• 제목/요약/키워드: model reaction

검색결과 2,874건 처리시간 0.033초

Evaluation of the hydration heat and strength progress of cement-fly ash binary composite

  • Xiao-Yong Wang
    • Journal of Ceramic Processing Research
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    • 제21권6호
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    • pp.622-631
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    • 2020
  • Fly ash is an industry by-product of thermal power factories that is broadly utilized in the concrete industry. This research shows a framework for evaluating the hydration heat, reaction amount, and strength progress of cement-fly ash binary composite. First, we conducted an experiment to study the isothermal hydration heat of fly ash composite paste with assorted fly ash contents and temperatures. According to the experimental outcomes of cumulative hydration heat, the coefficients of a kinetic reaction model of fly ash were determined. Furthermore, the reaction amount of fly ash was calculated using a fly ash reaction model. We discovered that the reaction of fly ash is considerably improved at elevated temperatures. The reaction amount of fly ash decreases with the growing content of fly ash. Second, in line with the reaction amount of fly ash and cement, we developed a straight-line equation for evaluating the strength progress of binary composite. The strength progress model applies to a number of water-to-binder ratios and fly ash substitution ratios. Summarily, the suggested hydration-heat-strength model is helpful for understanding the material style of fly ash concrete.

탄재를 포함한 산화철 펠릿 소성 공정 수치 모델의 입자 반응 모델 적용 (A discussion on the application of particle reaction model for iron ore pellet induration process modeling)

  • 안형준;최상민
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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    • pp.165-166
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    • 2014
  • The application of particle reaction model in the packed bed process modeling is discussed for iron ore pellet induration process. Combustion of coke breeze in the pellet is estimated by using shrinking unreacted-core model and grain model in which the progress of chemical reaction is described in different concepts. Under the identical inlet gas and solid conditions, the calculation using shrinking core model showed deviated results in terms of temperature profile and conversion fraction, which may imply the significance of selecting proper particle reaction model in consideration of particle characteristics and process operation conditions.

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大氣汚染物質의 光化學 反應 모델에 關한 硏究 (A Study on the Photochemical Reaction Model of Air Pollutants)

  • 이화운;박종길
    • 한국대기환경학회지
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    • 제8권1호
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    • pp.74-83
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    • 1992
  • Photochemical reactions are important for the diurnal variation of the concentrations of air pollutants in the urban atmosphere. A photochemical reaction model was developed, which includes in terms of the effective chemical reaction. Various experimental results were introduced to the construction of model. To verify the applicability of the model, the simulated results were compared with those observed. By comparing the simulated results with those observed, it was shown that those two are in good agreement qualitatively. As a result, the photochemical reaction model which has been developed in this study is found to be useful for the prediction of concentrations of air pollutants in the atmosphere.

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A new gas-solid reaction model for voloxidation process with spallation

  • Ryu, Je Ir;Woo, Seung Min
    • Nuclear Engineering and Technology
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    • 제50권1호
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    • pp.145-150
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    • 2018
  • A new methodology, the crack-spallation model, has been developed to analyze gas-solid reactions dominated by crack growth inside of the solid reactant and spallation phenomena. The new model physically represents three processes of the reaction progress: (1) diffusion of gas reactant through pores; (2) growth of product particle in pores; and (3) crack and spallation of solid reactant. The validation of this method has been conducted by comparison of results obtained in an experiment for oxidation of $UO_2$ and the shrinking core model. The reaction progress evaluated by the crack-spallation model shows better agreement with the experimental data than that evaluated by the shrinking core model. To understand the trigger point during the reaction progress, a detailed analysis has been conducted. A parametric study also has been performed to determine mass diffusivities of the gas reactant and volume increase constants of the product particles. This method can be appropriately applied to the gas-solid reaction based on the crack and spallation phenomena such as the voloxidation process.

과학기술위성 2호 Reaction Wheel Assembly Interface Unit Proto Flight Model 개발 (Engineering Model Design and Implementation Proto Flight Model of Reaction Wheel Assembly Interface Unit for STSAT-2)

  • 김세일;강경인;이성호
    • 한국항공우주학회지
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    • 제34권5호
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    • pp.88-92
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    • 2006
  • 과학기술위성 2호 사용되는 구동기인 반작용 휠(Reaction Wheel Assembly, RWA)과 위성 시스템을 연결해주는 인터페이스를 담당하는 Reaction Wheel Assembly Interface Unit(RIU)의 Proto Flight Model의 개발이 완료되고 동작시험을 마쳤다. RIU는 RWA에 공급되는 전원을 켜고 끄는 스위치와 명령을 주고 받는 위성탑재 컴퓨터(OBC)의 통신 회선을 선택하는 멀티플렉서, 그리고 RWA에 연결되는 물리적 통신라인으로 구성된다.

진동대 시험을 통한 액상화되는 지반의 수평지반반력계수에 대한 연구 (Modulus of Horizontal Subgrade Reaction in Liquefying Sand by Shaking Table Test)

  • 박종관;한성길;김상규;이용도
    • 한국지반공학회:학술대회논문집
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    • 한국지반공학회 2000년도 봄 학술발표회 논문집
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    • pp.255-262
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    • 2000
  • Shaking table tests were peformed to evaluate the subgrade reaction of ground according to the build-up of pore water pressure. Model pile was installed in the sand ground. The acceleration of the model ground, the pore water pressure build-up and displacement of pile were recorded by measuring devices. Subgrade reaction approach based on Winker soil model was applied to obtain the modulus of the horizontal subgrade reaction. The results of analysis show that the reduction factor of the subgrade reaction due to pore pressure increase is about 1 and the horizontal subgrade reaction of liquefied ground is not influenced by the stiffness of pile, a ground acceleration and the intial ground density.

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PATTERN FORMATION IN A GENERAL DEGN-HARRISON REACTION MODEL

  • Zhou, Jun
    • 대한수학회보
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    • 제54권2호
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    • pp.655-666
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    • 2017
  • In this paper, we study the pattern formation to a general Degn-Harrison reaction model. We show Turing instability happens by analyzing the stability of the unique positive equilibrium with respect to the PDE model and the corresponding ODE model, which indicate the existence of the non-constant steady state solutions. We also show the existence periodic solutions of the PDE model and the ODE model by using Hopf bifurcation theory. Numerical simulations are presented to verify and illustrate the theoretical results.

Dimethyl Naphthalate와 Ethylene Glycol의 에스테르 교환반응에 관한 연구 (A Study on the Ester Interchange Reaction of Dimethyl Naphthalate with Ethylene Glycol)

  • 소순용;정성일
    • 폴리머
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    • 제25권1호
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    • pp.25-32
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    • 2001
  • ${\circ}C$ 범위에서 아연과 망간촉매를 사용하여 에스테르 교환반응시켜 반응속도를 살펴보았다. 반응은 반회분식 반응기에서 비등온 조건으로 진행되었고 반응온도와 메탄올 유출량으로 반응성을 평가하였다. 반응모델로서는 관능기 모델과 분자종 모델을 적용하여 상호 비교하였다. 아연촉매를 사용할 경우 DMN과 EG의 반응속도는 methyl hydroxyethyl naphthalate(MHEN)와 EG의 반응속도에 비해 1.4배정도 였으나 망간촉매를 사용할 경우 4.3배정도로 촉매 종류에 따라 반응성이 크게 차이가 있음을 알 수 있었다. 아연촉매의 경우 DMN 및 MHEN과 EG의 반응에 대한 촉매농도의 반응차수는 1보다 작았으나, 망간촉매의 경우 오히려 1보다 컸다. 활성화에너지는 DMN과 MHEN의 분자종 차이에 관계없이 아연과 망간촉매의 경우 각각 25000, 28750 cal/mol이었다. 두 가지 반응모델을 비교하여 본 결과 분자종 모델이 반응현상을 잘 표현함을 알 수 있었다.

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액-액 불균일계에서 상이동촉매의 반응속도론 해석 (Kinetics in Phase Transfer Catalysis with Heterogeneous Liquid-Liquid System)

  • 박상욱;문진복;황경선
    • 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.

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다양한 온도에서 석탄/바이오매스의 혼합 촤-CO2 가스화 반응특성 연구 (Kinetic Study of Coal/Biomass Blended Char-CO2 Gasification Reaction at Various temperature)

  • 김정수;김상겸;조종훈;이시훈;이영우
    • Korean Chemical Engineering Research
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    • 제53권6호
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    • pp.746-754
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    • 2015
  • 본 연구는 이온교환법을 통해 Ni촉매를 담지한 저등급 석탄(인도네시아 Eco탄)과 바이오매스(대한민국 상록수)의 혼합물로부터 제조된 촤(char)를 $700{\sim}900^{\circ}C$ 등온조건에서 온도가 반응속도에 미치는 영향에 대해 알아보았다. $Char-CO_2$ 가스화 반응은 700, 750, 800, 850, $900^{\circ}C$의 온도에서 진행하였으며, 기-고체 반응의 가스화 거동특성을 알아보기 위하여 각각 다른 가정을 갖고 있는 shrinking core model(SCM), volumetric reaction model(VRM), random pore model(RPM), modified volumetric reaction model(MVRM)을 실험결과에 적용하여 비교하였다. Arrhenius equation를 이용하여 Ni-coal/biomass와 Non-catalyst coal/biomass의 활성화에너지를 구하였고 이를 비교하였다.