• 제목/요약/키워드: Formation Kinetics

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R-134a 가스 하이드레이트 형성 속도에 미치는 식용 계면활성제 첨가의 영향 (Kinetics Change of the R-134a Gas Hydrate Formation in Seawater with the Addition of Edible Surfactants)

  • 정희철;김아람;임준혁;원용선
    • 청정기술
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    • 제22권3호
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    • pp.154-160
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    • 2016
  • 가스 하이드레이트 형성을 이용하여 담수를 생산하고자 하는 어떠한 공정이라도 가스 하이드레이트 형성속도는 경제적인 관점에서 매우 중요한 공정변수일 수밖에 없다. 이에 본 연구에서는 촉진제를 사용하여 R-134a(또는 HFC-134a) 가스 하이드레이트의 형성속도를 향상시키고자 하였는데 최종목표가 음용수 생산이므로 촉진제로 세가지 다른 형태의 식용 계면활성제를 선정하여 사용하였다. 음이온성인 카라기난(κ-carrageenan), 양쪽성인 레시틴(lecithin), 그리고 비이온성인 폴리소르베이트 80(polysorbate 80)이 그것이다. 식용 계면활성제의 농도를 변화시키면서 R-134a 가스 하이드레이트 형성속도가 어떻게 변하는지 관찰하였다. 어떠한 경우이든 식용 계면활성제의 첨가가 R-134a 가스 하이드레이트 형성속도를 향상시키는 것으로 관찰되었으며 그 효과는 폴리소르베이트 80 > 카라기난 > 레시틴의 순서를 보였다. 이론적인 설명을 위해 범밀도함수(DFT) 이론을 기반으로 한 분자모델링을 이용하여 각 식용 계면활성제를 구성하고 있는 원자들의 전하를 계산하였고 실험으로 관찰된 촉진제 효과가 계면활성제 내의 수소결합을 할 수 있는 산소들의 수와 그 산소들의 원자전하 값들이 음수인 정도에 비례하는 관계가 있음을 알 수 있었다.

석탄가스 선회난류 비예혼합 화염장의 화염구조 및 NOx 배출특성 해석 (Numerical Study on Structure and Pollutant Formation for Syngas Turbulent Nonpremixed Swirling Flames)

  • 이정원;강성모;김용모;주용진
    • 한국연소학회지
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    • 제14권2호
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    • pp.10-17
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    • 2009
  • The present study numerically investigate the effects of the Syngas chemical kinetics on the basic flame properties and the structure of the Syngas nonpremixed flames. In order to realistically represent the turbulencechemistry interaction and the spatial inhomogeneity of scalar dissipation rate, the Eulerian Particle Flamelet Model (EPFM) with multiple flamelets has been applied to simulate the combustion processes and NOx formation in the syngas turbulent nonpremixed flames. Validation cases include the Syngas turbulent nonpremixed jet and swirling flames. Based on numerical results, the detailed discussion has been made for the effects of the chemical kinetics, the flame structure, and NOx formation characteristics in the turbulent Syngas nonpremixed flames.

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개질기 혼합영역에서 탄화수소 연료의 반응 특성에 대한 연구 (Kinetic Study on the Mixing Region of a Hydrocarbon Reformer)

  • 김선영;배중면
    • 한국수소및신에너지학회논문집
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    • 제22권3호
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    • pp.357-362
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    • 2011
  • Complete mixture preparation of reactants prior to catalytic reforming is an enormously important step for successful operation of a fuel reformer. Incomplete mixing between fuel and reforming agents such as air and steam can cause temperature overshoot and deposit formation which can lead the failure of operation. For that purpose it is required to apply computational models describing coupled kinetics and transport phenomena in the mixing region, which are computationally expensive. Therefore, it is advantageous to analyze the gas-phase reaction kinetics prior to application of the coupled model. This study suggests one of the important design constraints, the required residence time in the mixing chamber to avoid substantial gas-phase reactions which can lead serious deposit formation on the downstream catalyst. The reactivity of various gaseous and liquid fuels were compared, then liquid fuels are far more reactive than gaseous fuels. n-Octane was used as a surrogate among the various hydrocarbons, which is one of the traditional liquid fuel surrogates. The conversion was slighted effected by reactants composition described by O/C and S/C. Finally, threshold residence times in the mixing region of a hydrocarbon reformer were studied and the mixing chamber is required to be designed to make complete mixture of reactants by tens of milliseconds at the temperature lower than $400^{\circ}C$.

A Study on Reaction Kinetics of PTMG/TDI Prepolymer with MOCA by Non-Isothermal DSC

  • Ahn, WonSool;Eom, Seong-Ho
    • Elastomers and Composites
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    • 제50권2호
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    • pp.92-97
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    • 2015
  • A study on reaction kinetics for a PTMG/TDI prepolymer with 2,2'-dichloro-4,4'-methylenedianiline (MOCA), of which formulations may be generally used for fabricating high performance polyurethane elastomers, was peformed using non-isothermal differential scanning calorimetry (DSC). A number of thermograms were obtained at several constant heating rates, and analysed using Flynn-Wall-Ozawa (FWO) isoconversional method for activation energy, $E_a$ and extended-Avrami equation for reaction order, n. Urea formation reaction of the present system was observed to occur through the simple exothermic reaction process in the temperature range of $100{\sim}130^{\circ}C$ for the heating rate of $3{\sim}7^{\circ}C/min$. and could be well-fitted with generalized sigmoid function. Though activation energy was nearly constant as $53.0{\pm}0.5kJ/mol$, it tended to increase a little at initial stage, but it decreases at later stage by the transformation into diffusion-controlled reaction due to the increased viscosity. Reaction order was evaluated as about 2.8, which was somewhat higher than the generally well-known $2^{nd}$ order values for the various urea reactions. Both the reaction order and reaction rate explicitly increased with temperature, which was considered as the indication of occurring the side reactions such as allophanate or biuret formation.

Kinetic Studies of Alkaline Protease from Bacillus licheniformis NCIM-2042

  • Bhunia, Biswanath;Basak, Bikram;Bhattacharya, Pinaki;Dey, Apurba
    • Journal of Microbiology and Biotechnology
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    • 제22권12호
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    • pp.1758-1766
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    • 2012
  • An extensive investigation was carried out to describe the kinetics of cell growth, substrate consumption, and product formation in the batch fermentation using starch as substrate. Evaluation of intrinsic kinetic parameters was carried out using a best-fit unstructured model. A nonlinear regression technique was applied for computational purpose. The Andrew's model showed a comparatively better $R^2$ value among all tested models. The values of specific growth rate (${\mu}_{max}$), saturation constant ($K_S$), inhibition constant ($K_I$), and $Y_{X/S}$ were found to be 0.109 $h^{-1}$, 11.1 g/l, 0.012 g/l, and 1.003, respectively. The Leudeking-Piret model was used to study the product formation kinetics and the process was found to be growth-associated. The growth-associated constant (${\alpha}$) for protease production was sensitive to substrate concentration. Its value was fairly constant up to a substrate concentration of 30.8 g/l, and then decreased.

Monoclonal Antibody Refolding and Assembly: Protein Disulfide Isomerase Reaction Kinetics

  • Park, Sun-Ho;Ryu, Dewey D.Y.
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제8권2호
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    • pp.59-63
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    • 2003
  • The protein disulfide isomerase (PDI) reaction kinetics has been studied to evaluate its effect on the monoclonal antibody (Mab) refolding and assembly which accompanies disulfide bend formation. The MAb in vitro assembly experiments showed that the assembly rate of heavy and light chains can be greatly enhanced in the presence of PDI as compared to the rate of assembly obtained by the air-oxidation. The reassembly patterns of MAb in-termediates were identical for both with and without PDI, suggesting that the PDI does not determine the MAb assembly pathway, but rather facilitates the rate of MAb assembly by promoting PDI catalyzed disulfide bond formation. The effect of growth rate on PDI activities for MAb production has also been examined by using continuous culture system. The specific MAb productivity of hybridoma cells decreased as the growth rate increased. However, PDI activities were nearly constant fur a wide range of growth rates except very high growth rate, indicating that no direct correlation between PDI activity and specific MAb productivity exists.

Monoclonal Antibody Refolding and Assembly: Protein Disulfide Isomerase Reaction Kinetics

  • Park, Sun-Ho;Ryu, Dewey D.Y.
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제1권1호
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    • pp.13-17
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    • 1996
  • The protein disulfide isomerase(PDI) reaction kinetics has been studied to evaluate its effect on the monoclonal antibody(MAb) refolding and assembly which accompanies disulfide bond formation The MAb in vitro assembly experiments showed that the assembly rate of heavy and light chains can be greatly enhanced in the presence of PDI as compared to the rate of assembly obtained by the air-oxidation. The reassembly patterns of MAb intermediates were identical for both with and without PDI, suggesting that the PDI does not determine the MAb assembly pathway, but rather facilitates the rate of MAb assembly by promoting PDI catalyzed disulfide bond formation. The effect of growth rate on PDI activities for MAb production has also been examined by using continuous culture system. The specific MAb productivity of hybridoma cells decreased as the growth rate increased. However, PDI activities were nearly constant for a wide range of growth rates except very high growth rate, indicating that no direct correlation between PDI activity and specific MAb productivity exists.

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QCM Study of β-Casein Adsorption on the Hydrophobic Surface: Effect of Ionic Strength and Cations

  • Lee, Myung-Hee;Park, Su-Kyung;Chung, Chin-Kap;Kim, Hack-Jin
    • Bulletin of the Korean Chemical Society
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    • 제25권7호
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    • pp.1031-1035
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    • 2004
  • The adsorption kinetics of ${\beta}$-casein on a hydrophobic surface has been studied by means of the quartz crystal microbalance (QCM). The self assembled monolayer of 1-octadecanethiol on a gold coated quartz crystal was used as a hydrophobic surface for adsorption. The adsorption kinetics was monitored in different solution conditions. Formation of monolayer is observed in most cases. At high concentration of protein, micelle formation which is interrupted by high ionic strength of solution is observed. Casein binding cations such as $Ca^{2+},\;Ba^{2+}\;and\;Al^{3+}$ increase the hydrophobicity of the protein and the multiple layer adsorption occurs. The strong and weak points of the QCM method in the study of protein adsorption are discussed.

Effect of Dealloying Condition on the Formation of Nanoporous Structure in Melt-Spun Al60Ge30Mn10 Alloy

  • Kim, Kang Cheol;Kim, Won Tae;Kim, Do Hyang
    • Applied Microscopy
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    • 제46권3호
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    • pp.160-163
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    • 2016
  • Effect of dealloying condition on the formation of nanoporous structure in melt-spun $Al_{60}Ge_{30}Mn_{10}$ alloy has been investigated in the present study. In as-melt-spun $Al_{60}Ge_{30}Mn_{10}$ alloy spinodal decomposition occurs in the undercooled liquid during cooling, leading to amorphous phase separation. By immersing the as-melt-spun $Al_{60}Ge_{30}Mn_{10}$ alloy in 5 wt% HCl solution, Al-rich amorphous region is leached out, resulting in an interconnected nano-porous $GeO_x$ with an amorphous structure. The dealloying temperature strongly affects the whole dealloying process. At higher dealloying temperature, dissolution kinetics and surface diffusion/agglomeration rate become higher, resulting in the accelerated dealloying kinetics, i.e., larger dealloying depth and coarser pore-ligament structure.