• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1994.05a
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• pp.15-21
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• 1994

단계적 연료방식을 가지는 가스터빈 연소기의 해석을 위한 방법을 제안하였으며, 이를 바탕으로 연료배분방식에 따른 연소기의 연소 및 NOx 발생특성을 규명하였다. 연소기 해석모델은 연소기 내부를 선회기구역, 1차연소구역, 재순환구역, 2차연소구역 및 희석구역으로 나누어 각각의 반응구역을 혼합반응기, 플러그 유동반응기의 모델로서 근사하였다. 반응기내의 연소 및 NOx 생성반응은 천연가스 반응모델과 Zel'dovich 의 NOx 모델을 이용하여 예측하였다. 본 해석방법을 이용하여, 각 반응구역에 유입되는 연료량이 연소기내 연소특성, NOx 발생 특성 및 온도분포에 미치는 영향을 검토하였다. 또한, NOx 저감을 위해 증기분사를 사용하는 경우에 분사위치가 NOx 발생에 미치는 영향을 분석하여, 가스터빈 연소기설계에 필요한 기초자료를 제공하였다.

• Polymer(Korea)
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• v.25 no.1
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• pp.25-32
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• 2001

The kinetics of ester interchange reaction of dimethyl naphthalate(DMN) with ethylene glycol(EG) has been studied in the range of 180-200 $^{\circ}C$ using zinc and manganese catalysts. The reaction was performed in a semibatch reactor under nonisothermal condition and the degree of reaction was calculated from experimental data of methanol removal rate and reaction temperature. As a reaction model, both the functional group model and the molecular species model were applied and analysed. In case of zinc catalyst, the ratio of reaction rate of methyl hydroxyethyl naphthalate(MHEN) with EG on that of DMN with EG is about 1.4, whereas in case of manganese catalyst the ratio is about 4.3, which implies that the reaction rate is quite dependent on the type of catalyst. In case of zinc catalyst, the reaction order of catalyst concentration on either DMN or MHEN and EG is less than 1, whereas in case of manganese catalyst, the reaction order is larger than 1. The activation energy for zinc and manganese catalyst, irrespective of the type of molecular species, e.g., DMN and MHEN, were found to be 25000 and 28750 cal/mol, respectively. As a result of comparing two reaction model, the molecular species model fits well for the experimental data.

• The Journal of the Korea institute of electronic communication sciences
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• v.13 no.3
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• pp.579-586
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• 2018

With the beginning of the new era of bigdata, information extraction or prediction are an important research area. Here, we present the acquisition of semi-automatically curated large-scale biological database and the prediction of enzyme reaction annotation for analyzing the pharmacological activities of drugs. Because the xenobiotic metabolism of pharmaceutical drugs by cellular enzymes is an important aspect of pharmacology and medicine. In this study, we apply and analyze similarity models to predict bimolecular reactions between human enzymes and their corresponding substrates. Thirteen models select to reflect the characteristics of each cluster in the similarity model. These models compare based on sensitivity and AUC. Among the evaluation models, the Simpson coefficient model showed the best performance in predicting the reactivity between the enzymes. The whole similarity model implement as a web service. The proposed model can respond dynamically to the addition of reaction information, which will contribute to the shortening of new drug development time and cost reduction.

• Journal of Internet Computing and Services
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• v.13 no.1
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• pp.99-106
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• 2012

It is an important and a difficult task to analyze external inputs and interactions between objects for designing and modeling a reactive system consisting of multiple object. Also the reactive system is required huge efforts on confirm it can satisfy requirements under all possible circumstances. In this paper, we build from requirements to a scenario-based specification model using LSC(Live Sequence Chart) extending MSC(Message Sequence Chart) with richer syntax and semantic. Then the reactive system model satisfying all requirements for each object in this system can be automatically created through LTL Synthesis. Finally, we propose a method of reactive system development by iterative process transforming a reactive system model to codes.

• Korean Chemical Engineering Research
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• v.46 no.2
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• pp.301-309
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• 2008

In this study, the effect of formaldehyde to phenol (F/P) molar ratios, catalyst wt%, and reaction temperature on the chemical structure was studied utilizing a two-level full factorial experimental design. The effect of three variables on the chemical structure was analyzed by using three-way ANOVA of SPSS. Concentration of methyrol-substituted phenols after 300 min addition reaction increased with higher the F/P mole ratio, lower the reaction temperature and lower the catalyst wt%. Resol catalysed by barium hydroxide showed higher addition of formaldehyde onto ortho positions of phenolic rings. A simplified elementary reaction model for resole type phenolic resin formation which do not consider the dissociation of phenolic compounds and the fraction of formaldehyde in the form of methylene glycol was proposed and compared with Zavitsas' type models. Elementary reaction model showed error of 2.79% compared to the error of 3.27% in Zavitsas' type models. It was thought that the elementary reaction model could be used to predict the behavior of addition reaction in resol formation.

• Polymer(Korea)
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• v.26 no.4
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• pp.422-430
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• 2002

The kinetics of polycondensation of bishydroxyethyl naphthalate has been studied in the range of 241 -$260^{\circ}C$ using antimony trioxide catalyst. The reaction was performed in a batch reactor and the concentration of reaction mixture was measured with HPLC. The activation energy values of forward and reverse reaction determined from molecular species model were found to be 19.7 and 31.4 kcal/mole, respectively, and the equilibrium constants were in the range of 1.4-2.0, which were larger than that of polycondensation of PET and varied to some degree with temperature. It was confirmed by applying the Flory's distribution function that the reaction rate of the hyroxyethyl group does not depend on the molecular size. By applying functional group model, we observed that there was few difference between the activation energy of the forward reaction and that of reverse reaction, therefore the equilibrium constant has almost constant value of 1.4. The rate constants obtained from functional group model was about 3-4 times larger than that from molecular species model, which showed that both model explains the reaction system well. Although the molecular species model should predict the concentration of as many as ten molecules, it fits for the experimental results well.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.02a
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• pp.363-363
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• 2011

열분해 반응기 내에서 실리콘 필름을 성장시키는 것은 반도체/디스플레이, 태양전지, 신소재 등 다양한 분야에서 중요한 공정이다. 더욱이 반도체 소자 선폭이 줄어들면서 나노입자의 오염 제어가 더불어 중요해지고 있다. 생산 공정 기술의 집적화에 따라 패턴 사이 거리가 작아지고, 이에 불과 수 십 나노미터크기의 오염입자에 의해서 패턴불량이 발생하고 생산수율을 감소시킨다. 일반적으로 반도체 공정 중 발생한 오염입자는 반응기 내의 가스가 물리/화학적 공정에 의해 핵생성(nucleation)이 일어나 핵(nuclei)이 생성되고, 이 때 표면반응 및 응집(coagulation)에 의해 성장하게 된다. 이에 본 연구에서는 열분해 반응기 내에서 사일렌(SiH4) 가스를 열분해하여 발생되는 실리콘 오염입자의 핵생성과 성장 모델을 정립하고, 생성된 오염입자의 거동과 전달 현상을 이론적으로 고찰하였다. 열분해 반응기와 같은 기상공정(Gas to particle conversion)에서 오염입자가 생성될 때, 그 성질과 크기 등에 물리/화학적 영향을 주는 요소는 전구체/이송기체의 농도 및 유량, 작동 압력, 작동 온도와 반응기 고유 특성 등이 있다. 수치해석의 정당성과 빠른 계산을 위해 단순화시킨 0D 모델인 Batch 반응기와 1D모델인 plug flow 반응기 등에서 SiH4 가스의 열분해 과정시 생성되는 Si cluster를 상용코드인 CHEMKIN 4.1.1을 이용하여 계산하였으며, 2D모델인 Shear flow 반응기로 확장시켜 Si 오염입자가 생성특성을 연구하였다.

• Polymer(Korea)
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• v.28 no.2
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• pp.121-127
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• 2004

The instantaneous removal of ethylene glycol is very important fur obtaining high molecular weight polymer because of the reversibility of the polycondensation reaction of poly(ethylene naphthalate)(PEN). In this study, we investigated the mass transfer phenomena in the thin film of PEN oligomer where the polycondensation reaction took place at 280$^{\circ}C$ and under 0.1mmHg. In case of less than 0.025cm film thickness the mass transfer resistance through the thin film of the polymer melt was not so high that the overall reaction rate was governed only by the polycondenstion reaction. Both the mass transfer model and the diffusion model predicted the experimenatal data well but the diffusion model showed faster reaction rate in the low molecular weight range than the mass transfer model . It was estimated from the two models that the diffusivity was 4.7${\times}$10$\^$-6/$\textrm{cm}^2$/sec and the mass transfer coefficient was 1.4 ${\times}$10$\^$-4/cm/sec both of which were smaller than In case of poly(ethylene terephthalate).

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2005.11a
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• pp.450-454
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• 2005

A numerical analysis is performed to analyze the reacting flow-field of an axisymetric coaxial ramjet combustor. Two dimensional Navier-Stokes equation with low Reynolds number $k-\varepsilon$ turbulence model is utilized and finite-rate chemistry model is adopted. Eddy dissipation model is applied for a modeling of turbulent combustion. Two different types of combustors (combustor with a suddenly expanded dump and combustor with wedge-shaped flame holders) are compared in a view point of flame stabilizing.

• Journal of Food Hygiene and Safety
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• v.19 no.1
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• pp.19-24
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• 2004

Dose-response models in microbial risk assessment can be divided into biologically plausible models and empirical models. Biologically plausible models are formed by the assumptions in dose distribution of microbes, host sensitivity to microbes, and minimal infectious dose of microbes : there are Exponential model and $\beta$-Poisson model, representatively. Empirical models are mainly used to express the toxicity of chemicals : there are Weibull-Gamma model etc. Deviance function (Y) is used to fit available data to dose-response models, and some dose-response models for food-borne pathogens are developed in humans and experimental animals.