• 한국미생물·생명공학회지
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• 제37권4호
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• pp.365-370
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• 2009

재구성 지방질의 기질로서 사용될 수 있는 중쇄지방산을 함유한 디글리세리드(DG)를 생산하기 위하여 리파제를 사용하여 중쇄지방산과 모노글리세리드(MG)로부터 DG를 생산하는 유기용매를 사용하지 않는 반응 시스템을 고안하였다. 조사된 리파제 중에 Lipozyme RM IM과 Novozym 435만이 중쇄지방산(carpylic acid, caproic acid, capric acid)과 MG로부터 DG를 효과적으로 생산하였다. 고정화 효소인 Lipozyme RM IM을 사용하여 중쇄지방산인 카프릴산과 MG를 반응시킴으로써 DG 생산을 위하여 molecular sieve 첨가에 의한 반응혼합액 중의 수분 제거, 고정화 효소의 수분함량, 반응온도, MG/카프릴산의 몰비율 등의 생산 조건을 최적화하였다. Molecular sieve를 첨가 하였을 때 약 8%의 DG 함량이 증가되었으며 고정화효소(초기 수분함량: 3.8%(w/w))의 수분을 2.8%(w/w) 이상 감소시킴으로써 44%의 DG를 생산할 수 있었다. 최적의 반응 온도는 $60^{\circ}C$로 확인되었으며 $60^{\circ}C$에서 $25^{\circ}C$로의 온도 변화는 FFA의 함량이 증가하여 DG 생산에 적합하지 아니하였다. 조사된 모든 몰비율에서 반응 24시간 후의 DG의 생산량은 40% 전후로 큰 차이를 나타내지 않았으나 화학양론적인 몰비율 1:1(MG/caprylic acid)에서 가장 많은 DG가 생산되었다. 또한 MG와 카프릴산의 몰비율이 0.3에서 1.8로 높아질수록 반응물 중의 FFA의 함량이 34%에서 13%로 감소하였고 MG 함량은 37%에서 50%로 증가하였다.

• 한국항공우주학회지
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• 제44권4호
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• pp.333-342
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• 2016

액체로켓 추진시스템은 액체 추진제와 액체 산화제의 화학반응을 통해 추력을 발생하는 방식으로써 우주발사체 및 인공위성을 포함한 우주비행체에 광범위하게 적용되고 있다. 일반적으로 사용되는 액체로켓 추진제로는 모노메틸하이드라진/사산화이질소, 액체수소/액체산소 및 RP-1/액체산소 조합 등이 있다. 본 연구의 목적은 액체로켓 추진제의 열화학적 반응을 수치적으로 분석함으로써, 이를 통해 궁극적으로 액체로켓엔진의 설계와 성능에 필요한 유용한 정보를 예측하고자 하는 데 있다. 이를 위해 앞서 언급한 3가지 조합의 연료와 산화제에 대하여 연소반응 후 화학평형상태에 도달했을 때 주요 요소평형반응들의 평형상수 값들을 이용해 최종 생성물의 성분과 화학조성을 계산하였고 그 결과를 이용해 단열화염온도와 로켓성능변수인 비추력을 예측하는 연구를 진행하였다.

• Nuclear Engineering and Technology
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• 제52권2호
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• pp.279-286
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• 2020

In this article, we develop a reactive distillation (RD) column configuration for the production of hydrogen. This RD column is in the HI decomposition section of the sulphur - iodine (SI) thermochemical cycle, in which HI decomposition and H₂ separation take place simultaneously. The section plays a major role in high hydrogen production efficiency (that depends on reaction conversion and separation efficiency) of the SI cycle. In the column simulation, the rigorous thermodynamic phase equilibrium and reaction kinetic model are used. The tuning parameters involved in phase equilibrium model are dependent on interactive components and system temperature. For kinetic model, parameter values are adopted from the Aspen flowsheet simulator. Interestingly, there is no side reaction (e.g., solvation reaction, electrolyte decomposition and polyiodide formation) considered aiming to make the proposed model simple that leads to a challenging prediction. The process parameters are determined on the basis of optimal hydrogen production as reflux ratio = 0.87, total number of stages = 19 and feeding point at 8th stage. With this, the column operates at a reasonably low pressure (i.e., 8 bar) and produces hydrogen in the distillate with a desired composition (H₂ = 9.18 mol%, H₂O = 88.27 mol% and HI = 2.54 mol%). Finally, the results are compared with other model simulations. It is observed that the proposed scheme leads to consume a reasonably low energy requirement of 327 MJ/kmol of H₂.

• 한국물환경학회지
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• 제26권6호
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• pp.919-925
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• 2010

The features of precipitating reaction of fluoride have been examined by employing waste gypsum as a precipitant. The major component of waste gypsum was examined to be CaO with minor components of $SO_3$, $SiO_2$. In the experimental condition, the precipitating reaction of fluoride progressed rapidly within a few minutes after the reaction started and reached its equilibrium in 10 minutes. Kinetic analysis showed that the precipitating reaction of fluoride generally followed a first Oder and second Oder with decreasing rate constant with the initial dosage of precipitant. XRD analysis showed that the crystalline structure of precipitate was mainly $CaF_2$ with partly $Ca_5(PO_4)_3(OH)$.

• 한국산업융합학회 논문집
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• 제3권1호
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• pp.77-82
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• 2000

The stereoselective ligand exchange reaction of trans-$[Co(SS-epm)Cl_2]^+$ and racemic propane-1,2-diamine (rac-pn) produces the complex that is identified as $[CO(N)_6]^{3+}$ type of $[Co(SS-epm)(pn)]^{3+}$ by absorption spectrum. It is conceivable that the reaction mechanism involves substitution and isomerization. The calculated and experimentally determined ratios of the complexed enantiomeric substrates at equilibrium were as follows: $[Co(SS-epm)(pn)]^{3+}$,calcd 32 % / 68 %, exptl 19 % / 81 % R-pn / S-pn. It has been shown that the employment of molecular mechanics calculations as a predictive tool may lead to the design of chiral complexes that may be applied to the separation of racemic mixtures of simple bidentate ligands.

• 한국수소및신에너지학회논문집
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• 제18권3호
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• pp.317-324
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• 2007

The conversion reaction of ortho to para hydrogen was studied. The percentage of ortho and para hydrogen is mainly dependent on the equilibrium temperature. Because this reaction is known to be accelerated by the catalyst such as nickel-silicate and ruthenium on silica, we focused in the test and development of the catalysts. We studied metal-silicates because they provide high metal dispersion on support. Nickel-silicate, ruthenium-silicate and mixed-silicate were prepared by the coprecipitation method and used in the reaction at the temperature of liquid nitrogen. The conversion was measured by the difference of thermal conductivity between reference gas and sample gas. The activation condition was important and it affected the activities of the catalysts. Nickel-silicate showed high activities. Ruthenium-silicate also showed relative high activities but mixed-silicate showed poor activities.

• 한국분말재료학회지
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• 제6권1호
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• pp.18-35
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• 1999

Phase equilibria in the system Si3N4-TiC-TiCxN1-x-C-N were determined by thermodynamic calculations (CALPHAD-method). The reaction peaction paths for Si3N4-TiC and SiC-TiC composites in the Ti-Si-C-n system were simulated at I bar N2-pressure and varying terpreatures. At a temperature of 1923 K two tie-triangles (TiC0.34N0.66+SiC+C and TiC0.13N0.87+SiC+Si3N4) and two 2-phase fieds (TiCxN1-x+SiC; 0.13

• KSBB Journal
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• 제5권2호
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• pp.133-139
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• 1990

1회의 회분실험 데이터로부터 효소반응 속도식의 매개 변수를 쉽게 추정할 수 있는 방법을 제시하였다. 여러 가지 반응패턴을 갖는 모델식에 있어서 효소반응 데이터를 적용시킨 결과 정확하고 간편하게 매개변수값을 추정할 수 있었다. 가역반응의 경우에는 3개의 매개변수를 갖는 모델식의 형태로 평형 기질농도 및 매개변수를 추정할 수 있었다. 또한 반응특성이 잘 알려져 있지 않은 효소 반응 시스템에 있어서는 효소반응이 기질이나 생산물의 저해작용을 받는지 여부와 그 저해패턴을 확인할 수 있었다.

• 한국세라믹학회지
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• 제35권11호
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• pp.1233-1239
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• 1998

Gas phase compositions of the hot filament-assisted diamond CVD reaction were analyzed by on-line quadrupole mass analysis(QMA) technique. D2 isotope experiments showed that methance molecules were decomposed into atomic state and then recombined in to acetylene during transport the probe line. Although acetylene or ethylene was supplied instead of methane similar gas compositions were obtained when filament temperature was above 1500$^{\circ}C$ Therefore this system could be assumed near thermal equilibrium state. Filament temperature and reaction pressure variation experiments exhibited the same tendency between acetylene concentration and diamond growth rate and these results implied that acetylene molecule played the role of the reactive species in the diamond CVD reaction.

• Environmental Engineering Research
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• 제20권1호
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• pp.73-78
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• 2015

The aim of this study was to examine the phosphate (P) removal by quintinite from aqueous solutions. Batch experiments were performed to examine the effects of reaction time, temperature, initial phosphate concentration, initial solution pH and stream water on the phosphate adsorption to quintinite. Kinetic, thermodynamic and equilibrium isotherm models were used to analyze the experimental data. Results showed that the maximum P adsorption capacity was 4.77 mgP/g under given conditions (initial P concentration = 2-20 mgP/L; adsorbent dose = 1.2 g/L; reaction time = 4 hr). Kinetic model analysis showed that the pseudo second-order model was the most suitable for describing the kinetic data. Thermodynamic analysis indicated that phosphate sorption to quintinite increased with increasing temperature from 15 to $45^{\circ}C$, indicating the spontaneous and endothermic nature of sorption process (${\Delta}H^0=487.08\;kJ/mol$; ${\Delta}S^0=1,696.12\;J/(K{\cdot}mol)$; ${\Delta}G^0=-1.67$ to -52.56 kJ/mol). Equilibrium isotherm analysis demonstrated that both Freundlich and Redlich-Peterson models were suitable for describing the equilibrium data. In the pH experiments, the phosphate adsorption to quintinite was not varied at pH 3.0-7.1 (1.50-1.55 mgP/g) but decreased considerably at a highly alkaline solution (0.70 mgP/g at pH 11.0). Results also indicated that under given conditions (initial P concentration=2 mgP/L; adsorbent dose=0.8 g/L; reaction time=4 hr), phosphate removal in the stream water (1.88 mgP/g) was lower than that in the synthetic solution (2.07 mgP/g), possibly due to the presence of anions such as (bi)carbonate and sulfate in the stream water.