• Bulletin of the Korean Chemical Society
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• 제34권4호
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• pp.1145-1152
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• 2013

The rate constant of alkaline fading of methyl green ($ME^{2+}$) was measured in the presence of non ionic (TX-100), cationic (DTAB) and anionic (SDS) surfactants. $ME^{2+}$ hydrolyses and fades in neutral water and in this work we search the effects of surfactants on its fading rate. The rate of reaction showed remarkable dependence on the electrical charge of the used surfactants. It was observed that the reaction rate constant decreased in the presence of DTAB and SDS and increased in the presence of TX-100. Binding constants of $ME^{2+}$ to TX-100, DTAB and SDS and the related thermodynamic parameters were obtained by classical (or stoichiometric) model. The results show that binding of $ME^{2+}$ to TX-100 and DTAB are two-region and that of SDS is three-region. Also, the binding constants of $ME^{2+}$ to surfactant molecules in DTAB/TX-100 and SDS/TX-100 mixed solutions and their stoichiometric ratios were obtained.

• 한국물환경학회지
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• 제27권2호
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• pp.141-146
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• 2011

Loess, a natural clay, was evaluated as an adsorbent for the decolorization of Acid Orange II, an azo and reactive dye, from aqueous solution. Adsorption studies were performed at $30^{\circ}C$ and the effect of reaction time, loess dosage, initial concentration, loess particle size, pH, agitation rate were investigated to determine the optimum operation conditions. The removal efficiencies of color were measured to evaluate the effectiveness of loess. From this study, it was found that optimal reaction time was 10 min. Color removal efficiencies of Acid Orange II were increased as higher loess dosage, initial concentration and agitation rate. However, color removal efficiencies decreased when pH is high and loess particle becomes large. Adsorption of Acid Orange II fitted to the pseudo-second-order rate kinetics more than first-order rate kinetics. Langmuir and Freundlich adsorption isotherm constants and correlation coefficients were calculated and compared. It was concluded that the adsorption data of Acid Orange II onto loess fitted to the Freundlich model more than Langmuir model.

• 공업화학
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• 제5권2호
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• pp.230-237
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• 1994

Aliquat 336 상이동촉매에 의한 n-butyl acetate의 알칼리 가수분해반응을 액-액 불균일 반응계로 한 반응기구를 준1차반응 모델, 계면반응 모델 및 본체반응 모델로 나타내어 복잡한 액-액 불균일계 반응을 간단히 취급할 수 있었다. 분산교반조를 사용하여 측정한 반응전화율로부터 준1차반응 모델과 계면반응 모델 그리고 평면교반조로부터 본체반응 모델로서 반응기구를 각각 설명할 수 있었으며, 각 모델로부터 구한 반응속도상수는 $25^{\circ}C$에서 각각 $3.1{\times}10^{-4}$, $7.3{\times}10^{-4}$, $6.6m^3/kmol.s$이었다.

• 공업화학
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• 제18권5호
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• pp.415-423
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• 2007

톱밥 및 왕겨를 주 바이오매스 원으로 선정하여 열분해 특성을 고찰하였다. 열 중량 분석기를 이용하여 승온 속도를 달리하여 질소 분위기의 비등온 조건에서 열분해 분석을 수행하였다. 시료의 열분해 반응은 holocellulose가 주 열분해 대상인 저온 반응 영역과 lignin이 열분해 대상이 되는 고온 반응 영역으로 구분되며 이를 2단계 연속 반응 모델을 사용하여 해석하였다. 각 영역에 따라 1st order reaction model과 3-way transport model을 적용하여 톱밥 및 왕겨의 활성화 에너지를 저온 영역에서 82.5 kJ/mol, 85.1 kJ/mol 그리고 고온 영역에서 19.7 kJ/mol, 22.0 kJ/mol로 결정하였다. 승온 속도를 달리하여 결정된 반응 속도 상수는 Gaur-Reed의 제안 식에 따라 kinetic compensation relation을 통해 해석할 수 있었으며 이를 통해 임의의 승온 속도에서의 열분해 속도 상수를 잘 예측할 수 있었다.

• 폴리머
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• 제28권2호
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• pp.121-127
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• 2004

폴리(에틸렌 나프탈레이트)의 축중합 반응은 가역반응이므로 부반응 물질인 에틸렌 글라이콜의 신속한 제거가 높은 분자량의 제품을 얻는데 매우 중요하다. 본 연구에서는 폴리(에틸렌 나프탈레이트)올리고머로 박막을 제조하여 실제 반응기와 동일한 조건 하에서 (28$0^{\circ}C$, <0.1mmHg) 반응시켜 이 때 일어나는 물질 전달 현상을 관찰하고자 하였다. 여러 가치 두께의 박막을 제조하여 반응 실험한 결과 두께가 0.025cm 이하의 영역에서는 박막에서의 물질 전달 저항이 크지 않아 총괄 반응 속도에 영향을 미치지 않음을 관찰하였다. 물질 전달 모델 및 확산 모델을 사용하여 반응 결과를 예측한 결과 두 모델 모두 실험 결과를 잘 예측하였으나 확산 모델의 경우 중합도가 낮은 영역에서 물질 전달 모델에 비해 반응이 더 빨리 진행되는 경향을 보였다. 두 모델을 이용하여 물질 전달 관련 계수를 예측한 결과 폴리(에틸렌 나프탈레이트)에서의 확산 계수는 4.7${\times}$$10^{-6}$$\textrm{cm}^2$/sec, 물질 전달 계수는 1.4${\times}$$10^{-4}$cm/sce로 폴리(에틸렌 테레프탈레이트) 경우보다 작은 값을 보였다.

• 한국환경과학회지
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• 제30권6호
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• pp.429-439
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• 2021

Food waste is both an industrial and residential source of pollution, and there has been a great need for food waste reduction. As a preliminary step in this study, waste reduction is quantitatively modeled. This study presents two models based on kinetics: a simple kinetic model and a mass transport-shrinking model. In the simple kinetic model, the smaller is the reaction rate constant ratio k₁, the lower the rate of conversion from the raw material to intermediate products. Accordingly, the total elapsed reaction time becomes shorter. In the mass transport-shrinking model, the smaller is the microbial decomposition resistance versus the liquid mass transfer resistance, the greater is the reduction rate of the radius of spherical waste particles. Results showed that the computed reduction of waste mass in the second model agreed reasonably with that obtained from a few experimantal trials of biodegradation, in which the microbial effect appeared to dominate. All calculations were performed using MATLAB 2020 on PC.

• 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.

• 한국수소및신에너지학회논문집
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• 제29권1호
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• pp.90-96
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• 2018

Reaction characteristics and kinetics of a oxygen carrier (OCN717-R1SU) for chemical looping combustion (CLC) have been investigated using TGA by changing gas concentration (10-30 vol.% $CH_4$) and reaction temperature ($825-900^{\circ}C$). Reaction rate of OCN717-R1SU increased as temperature increased and it was found that reaction is delayed at the initial reaction regime. Johnson-Mehl-Avrami (JMA) model was adopted to explain the reaction phenomenon. The activation energy (E) determined by JMA model in reduction reaction of OCN717-R1SU is $151.7{\pm}2.03kJ/mol$ and pre-exponential factor and JMA exponent were also obtained. The parameters calculated in this study will be applied in design of the reactor and operation conditions for CLC process.

• 한국물환경학회지
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• 제25권3호
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• pp.459-463
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• 2009

The adsorption features of malachite green onto activated carbon have been investigated for its treatment from aqueous solution. The influential factors were examined the initial concentration of malachite green, reaction temperature, and pH. Under experimental conditions, adsorption equilibrium of malachite green was attained within 2 hr after the adsorption started. The adsorption reaction of malachite green followed the pseudo-second order rate model, and the adsorption rate constants(k2) decreased with increasing initial concentrations of malachite green. Adsorption behavior of malachite green on activated carbon was found to follow the Freundlich model well in the initial adsorbate concentration range. With increase in temperature, the adsorbed amount of malachite green at equilibrium increased, which indicate that the adsorption reaction was endothermic reaction. Thermodynamic parameters for malachite green adsorption reaction were estimated at varying temperatures, and in the pH range of 2-10, adsorption of malachite green increased.

• 한국연소학회지
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• 제22권4호
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• pp.19-26
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• 2017

This study investigates the gasification of coal char by $CO_2$ under high pressures in a drop tube furnace(DTF). The rate constants are derived for the shrinking core model using the conventional method based on the set reactor conditions. The computational fluid dynamic(CFD) simulations adopting the rate constants revealed that the carbon conversion was much slower than the experimental results, especially under high temperature and high partial pressure of reactants. Three reasons were identified for the discrepancy: i) shorter reaction time because of the entry region for heating, ii) lower particle temperature by the endothermic reaction, and iii) lower partial pressure of $CO_2$ by its consumption. Therefore, the rate constants were corrected based on the actual reaction conditions of the char. The CFD results updated using the corrected rate constants well matched with the measured values. Such correction of reaction conditions in a DTF is essential in deriving rate constants for any char conversion models by $H_2O$ and $O_2$ as well as $CO_2$.