• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2010년도 제34회 춘계학술대회논문집
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• pp.401-405
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• 2010

스크램제트 엔진에 대한 주요 성능설계기법에 대한 연구를 통해 효율적인 해석모델을 제시하였다. 초음속 흡입구의 설계에 있어 최대 전압력회복률을 얻기 위한 Oswatisch의 설계기준을 적용하여 흡입구의 압축각도를 설계하였다. 초음속 연소기의 해석을 위해 준 1차원 해석모델을 제시하였으며, 이에 화학평형 모델 및 유한화학반응 모델의 두 연소모델을 적용함으로서 그 결과를 비교분석하였다. 또한 Starkey의 Waverider에 대한 1차원 해석결과와 비교를 통해 연소모델의 결과를 검증하였다. 가상의 설계조건에 대한 엔진의 성능해석을 수행함으로서 모델의 적용가능성을 확인하였다.

• Bulletin of the Korean Chemical Society
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• 제18권6호
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• pp.628-631
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• 1997

The preparation and characterization of $Co(dmppz)_2(3,6-dbq)_2$ (dmppz=1,4-dimethylpiperazine; 3,6-dbq=3,6-di-tert-butyl-1,2-quinone) are established. Temperature-dependent magnetic moments (100-400 K), variable-temperature IR, and electronic spectra are presented to show that the title complex exhibits an equilibrium via a catechol to cobalt intramolecular electron transfer. At temperatures below 350 K, the charge distribution of the complex is $Co^Ⅲ(dmppz)_2(3,6-dbsq)(3,6-dbcat)$ (3,6-dbsq=3,6-di-tert-butyl-1,2-semiquinonato; 3,6-dbcat=3,6-di-tert-butylcatecholato) whereas at the temperature beyond 390 K, the complex is predominantly Co^Ⅱ(dmppz)_2(3,6-dbsq)_2$ form in the solid state. At the temperature range of 350-390 K a mixture of Co(Ⅲ) and Co(Ⅱ) redox isomers exist at equilibrium. The transition temperature (Tc) of Co(Ⅲ)/Co(Ⅱ) in solution is approximately 50° lower than that in the solid state. In particular, thermal analysis on solid sample of the complex discloses that the transition for the Co(Ⅲ)/Co(Ⅱ) is accompanied by the change in heat content of 12.30 kcal/mol.

• Bulletin of the Korean Chemical Society
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• 제28권9호
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• pp.1523-1530
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• 2007

The first reduction peak of the cyclic voltammogram (CV) for sulfur reduction in dimethyl sulfoxide has been studied using time resolved Fourier transform electrochemical impedance spectroscopic (FTEIS) analysis of small potential step chronoamperometric currents. The FTEIS analysis results reveal that the impedance signals obtained during short potential steps can be resolved into electron transfer reactions of two different time constants in a high frequency region. The FTEIS method provides snap shots of impedance profiles during an earlier phase of the reaction, leading to time resolved EIS measurements. Our results obtained by the FTEIS analysis are consistent with a series of electron transfer and chemical equilibrium steps of a complex reaction, making up an ECE (electrochemical-chemical-electrochemical) mechanism postulated from the results of computer simulation.

• Advances in environmental research
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• 제1권1호
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• pp.69-82
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• 2012

Based on the measurement data of the particulate matter with an aerodynamic diameter of less than or equal to a nominal 10 ${\mu}m$ (PM10) by the ${\beta}$-ray absorption method (BAM) equipped with an inlet heater and the gravimetric method (GMM) at two coastal sites in Korea, the optimal inlet heater temperature was estimated. By using a gas/particle equilibrium model, Simulating Composition of Atmospheric Particles at Equilibrium 2 (SCAPE2), water content in aerosols was estimated with varying temperature to find the optimal temperature increase to make the PM10 concentration by BAM comparable to that by GMM. It was estimated that the heated air temperature inside the BAM should be increased up to $35{\sim}45^{\circ}C$ at both sites. At this temperature range, evaporation of volatile aerosol components was minor. Similar ($30{\sim}50^{\circ}C$) temperature range was also obtained from the calculation based on the absolute humidity which changed with ambient absolute humidity and chemical composition of hygroscopic species.

• 한국환경과학회지
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• 제21권7호
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• pp.805-813
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• 2012

The removal property of Cu and Zn ions by chemical precipitation and adsorption using zeolite(Z-C1) prepared from coal fly ash(CFA) were evaluated in this study. Adsorption kinetic and equilibrium mechanisms described to analyze parameters and correlation factors with Lagergen $1^{st}$ and $2^{nd}$ order model and Langmuir and Freundlich model. Analysis of adsorption kinetics data revealed that the pseudo $2^{nd}$ order kinetics mechanism was predominant. The equilibrium data in pH 3 - 5 were able to be fitted well to a Langmuir model, by which the maximum adsorption capacities($q_{max}$) were determined at 124.9 - 140.1 mg $Cu^{2+}/g$ and 153.2 - 166.9 mg $Zn^{2+}/g$, respectively. We found that Z-C1 has a potential application as absorbents in metal ion recovery with low pH.

• 한국해양공학회지
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• 제17권6호
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• pp.77-82
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• 2003

The absorption of water into an anti-corrosive organic coating, such as alkyd and urethane resin coating, was investigated, using a quartz crystal microbalance (QCM). Anticorrosive properties of the coatings were also measured, by means of electrochemical impedance spectroscopy (EIS). The overall absorption of water in the coating is determined by the chemical nature of resin, and decreases with increasing thickness. The enhancement of anti-corrosive performance, through increase of coating thickness, was more remarkable in the case of the coating that hadlower equilibrium water absorption. The absorption kinetics curves were Fickian in nature. The EIS analysis confirmed that the resin, having lower equilibrium water absorption, shows higher anti-corrosive performan.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.424-428
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• 2007

In the current most tool using heat and mass balance in a coal gasifier is dependent on commercial code such as STANJAN, CHEMKIN. However, in order to keep the self-reliance technology, it is necessary to develop the original design tool available for comprehension and analysis on the spot. So in this study, its own heat and mass balance program is developed on the assumption that the process in a coal gasifier is adiabatic and quasi-equilibrium. The mass balance is calculated by using the chemical equilibrium principle. Also the heat and mass balance according to main operating factors such as temperature, pressure and O2/Coal ratio, was carried in this tool. This heat and mass balance was verified on the basis of the results simulated in STANJAN, commercial codes using similar logic.

• 대한금속재료학회지
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• 제46권4호
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• pp.227-232
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• 2008

Solvent extraction reaction of cobalt by Alamine336 from strong hydrochloric acid solution was identified by analyzing the solvent extraction data reported in the literature. Analysis of the data by graphical method revealed that Alamine336 took part in the solvent extraction reaction as a monomer in the concentration ranges, [Co(II)] : 0.0169 - 0.102 M, [Alamine336] ; 0.02- 1.75 M, and [HCl ] : 5 - 10 M. The following solvent extraction reaction and equilibrium constant was obtained from the experimental data by considering the activity coefficients of chemical species present in the aqueous phase. $Co^{2+}+2Cl^{-}+R_3NHCl_{org}=CoCl_3\;R_3NH_{org}$, $K_{ex}=2.21$ The distribution coefficients of cobalt predicted in this study agreed well with those reported in the literature.

• 대한환경공학회지
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• 제27권12호
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• pp.1270-1276
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• 2005

대기 중 PAHs의 가스/입자 분배반응이 평형상태일 때 가스/입자분배계수($logK_p$)와 각 화합물의 증기압($logP_L^O$)과 선형식의 기울기가 -1이라는 것이 지금까지 알려진 사실이었다. 기러나 실제 대기에서 일어나는 가스/입자 분배와 차이를 보이는 현상에 대한 연구가 진행되면서 대기 입자의 불균일성 및 입자특성의 차이로 평형상태일 때 가스/입자 분배계수와 증기압과 기울기가 -1이 되지 않을 수도 있다는 주장이 제기되었다. 따라서 본 연구에서 이러한 가설을 토대로 대기 입자의 입경 크기에 따라 시료를 채취하여 평형상태일 때 입경의 크기에 따른 가스/입자 분배를 연구하였다. 대기 중 PAHs의 분배평형상태를 추정하기 위해 High-volume air sampler에서 채취된 입자와 가스를 이용하여 분배계수와 증기압을 구하고 이때 기울기가 -1에 가까운 시료를 평형상태에 있는 시료로 간주하였다. 그러나 평형상태에 해당하는 시료 중 같은 날 동시에 채취한 입경별 입자를 이용하여 각 입경 크기에 따라 분배계수와 증기압의 기울기를 계산한 결과에서는 평형상태일지라도 입경크기에 따라 동일한 기울기를 갖지 않고 입자가 커질수록 기울기가 완만해지는 현상을 나타내었다. 이러한 현상을 규명하기 위해 가스/입자 분배 반응의 두 가지 기작에 대하여 평형상태일 때 기울기가 -1이라는 결과를 도출하기 위해 가정했던 조건에 대하여 검토하였다. 그 결과 가스/입자 분배가 흡착이 주 반응이라 가정했을 때 입자의 크기에 따라 탈착엔탈피 변화량에 차이가 있었으며, 흡수인 경우에는 입자간의 활성계수의 차이를 간접적으로 확인할 수 있었다. 이는 평형상태일 경우에도 입자의 크기에 따라 가스/입자 분배평형에 이르는 정도가 다른 것으로 판단된다. 또한 가스/입자 분배반응 현상을 규명하기 위해서는 입자의 크기를 고려함으로써 그 현상을 좀 더 명확히 밝힐 수 있을 것으로 판단된다.

• Journal of Korean Society for Atmospheric Environment
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• 제21권E3호
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• pp.75-85
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• 2005

A mathematical sensitivity analysis of the flow-through dynamic flux chamber technique, which has been utilized usually for various trace gas flux measurement from soil and water surface, was performed in an effort to provide physical and mathematical understandings of parameters essential for the NO flux calculation. The mass balance equation including chemical reactions was analytically solved for the soil NO flux under the steady state condition. The equilibrium concentration inside the chamber, $C_{eq}$, was found to be determined mainly by the balance between the soil flux and dilution of the gas concentration inside the chamber by introducing the ambient air. Surface deposition NO occurs inside the chamber when the $C_{eq}$ is greater than the ambient NO concentration ($C_{0}$) introducing to the chamber; NO emission from the soil occurs when the $C_{eq}$ is less than the ambient NO concentration. A sensitivity analysis of the significance of the chemical reactions of NO with the reactive species (i.e. $HO_{2},/CH_{3}O_{2},/O_{3}$) on the NO flux from soils was performed. The result of the analysis suggests that the NO flux calculated in the absence of chemical reactions and wall loss could be in error ranges from 40 to $85\%$ to the total flux.