• 한국추진공학회지
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• 제18권6호
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• pp.1-10
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• 2014

극초음속 흡입구를 직관적이며 체계적으로 설계할 수 있는 최적화된 방법을 제시한다. 마하 7의 이론식으로 계산된 극초음속 흡입구는 점성 조건의 전산수치해석을 수행하여 점성에 대한 오차를 보정한다. 전산수치해석을 통한 성능 비교에서 1단 쐐기에 비해 2단 쐐기를 가지는 흡입구 형상이 성능비교에서 좋은 결과를 보였다. 또한 비설계 조건에서 극초음속 흡입구의 성능은 설계 마하수 성능에 비해 손실이 크지 않았다.

• 상하수도학회지
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• 제22권2호
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• pp.187-193
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• 2008

Biological removal capacities for volatile organic compounds (VOCs) were determined using a yeast strain, Candida tropicalis. In this study, VOCs including toluene, benzene, p-xylene, and styrene as single substrates or mixtures were tested in the batch culture of the yeast strain. In addition, a kinetic model was applied to evaluate substrate interactions between the VOCs. The yeast strain was able to biodegrade each VOC effectively as a growth substrate, implying it could applied to wide range of VOCs. When the yeast strain was subjected to VOCs in mixtures, the biodegradation rate of one substrate were either increased (stimulated) or decreased (inhibited) by the presence of the others. Both benzene and toluene were inhibited by the other VOCs, and substrate interaction parameters estimated in the model indicated that styrene was the strongest inhibitor for the benzene and toluene biodegradation. Meanwhile, the biodegradation of p-xylene and styrene was stimulated by the presence of either benzene or toluene. The biodegradation rate of p-xylene was significantly increased especially by the presence of toluene, and the styrene biodegradation was enhanced greatly by the benzene addition. The results of the substrate interaction by the yeast strain suggest that the biodegradation rates for the VOCs in mixtures should be carefully evaluated. Furthermore, the competitive inhibition coefficient could be applied as a useful index to determine the substrate interaction

• Journal of Microbiology and Biotechnology
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• 제21권12호
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• pp.1257-1263
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• 2011

This paper is dedicated to the study on the external and internal mass transfers of glucose for succinic acid fermentation under substrate and product inhibitions using a bioreactor with stirred bed of immobilized Actinobacillus succinogenes cells. By means of the substrate mass balance for a single particle of biocatalysts, considering the kinetic model adapted for both inhibitory effects, specific mathematical models were developed for describing the profiles of the substrate concentration in the outer and inner regions of biocatalysts and for estimating the substrate mass flows in the liquid boundary layer surrounding the particle and inside the particle. The values of the mass flows were significantly influenced by the internal diffusion velocity and rate of the biochemical reaction of substrate consumption. These cumulated influences led to the appearance of a biological inactive region near the particle center, its magnitude varying from 0 to 5.3% of the overall volume of particles.

• 한국환경과학회지
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• 제27권11호
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• pp.975-982
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• 2018

In this study, zeolite (Z-C1) was synthesized using a fusion/hydrothermal method from coal fly ash. The morphological structures of Z-C1 were confirmed to be highly crystalline with a cubic crystal structure. Exchange capacities of $Ca^{2+}$ and $Mg^{2+}$ ions in a single and a mixed solution reached equilibrium within 120 min. The exchange kinetics of these ions were well predicted by the pseudo-second-order rate equation. The exchange isotherms of the $Ca^{2+}$ and $Mg^{2+}$ ions matched the Langmuir isotherm better than the Freundlich isotherm. The maximum cation exchange capacities ($q_m$) obtained by the Langmuir isotherm model were 2.11 mmol/g (84.52 mg/L) and 1.13 mmol/g (27.39 mg/L) for the $Ca^{2+}$ and $Mg^{2+}$ ions, respectively.

• Korean Chemical Engineering Research
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• 제61권2호
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• pp.273-277
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• 2023

The biosorption of methylene blue (MB) from aqueous solution was investigated using dried Rhodotorula glutinis as the biosorbent. The effects of pH, initial dye concentration, biosorbent dosage, and kinetic studies were determined to obtain valuable information for biosorption. Results indicated that most of the adsorbed MB bound within 30 minutes of contact and the MB adsorption capacity increased from 21.1 to 101.8 mg/g with the initial MB concentration increased from 50 to 300 mg/L. Additionally, the MB adsorption capacity gradually increased from pH 4.0 to 9.0, reaching its peak at an initial pH of 9.0. As the biomass load was increased from 0.25 to 4.0 g/L, the MB removal efficiency increased from 14.1 to 84.5%. The Langmuir model provided the best fit throughout the concentration range, and the maximum adsorption capacity (q_max) and Langmuir constant (b) were determined to be 135.14 mg/g and 0.026 l/mg, respectively. Furthermore, the biosorbent process of R. glutinis was found to follow pseudo-second-order kinetics and the calculated q_eq,cal value showed good agreement with the experimental q_eq value. Overall, the biosorption of MB by R. glutinis can be characterized as a monolayer, single site type phenomenon, and the rate-limiting step was determined to be the chemical reaction between the adsorbent and the adsorbate.

• 제어로봇시스템학회:학술대회논문집
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• 제어로봇시스템학회 1991년도 한국자동제어학술회의논문집(국제학술편); KOEX, Seoul; 22-24 Oct. 1991
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• pp.1639-1645
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• 1991

Because of the important role LD converters play in the production of high quality steel, various dynamic models have been attempted in the past by many researchers not only to understand the complex chemical reactions that take place in the converter process but also to assist the converter operation itself using computers. And yet no single dynamic model was found to be completely satisfactory because of the complexity involved with the process. The process indeed involves dynamic energy and mass balances at high temperatures accompanied by complex chemical reactions and transport phenomena in the molten state. In the present study, a mathematical model describing the dynamic behavior of LD converter process has been developed. The dynamic model describes the time behavior of the temperature and the concentrations of chemical species in the hot metal bath and slag. The analysis was greatly facilitated by dividing the entire process into three zones according to the physical boundaries and reaction mechanisms. These three zones were hot metal (zone 1), slag (zone 2) and emulsion (zone 3) zones. The removal rate of Si, C, Mn and P and the rate of Fe oxidation in the hot metal bath, and the change of composition in the slag were obtained as functions of time, operating conditions and kinetic parameters. The temperature behavior in the metal bath and the slag was also obtained by considering the heat transfer between the mixing and the slag zones and the heat generated from chemical reactions involving oxygen blowing. To identify the unknown parameters in the equations and simulate the dynamic model, Hooke and Jeeves parttern search and Runge-Kutta integration algorithm were used. By testing and fitting the model with the data obtained from the operation of POSCO #2 steelmaking plant, the dynamic model was able to predict the characteristics of the main components in the LD converter. It was possible to predict the optimum CO gas recovery by computer simulation

• 대한수의학회지
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• 제35권4호
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• pp.815-822
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• 1995

The toxicokinetics of rifapentine was studied after an oral administration to beagle dogs. High-performance liquid chromatography(HPLC) using column-switching technique was performed to determine the serum concentrations of rifapentine. The pharmacokinetic profiles of rifapentine were analysed using one-compartment open model. Following a single oral administration of 10mg/kg, pharmacokinetic parameters were determined as follows: maximum serum concentration($C_{max}$), $28.90{\mu}g/ml$; maximum concentration time($T_{max}$), 3.7hr; elimination half-life($t_{1/2}$, 4.7hr; area under the curve(AUC), $339.0{\mu}g{\cdot}hr/ml$; volume of disiribution/bioavailability (Vd/F), 0.21 l/kg; lag time, 24min; absorption rate constant($k_a$), $0.445hr^{-1}$; elimination rate constant($k_{el}$), $0.148hr^{-1}$. After 6 month multiple oral doses of 10mg/kg/day, parameters were as follows: $C_{max}$, $34.40{\mu}g/ml$; $T_{max}$, 2.6hr; $t_{1/2}$, 6.7hr; AUC, $391.3{\mu}g{\cdot}hr/ml$; Vd/F, 0.291/kg; $k_a$, $0.976hr^{-1}$; $k_{el}$, $0.104hr^{-1}$. The consistant kinetic parameters after a single and multiple oral administration show that there was no accumulation of rifapentine after 6 month oral administration. We also simulated the concentration of rifapentine after oral multiple administration of 10 and 50mg/kg/ day, based on the parameters obtained form the single administration. The measured serum concentrations of rifapentine were well fitted to the simulated results. The simulated results show that rifapentine readily reaches to steady-state after about 3 doses and the steady-state serum concentrations($C_{ss}$) are fluctuated in between $2.2{\sim}25.2{\mu}g/ml$, and $10.6{\sim}125.2{\mu}g/ml$ at the doses of 10 and 50mg/kg/day, respectively.

• 한국미생물·생명공학회지
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• 제13권4호
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• pp.397-402
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• 1985

C. thermosaccharolyticum을 이용하여 xylose, glucose, cellobiose등을 각각 단일기질 및 혼합기질로 배양한 결과는 다음과 같다. 기질의 종류에 관계없이 에탄올의 생산양상은 Leudeking-Piret모델에 따랐으며 q$_{p}$=$\alpha$ $\mu$＋$\beta$의 식으로 나타낼 수 있었다. 단일당에서의 배양결과 glucose, xylose, cellobiose 각 당에서의 비증식속도는 0.363 h$^{-1}$, 0.242 h$^{-1}$, 0.144 h$^{-1}$로 균의 증식은 glucose를 기질로 사용하였을 때가 가장 좋았다. 에탄올 생산성은 xylose에서 가장 좋았으며, 각 당에서의 에탄올수율은 0.38g ethanol/g xylose, 0.34 g ethanol/g cellobiose, 0.242g ethano1/g glucose 이었다. glucose에서의 배양결과, 배양 12시간이후 균의 자기소화현상이 현저히 일어났으며, 다른 당에서와는 달리 에탄올 생산양상은 $\alpha$값이 음수를 나타내므로써, 균의 생육이 증가하면 오히려 에탄을 비생산속도는 감소하는 경향을 보였다. 서로 다른 당을 혼합하여 기질로 사용할 경우, 각 당의 이용특성은 이들을 단독기질로 배양하였을 때의 소비양상과 유사하여 각 당은 서로 영향을 미치지 않고, 독립적으로 자화되는 것으로 생각된다. 혼합당에서의 기질소비는 glucose, xylose, cellobiose순으로 소비되었으며, 또한 에탄을 생산성은 glucose가 첨가된 경우 glucose 농도가 낮고(5g/l), glucose를 기질로 하여 균이 왕성하게 증식한 상태에서 xylose나 cellobiose를 이용하므로써 glucose만을 단독기질로 배양한 결과보다 좋았다.

• 대한기계학회논문집B
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• 제38권6호
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• pp.451-464
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• 2014

본 연구에서는 HCCI엔진의 과급조건에서 EGR의 영향에 대하여 수치해석적인 방법으로 연구하였다. 수치해석은 CHEMKIN-PRO에 있는 single-zone model을 사용하였고 연료로는 N-heptnae, Iso-octane 그리고 PRF50을 사용하였다. 사용된 연료의 화학반응 매커니즘과 열역학적 변수들은 Lawrence Livermore National Laboratory(LLNL)의 모델을 사용하였다. 연소상의 변화는 열효율에 큰 영향을 미치게 되므로 이영향을 배제하기 위해 본 연구에서는 CA50을 $365^{\circ}CA$($5^{\circ}CA$ aTDC)로 일정하게 고정하였다. 연구결과 EGR의 영향으로 줄어든 산소의 영향에 의해 저온산화반응과 NTC, 고온산화반응이 모두 약화되고 열발생률이 감소하는 것을 확인할 수 있었다. 과급과 EGR을 함께 사용하게 되면 과급에 의해 증가한 산소량과 연료의 영향으로 인해 연소가 강화되어 저온산화반응, NTC, 고온산화반응이 강화되고 열 발생률이 증가하는 것을 확인할 수 있었다. EGR만을 사용하는 경우 IMEP가 감소하는 경향을 나타내지만 과급과 EGR을 함께 사용하는 경우 과급의 영향으로 인해 IMEP가 크게 증가하여 낮은 압력상승률과 높은 출력을 함께 얻을 수 있는 것을 확인하였다.