M 황산용액에서 세륨(Ⅳ) 이온에 의한 말론산의 산화반응에 관한 반응속도를 분광광도법으로 연구하였다. 말론산이 과량으로 존재하는 조건하에서 측정된 유사일차 속도상수, $k_{obs}$는 말론산의 농도, [MA]에 따라 크게 의존함을 보였으며 $k_{obs}$ = (0.592[MA])/(1+14.5[MA]$^2$)의 관계를 만족하였다. 이에 근거하여 반응메카니즘을 제안하였다. 말론산의 산해리에 의해 생성된 enolate형 음이온과 Ce(Ⅳ)간의 전자이동반응이 반응속도 결정단계이며, MA의 고농도하에서 Ce(Ⅳ)과 enolate형 음이온간의 1:2 chelate생성반응에 의하여 Ce(Ⅳ)의 농도가 감소하여 산화반응이 억제됨을 알 수 있었다. 본 연구에서 제안된 메카니즘에 근거하여 Sengupta 등에 의해 연구된 pH 의존성을 설명할 수 있었다.

• 폴리머
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• 제25권1호
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• pp.25-32
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• 2001

${\circ}C$ 범위에서 아연과 망간촉매를 사용하여 에스테르 교환반응시켜 반응속도를 살펴보았다. 반응은 반회분식 반응기에서 비등온 조건으로 진행되었고 반응온도와 메탄올 유출량으로 반응성을 평가하였다. 반응모델로서는 관능기 모델과 분자종 모델을 적용하여 상호 비교하였다. 아연촉매를 사용할 경우 DMN과 EG의 반응속도는 methyl hydroxyethyl naphthalate(MHEN)와 EG의 반응속도에 비해 1.4배정도 였으나 망간촉매를 사용할 경우 4.3배정도로 촉매 종류에 따라 반응성이 크게 차이가 있음을 알 수 있었다. 아연촉매의 경우 DMN 및 MHEN과 EG의 반응에 대한 촉매농도의 반응차수는 1보다 작았으나, 망간촉매의 경우 오히려 1보다 컸다. 활성화에너지는 DMN과 MHEN의 분자종 차이에 관계없이 아연과 망간촉매의 경우 각각 25000, 28750 cal/mol이었다. 두 가지 반응모델을 비교하여 본 결과 분자종 모델이 반응현상을 잘 표현함을 알 수 있었다.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1991년도 한국자동제어학술회의논문집(국제학술편); KOEX, Seoul; 22-24 Oct. 1991
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• pp.1873-1878
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• 1991

An high-speed isothermal calorimeter which can trace the progress of a liquid phase reversible reaction was constructed using analog and digital computer. By means of a set point change of the calorimeter, the thermal energy capacity and the heat of reaction in reversible reaction mixture can be measured. The heat of reaction between 2-methyl furan and maleic anhydride and the heat capacities of the adduct were 61,200 J/mol and 2.38 J/ g K, respectively. Also reaction equilibrium constant and reaction rate constants can be estimated from the response curves of the calorimeter.

• Macromolecular Research
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• 제13권1호
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• pp.68-72
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• 2005

A low-molecular-weight poly(lactic acid) was synthesized through the condensation reaction of L-lactic acid. The effects that the catalyst and temperature have on the reaction rate were studied to determine the optimum reaction conditions. The reaction kinetics increased with temperature up to $210^{\circ}C$, but no further increase was observed above this temperature. Among a few selective catalysts, sulfuric acid was the most effective because it maximized the polymerization reaction rate. Reduction of the pressure was another important factor that enhanced this reactions kinetics.

• 한국세라믹학회지
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• 제35권6호
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• pp.569-574
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• 1998

자체의 반응열에 의해 반응이 자발적으로 진행되는 SHS법을 이용하여 $Ti_3AI$ 금속간 화합물의 생성반응에서의 화염대 두계, 반응속도 그리고 겉보기 활성화에너지에 대하여 고찰하였다. 이 반응에서 화염대 두께는 1.4mm이었고, 반응속도는 $0.4g/\textrm{cm}^2{\cdot}sec$이었다. 또한, 반응물의 상대밀도를 조절하여 얻은 실험 data를 이용하여 구한 반응의 겉보기 활성화에너지는 40kJ/mol이었다.

• 청정기술
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• 제19권1호
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• pp.51-58
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• 2013

니켈 촉매 상에서 에탄의 수증기 개질 반응과 수성가스 전환반응 반응에 대한 반응속도 데이터를 얻기 위하여 반응온도와 반응물의 분압을 변화시키면서 반응 실험을 수행하였다. 반응속도 데이터를 사용하여 거듭제곱 속도식 모델(power law kinetic model)과 랭미어-힌쉘우드 모델(Langmuir-Hinshelwood model)의 매개변수를 구하였다. 또한 반응 속도 모델식을 적용하여 PRO/II를 이용한 공정 모사를 통해서 에탄의 수증기 개질 반응기 사이징(sizing)을 수행하였다. 에탄을 반응물로 하여 수증기 개질 반응을 수행한 결과, 단순한 거듭제곱 속도식 모델보다 표면반응에 의하여 반응속도가 결정되는 랭미어-힌쉘우드 모델이 보다 적합하였고, 수성가스 전환반응에 대한 반응속도식은 거듭제곱 속도식 모델이 적합함을 보였다. PRO/II 시뮬레이션을 통해서 수소 생산량에 필요한 반응기의 크기를 결정할 수 있었다.

• 한국환경과학회지
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• 제26권7호
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• pp.859-868
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• 2017

In this study, the reductive dechlorination of triclosan using zero-valent iron (ZVI, $Fe^0$) and modified zero-valent iron (i.e., acid-washed iron (Aw/Fe) and palladium-coated iron (Pd/Fe)) was experimentally investigated, and the reduction characteristics were evaluated by analyzing the reaction kinetics. Triclosan could be reductively decomposed using zero-valent iron. The degradation rates of triclosan were about 50% and 67% when $Fe^0$ and Aw/Fe were used as reductants, respectively, after 8 h of reaction. For the Pd/Fe system, the degradation rate was about 57% after 1 h of reaction. Thus, Pd/Fe exhibited remarkable performance in the reductive degradation of triclosan. Several dechlorinated intermediates were predicted by GC-MS spectrum, and 2-phenoxyphenol was detected as the by-product of the decomposition reaction of triclosan, indicating that reductive dechlorination occurred continuously. As the reaction proceeded, the pH of the solution increased steadily; the pH increase for the Pd/Fe system was smaller than that for the $Fe^0$ and Aw/Fe system. Further, zero-order, first-order, and second-order kinetic models were used to analyze the reaction kinetics. The first-order kinetic model was found to be the best with good correlation for the $Fe^0$ and Aw/Fe system. However, for the Pd/Fe system, the experimental data were evaluated to be well fitted to the second-order kinetic model. The reaction rate constants (k) were in the order of Pd/Fe > Aw/Fe > $Fe^0$, with the rate constant of Pd/Fe being much higher than that of the other two reductants.

• 한국막학회:학술대회논문집
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• 한국막학회 2004년도 Proceedings of the second conference of aseanian membrane society
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• pp.82-85
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• 2004

Microinterface of W/Omicroemulsion prepared by phosphatidylcholine was used as reaction media of hydrolysis of phosphatidylcholine by phospholipaseA$_2$. Phosphatidylcholine was used as an amphiphile and was acted as a substrate. Organic phase of W/Omicroemulsion in this study was prepared by mixed organic solvents i.e. 2,2,4-trimethylpentane (isooctane) as a main solvent and 1-butanol as a co-solvent. The effect of added 1-butanol was remarkable not only on reaction beginning but also on high reaction rate. The hydrolysis reaction was dramatically initiated when 1-butanol was injected into the running isooctane/PC system. The enhancement by 1-butanol addition into single organic solvent was our original finding compare with previous conventional organic solvent. The reaction rate was elevated by the added amount of 1-butanol. The enhanced reaction rate was about 150-folds. This enhancement was speculated as 1-butanol adsorption on the microinterface. The adsorbed 1-butanol improved the properties of microinterface, especially its mobility was increased by difference of the chain length between phosphatidylcholine and 1-butanol. PhospholipaseA$_2$ molecules were located on the microinterface due to modified mobility of microinterface. Located phospholipaseA$_2$ on the microinterface reacted easily with phosphatidylcholine molecule. As a result high reaction rate was obtained. Microinterfacial properties were successfully improved by adsorbed 1-butanol molecule, and were favorable to appear higher reactivity of phospholipaseA$_2$.

• Nuclear Engineering and Technology
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• 제31권2호
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• pp.133-138
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• 1999

Research on the etching reaction of UO$_2$ with CF$_4$/O$_2$gas mixture plasma is carried out. The reaction rates are investigated as a function of CF$_4$/O$_2$ ratio, plasma power, and substrate temperature. It is found that there exists an optimum CF$_4$/O$_2$ ratio around 4:1 at all temperatures up to 37$0^{\circ}C$ and surface analysis using XPS X-ray Photoelectron Spectroscopy) confirms the result. Peak rate at the optimum gas composition increases with increasing temperature. Highest rate obtained in this study leaches 1050 monolayers/min. at 37$0^{\circ}C$ under r. f. power of 150 W, which is equivalent to about 0.5${\mu}{\textrm}{m}$/min. The rate also increases with increasing r. f. power, thus, higher power and higher substrate temperature will undoubtedly raise the etching reaction rate much further. This reaction seems to be an activated process, whose activation energy will be derived in the following experiments.

• 한국환경과학회지
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• 제25권7호
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• pp.905-916
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• 2016

The characteristics of phenol removal and $UV_{254}$ matters variance were investigated and compared by the variation of operating factors (NaCl concentration, air flow rate, initial phenol concentration) in electrochemical reaction (ER) and dielectric barrier discharge plasma reaction (DBDPR), respectively. The phenol removal rate was shown as $1^{st}$ order both in ER and DBDPR. Also, the absorbance of $UV_{254}$ matters which means aromatic intermediates was analyzed to investigate the complete phenol degradation process. In ER, the phenol degradation and aromatic intermediates production rates increased by the increase of NaCl concentration. However, in DBDPR, the variation of NaCl concentration had no effect on the degradation of phenol and $UV_{254}$ matters. Air flow rate had a little effect on the removal of phenol and the variation of $UV_{254}$ matters in ER. The phenol removal rate in ER was a little higher than that in DBDPR. The produced $H_2O_2$ and $O_3$ amounts in ER were 2 times and 10 times higher than those in DBDPR. The chlorine intermediates ($ClO_2$ and free chlorine) were produced in ER, however, they were not produced in DBDPR.