• 한국연소학회:학술대회논문집
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• 한국연소학회 2002년도 제25회 KOSCI SYMPOSIUM 논문집
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• pp.173-184
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• 2002

In order to evaluate the devolatilization models of pulverized coal, various devolatilization models are examined for the numerical analysis of Drop Tube Furnace.The results of analysis are compared with the experimental results. A numerical study was conducted to explore the sensitivities of the predictions to variation of the model parameters. It helps to elucidate the source of the discrepancies. Three different wall temperature conditions of the DTF, 1100, 1300 and $1500^{\circ}C$ were considered in this analysis. Two fuels are U.S.A. Alaska coal and Australia Drayton coal. The results of analysis with constant rate model, single kinetic rate model and two competing rate modes well presented fast volatile matter release in the early devolatilization. However, in the latter devolatilization they did not coincide with experimental results which presented tardy volatile matter release on account of pyrolysis of high molecular substance. On the other hand, the results of analysis with DAEM(Distribute Activation Energy Model) coincided with experiment al results in overall devolatilization.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2012년도 제45회 KOSCO SYMPOSIUM 초록집
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• pp.67-70
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• 2012

Many computational fluid dynamic (CFD) simulations have treated the coal kinetics poorly due to large physical domain sizes and high computational complexity, particularly for the recent oxy-coal boilers. Furthermore, some modelers' lack of understanding of the kinetic rate model seems to worsen the simulation accuracy. This study is to suggest the importance of proper use of single-film global kinetic model generally used in CFD code to describe the oxy-fuel combustion of coal char through simple char burnout calculation.

• Biotechnology and Bioprocess Engineering:BBE
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• 제11권1호
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• pp.61-66
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• 2006

The simple Langmuir isotherm is frequently employed to describe the equilibrium behavior of protein adsorption on a wide variety of adsorbents. The two adjustable parameters of the Langmuir isotherm - the saturation capacity, or $q_m$, and the dissociation constant, $K_d$ - are usually estimated by fitting the isotherm equation to the equilibrium data acquired from batch equilibration experiments. In this study, we have evaluated the possibility of estimating $q_m$ and $K_d$ for the adsorption of bovine serum albumin to a cation exchanger using batch kinetic data. A rate model predicated on the kinetic form of the Langmuir isotherm, with three adjustable parameters ($q_m,\;K_d$, and a rate constant), was fitted to a single kinetic profile. The value of $q_m$ determined as the result of this approach was quantitatively consistent with the $q_m$ value derived from the traditional batch equilibrium data. However, the $K_d$ value could not be retrieved from the kinetic profile, as the model fit proved insensitive to this parameter. Sensitivity analysis provided significant insight into the identifiability of the three model parameters.

• 상하수도학회지
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• 제33권3호
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• pp.205-213
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• 2019

Batch adsorption tests were performed to evaluate the applicability of adsorption kinetic model by using hydrogel chitosan bead crosslinked with glutaraldehyde (HCB-G) for Cu(II) as cation and/or phosphate as anion. Pseudo first and second order model were applied to determine the sorption kinetic property and intraparticle and Boyd equation were used to predict the diffusion of Cu(II) and phosphate at pore and boundary-layer, respectively. According to the value of theoretical and experimental uptake of Cu(II) and phosphate, pseudo second order is more suitable. On comparison with the value of adsorption rate constant (k), phosphate kinetic was 2-4 times faster than that of Cu(II) at any experimental condition indicating the electrostatic interaction between ${NH_3}^+$ and phosphate is dominated at the presence of single component. However, when Cu(II) and phosphate simultaneously exist, the value of k for phosphate was sharply decreased and then the difference was not significant. Both diffusion models confirmed that the sorption rate was controlled by film mass transfer at the beginning time (t < 3 hr) and pore diffusion at next time section (t > 6 hr).

• 생명과학회지
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• 제14권1호
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• pp.131-140
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• 2004

T7박테리오파지 gp4는 dTTP 가수분해에너지를 이용하여 DNA복제시 이중 나선 DNA를 단일가닥 DNA로 풀어내는 나선효소(helicase)이다. T7 나선효소의 활성형의 4차구조는 한가운데 구멍을 지닌 육량체 고리모양이다. 단일가닥 DNA는 나선효소가 $5'\rightarrow3'$방향으로 이동할 때 육량체 고리의 구멍으로 빠져나간다. 이러한 DNA의 이중나선 풀어헤침을 빠른 효소반응속도 측정법을 이용하여 정량적으로 측정하였으며, 그 결과 단일가닥 DNA 산물들이 생성되기 전에 지연상태(lag phase)가 존재함을 관찰하였다. 이러한 지연상태를 나선효소에 의한 이중나선 DNA의 풀어헤침이 속도론적 단계과정(kinetic stepping)을 거친다는 모델로써 분석하였다. 예상대로 이중나선의 길이가 클수록 지연상태의 지속시간이 늘어났다. $\tau7$ 나선효소가 이중나선 DNA를 풀어내는 과정에서 넣어준 trap DNA는 풀어내는 이중나선 DNA의 양을 변화시키지 못하여서, $\tau7$ 나선효소가 매우 큰 공정성을 지닌 효소임을 알 수 있었다. 이러한 속도론적 data를 global fitting법을 써서 kinetic stepping 모델에 적용한 결과 매 단계(step)마다 10∼l개의 염기쌍이 풀려지고 1초당 3.7번의 step이 일어난다는 것을 알 수 있었다. DNA 풀어헤침과 dTTP가수분해의 메커니즘과 이들의 연계성은 $4∼37^{\circ}C$사이의 온도범위에서 영향을 받지 않았다. 이상을 종합할 때, T7나선효소의 이중나선 DNA의 풀어헤침 시 나타나는 속도론적 단계과정은 DNA복제 시 이용되는 나선효소의 내재적 속성임을 알 수 있다.

• 환경위생공학
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• 제16권1호
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• pp.66-71
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• 2001

The objective of this study was to depict the kinetic behavior of the platinum catalyst for the deep oxidation of aromatic solvents and their binary mixtures. The oxidation kinetics of aromatic solvents, which were benzene, toluene and m-xylene, was studied on a 0.5% $Pt/{\gamma}-Al_2O_3$ catalyst. Deep oxidation of binary mixtures, which were 1:1 in volume, was carried out and the inlet concentration was controlled in the range of 133 and 333ppmv. An approach based on the two-stage redox model was used to analysis the results. The deep oxidation conversion of aromatic solvents was inversely proportional to inlet concentration in plug flow reactor. This trend is due to the zeroth-order kinetics with respect to inlet concentration. The kinetic parameters of multicomponent model were independently evaluated from the single compound oxidation experiments. A simple multicomponent model based on two-stage redox rate model made reasonably good predictions of conversion over the range of parameters studied.

• 공업화학
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• 제17권3호
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• pp.296-302
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• 2006

산소농도에 따른 폐폴리우레탄의 열적 산화분해에 관한 속도론적 연구를 $10{\sim}50^{\circ}C/min$ 사이의 여러 가열속도에서 비등온 질량감소 기술을 이용하여 수행하였다. 폐폴리우레탄의 열적 산화분해를 묘사하기 위하여 Arrhenius식에 근거한 미분법과 적분법을 이용하여 산소농도에 대한 영향을 고려할 수 있는 속도론 모델을 제시하였으며 활성화 에너지 및 반응차수 그리고 pre-exponential 인자와 같은 속도 상수들에 대한 정보를 얻기 위하여 본 연구에서 제시한 속도론 해석 방법을 이용하여 질량감소 곡선 및 그 미분값을 해석하였다. 본 연구로부터 산소농도에 대한 반응차수는 모두 음의 값을 나타내었으며 활성화 에너지는 산소농도가 증가함에 따라 감소함을 확인할 수 있었다. 또한 단일 가열속도에서의 실험값을 이용하는 적분법의 경우 가열속도에 따라 반응속도 상수의 값이 변화함을 알 수 있었다. 따라서 여러 가열속도에서의 실험값을 이용하는 미분법이 폐폴리우레탄의 열적 산화분해 반응을 보다 효율적으로 나타내고 있는 것으로 판단된다.

• 대한화학회지
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• 제55권3호
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• pp.341-345
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• 2011

Schiff base 코발트(II) 착물, bis[4-chloro-2-((E)-(isopropylimino) methyl) phenol]cobalt(II), 을 합성하고 단결정 X-ray 회절 분석을 하였다. 코발트 (ii) 합성물의 현상학적, 속도론적 및 기계적 특성은 TG/DTG법으로 연구하였다. 실험 데이터에 기초하여, 활성화 에너지, 지수 앞자리인자, 활성화 엔트로피와 같은 속도론적 파라미터를 계산하였으며, 가장 가능성 있는 메카니즘 함수로는 $g({\alpha})={\alpha}^2$이 추정되었다. 따라서, 모든 분해 단계에서 속도 조절 단계는 1차원 확산 과정(Parabolic model) 이다.

• 한국수소및신에너지학회논문집
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• 제33권1호
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• pp.77-84
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• 2022

The experimental work has been carried out for the study of pyrolysis of oil samples used in industrial and utility boilers in Korea. For five oil samples, the characteristics of pyrolysis have been investigated with a thermogravimetric analyzer (TGA), and their kinetic parameters were obtained and compared each other. The rate order of pyrolysis rate for five oils were as follows: by-product fuel oil, pyrolysis oil, diesel, a heavy oil and refined oil. The pyrolysis of refined oil has been successfully described by the three step, first order reaction model while the single step reaction model has been used for other oils. For the reaction temperature over 550 K, the reactivity of refined oil was very poor compared with other oils.

• Food Science and Biotechnology
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• 제15권5호
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• pp.664-671
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• 2006

Modeling the growth kinetics of lactic acid bacteria (LAB), one of the most valuable microbial groups in the food industry, has been actively pursued in order to understand, control, and optimize the relevant fermentation processes. Most modeling approaches have focused on the development of single population models. Primary single population models provide fundamental kinetic information on the proliferation of a primary LAB species, the effects of biological factors on cell inhibition, and the metabolic reactions associated with cell growth. Secondary single population models can evaluate the dependence of primary model parameters, such as the maximum specific growth rate of LAB, on the initial external environmental conditions. This review elucidates some of the most important single population models that are conveniently applicable to the LAB fermentation analyses. Also, a well-defined mixed population model is presented as a valuable tool for assessing potential microbial interactions during fermentation with multiple LAB species.