• Title/Summary/Keyword: Reaction rates

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Effects of Reaction Conditions for Improvement of Caramelization Rate (Caramel화 반응속도 향상을 위한 반응조건의 영향)

  • Park, Cheon-Woo;Kang, Kun-Og;Kim, Woo-Jung
    • Korean Journal of Food Science and Technology
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    • v.30 no.4
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    • pp.983-987
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    • 1998
  • Effects of sugars, temperature, pH and some chemicals on caramelization were investigated for improving of its reaction rates. Among the sugars tested, fructose showed the fastest reaction rate, followed by sucrose, glucose, starch syrup and maltose. As the reaction temperature increased from 80 to $110^{\circ}C$, the rate greatly increased by the range of $150{\sim}8000$ folds depending on sugars. It was indicated that pH 10 resulted in the highest reaction rate in the range of $pH{\;}4{\sim}10$. When several chemicals, such as phosphates and organic acid salts, were added to starch syrup, the rate increased by more than 10 folds, in particular effects of $K_2HPO_4$ and sodium salts of citrate, oxalate and succinate were significant.

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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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    • v.50 no.2
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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.

Recycling of Li2ZrO3 as LiCl and ZrO2 via a Chlorination Technique

  • Jeon, Min Ku;Kim, Sung-Wook;Lee, Keun-Young;Choi, Eun-Young
    • Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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    • v.19 no.2
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    • pp.271-278
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    • 2021
  • In this study, a chlorination technique for recycling Li2ZrO3, a reaction product of ZrO2-assisted rinsing process, was investigated to minimize the generation of secondary radioactive pyroprocessing waste. It was found that the reaction temperature was a key parameter that determined the reaction rate and maximum conversion ratio. In the temperature range of 400-600℃, an increase in the reaction temperature resulted in a profound increase in the reaction rate. Hence, according to the experimental results, a reaction temperature of at least 450℃ was proposed to ensure a Li2ZrO3 conversion ratio that exceeded 80% within 8 h of the reaction time. The activation energy was found to be 102 ± 2 kJ·mol-1·K-1 between 450 and 500℃. The formation of LiCl and ZrO2 as reaction products was confirmed by X-ray diffraction analysis. The experimental results obtained at various total flow rates revealed that the overall reaction rate depends on the Cl2 mass transfer rate in the experimental condition. The results of this study prove that the chlorination technique provides a solution to minimize the amount of radioactive waste generated during the ZrO2-assisted rinsing process.

Effects of Inorganic Aerosols on the Gas-Phase Reactions of the Hydroxyl Radical with Selected Aliphatic Alkanes

  • Oh, Sewon;Andino, Jean M.
    • Journal of Korean Society for Atmospheric Environment
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    • v.19 no.E3
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    • pp.129-136
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    • 2003
  • Effects of inorganic aerosols on the kinetics of the hydroxyl radical reactions with selected aliphatic alkanes have been investigated using the relative rate technique. The relative rates in the absence and presence of aerosols were determined for n-butane, n-pentane, n-hexane, n-octane, and n-decane. P-xylene was used as a reference compound. Inorganic aerosols including (NH$_4$)$_2$SO$_4$, NH$_4$NO$_3$, and NaCl aerosols at two different aerosol concentrations that are typical of polluted urban conditions were tested. Total surface areas of aerosols were 1400 (Condition I) and 3400 $\mu$$m^2$ cm$^{-3}$ (Condition II). Significant changes in the relative rates in the presence of the inorganic aerosols were not observed for the n-butanel/$.$OH, n-pentanel/$.$OH, n-hexanel/$.$OH, n-octanel/$.$OH, and n-decanel/$.$OH reactions versus p-xylenel/$.$OH reaction. These results suggest that the promoting effects depend on the semiconducting property of the aerosols and the nature of the organic compounds.

Hydrated Lime Roasting of Precious Metal Ores with A Cyclone Reactor

  • Cho, Chong S.
    • Proceedings of the Korea Association of Crystal Growth Conference
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    • 1997.06a
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    • pp.53-60
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    • 1997
  • The roasting of pyrite with a cyclone reactor have been studied in terms of investigating the reaction behavior of pyrite. The development of a fundamental model for pyrite oxidation and lime sulfation in a vertical cyclone reactor. The model assumes a chemical control shrinking core behavior for the pyrite and a fluid film control shrinking core behavior for the lime. The oxygen and sulphur dioxide concentrations and the energy balance for the gas, pyrite and lime particles are solved. The model was solved and characterized numerically. Experiments have been performed to study the influence of reaction parameters such as reactor temperatures, pyrite particle sizes, air flow rates, feeding rates, and mixing ratio of pyrite and lime. The oxidation and sulfation products were characterized chemically and physically.

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On the Number of Modes Required to Observe Forces in Flexible Structures (유연 구조물에서 반력 평가를 위해 요구되는 모드의 수)

  • Kim, Joo-Hyung;Kim, Sang-Sup
    • Proceedings of the KSME Conference
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    • 2001.11a
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    • pp.562-567
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    • 2001
  • The number of required modes to provide accurate force information in a truncated model of a flexible structure is investigated. In the case of modal truncation of a distributed parameter system, the difference in convergence rates between displacements and forces is discussed. The residual flexibility, a term from past literature, is used to recapture some of the lost force information in a truncated model. This paper presents numerical and experimental results of a study where the residual flexibility is used in conjunction with a Kalman filter so that accurate force information may be obtained from a small set of displacement measurements with a reduced-order model. The motivation for this paper is to be able to obtain accurate information about unmeasurable dynamic reaction forces in a rotating machine for diagnostic and control purposes.

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A Study on Gasification Reaction and Strength of Foundry Coke and Lump Anthracite Coal (주물용 코우크스와 무연괴탄의 가스화 반응과 강도에 관한 연구)

  • Cho, Nam-Don;Kim, Jong-Hoon
    • Journal of Korea Foundry Society
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    • v.9 no.3
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    • pp.247-256
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    • 1989
  • The gasification reaction rates by $CO_2$ in $CO/CO_2/N_2$ of various compositions in the temperature range of $900-1200^{\circ}C$ were measured for foundry coke and anthracite lump. The data for the rates was analyzed with Langmuir-Hinshelwood rate equations for the gasification of carbonaceous specimens. The values of the apparent activation energies of the reactions obtained from these data were ranged to be 47-99 and 73-128Kcal/mol respectively for foundry coke and for anthracite lump. The major contribution to decrease in tensile strength was shown to be attributable to the enlarging of the macropores in the coke and that of crack in the anthracite lump. Under the same experiment of the gasification of foundry coke, the rate of form coke was increasing as the addition of $Fe_2O_3$ increases.

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Kinetics and Mechanism of the Pyridinolysis of Diisopropyl Thiophosphinic Chloride in Acetonitrile

  • Hoque, Md. Ehtesham Ul;Lee, Hai-Whang
    • Bulletin of the Korean Chemical Society
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    • v.32 no.12
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    • pp.4387-4391
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    • 2011
  • The kinetic studies on the pyridinolysis of diisopropyl thiophosphinic chloride have been carried out in acetonitrile at $55.0^{\circ}C$. The free energy correlations for substituent X variations in the X-pyridines are biphasic concave upwards with a break point at X = 3-Ph. A concerted SN2 mechanism is proposed with a change of the attacking direction of the X-pyridine from a frontside attack for the strongly basic pyridines to a backside attack for the weakly basic pyridines. The factors to determine the rates and thio effects on the rates for the pyridinolyses of thiophophinic chloride, chlorothiophosphate, phosphinic chloride, phosphonochloridothioate, and chlorophosphate systems are briefly reviewed on the basis of the magnitude of the positive charge of the reaction center P atom and steric effects of the two ligands.

Rotary Kiln Flame and Heat Transfer Model - Analysis of Thermal Performance according to Fuel (로터리킬른 화염 및 열전달 모형 - 연료에 따른 열 성능 분석 사례)

  • Choi, Donghwan;Choi, Sangmin
    • Journal of the Korean Society of Combustion
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    • v.22 no.4
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    • pp.9-18
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    • 2017
  • This paper is to suggest a simple flame model for the analysis of an internal flame of rotary kilns and to present the application cases. Reaction rates in the multi combustion stages of the selected solid fuel were calculated considering the reaction rates with the Arrhenius type equations. In addition, primary and secondary air flow arrangement were considered. As a simple application case, the combustion trends according to the different solid fuels were described. Improved operating conditions as related with the fuel characteristics were shown to be important for the stable combustion characteristics and the performance of the reactors as defined by the exit temperature of the solid materials.