• 제목/요약/키워드: reaction kinetics

검색결과 1,382건 처리시간 0.026초

알칼리성 용매에서 과망간에 의한 세프포독심 프록세틸의 산화의 분광광도법적 조사: 속도론적 연구 (Spectrophotometric Investigation of Oxidation of Cefpodoxime Proxetil by Permanganate in Alkaline Medium: A Kinetic Study)

  • Khan, Aftab Aslam Parwaz;Mohd, Ayaz;Bano, Shaista;Siddiqi, K. S.
    • 대한화학회지
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    • 제53권6호
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    • pp.709-716
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    • 2009
  • 일정한 이온 세기의 알칼리 용액에서 과망간산에 의한 프포독심 프록세틸(Cefpodoxime Proxetil) 의 산화의 속도론적 경로가 분광광도법적으로 연구되었다. 그 반응은 과망간산 이온 농도에서 일차 속도론적으로 나타났으며, 프포독심 산과 알칼리 농도에서 단일 이하의 차수를 나타내었다. 용매의 이온 세기가 증가함에 따라 속도도 증가하였다. 산화 반응은 프포독심 산과 함께 복합체를 형성하는 알칼리-과망간산 종들을 통하여 진행된다. 반응물을 만들기 위해서 프포독심 산의 자유 라디칼과 과망간산의 다른 분자 사이의 빠른 반응에 이어서 다음 분해가 천천히 진행된다. 다양한 온도에서 반응의 조사는 제안하는 메커니즘의 느린 단계를 고려한 활성화 변수들의 결정할 수 있게 하고 일차 속도론을 따른다. 제안하는 메커니즘과 유도된 속도 법칙들은 관찰된 속도들과 일치하였다.

루테늄 촉매를 이용한 에탄의 수증기 개질 반응 Kinetics와 반응기 Sizing (Reaction Kinetics for Steam Reforming of Ethane over Ru Catalyst and Reactor Sizing)

  • 신미;성민준;장지수;이경은;조정호;이영철;박영권;전종기
    • 공업화학
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    • 제23권2호
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    • pp.204-209
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    • 2012
  • 상업용 루테늄 촉매 상에서 에탄의 수증기 개질 반응에 대한 kinetics 데이터를 얻기 위하여 반응온도, 에탄의 분압, 수증기/에탄의 비 등을 변화시키면서 반응 실험을 수행하였다. Kinetics 데이터를 사용하여 Power rate law kinetic model 과 Langmuir-Hinshelwood model의 parameter를 구하였다. 또한 kinetic model식을 적용하여 PRO/II를 이용한 공정 모사를 통해서 에탄의 수증기 개질 반응기 sizing을 수행하였다. 동일한 전환율을 얻기 위해서는 Power rate law model을 적용하였을 경우가 Langmuir-Hinshelwood model을 적용하였을 경우보다 개질 반응기의 부피가 더 큼을 알 수 있었다. Langmuir-Hinshelwood model에 의해 계산된 반응 속도가 반응 실험 결과에 의해 구해진 반응 속도와 더 잘 일치했기 때문에 Langmuir-Hinshelwood model을 적용하여 계산된 반응기의 크기가 실제 반응기 설계에 더 적절하다고 판단된다.

In Situ Transmission Electron Microscopy Study on the Reaction Kinetics of the Ni/Zr-interlayer/Ge System

  • Lee, Jae-Wook;Bae, Jee-Hwan;Kim, Tae-Hoon;Shin, Keesam;Lee, Je-Hyun;Song, Jung-Il;Yang, Cheol-Woong
    • Applied Microscopy
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    • 제45권1호
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    • pp.16-22
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    • 2015
  • The reaction kinetics of the growth of Ni germanide in the Ni/Zr-interlayer/Ge system was investigated using isothermal in situ annealing at three different temperatures in a transmission electron microscope. The growth rate of Ni germanide in the Ni/Zr-interlayer/Ge system was determined to be diffusion controlled and depended on the square root of the time, with the activation energy of $1.04P{\pm}0.04eV$. For the Ni/Zr-interlayer/Ge system, no intermediate or intermixing layer between the Zr-interlayer and Ge substrate was formed, and thus the Ni germanide was formed and grew uniformly due to Ni diffusion through the diffusion path created in the amorphous Zr-interlayer during the annealing process in the absence of any intermetallic compounds. The reaction kinetics in the Ni/Zr-interlayer/Ge system was affected only by the Zr-interlayer.

Investigation of Cure Kinetics and Storage Stability of the o-Cresol Novolac Epoxy Nanocomposites with Pre-intercalated Phenolic Hardeners

  • Hwang, Tae-Yong;Lee, Jae-Wook;Lee, Sang-Min;Nam, Gi-Joon
    • Macromolecular Research
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    • 제17권2호
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    • pp.121-127
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    • 2009
  • The cure kinetics of the epoxy-layered, silicate nanocomposites were studied by differential scanning calorimetry under isothermal and dynamic conditions. The materials used in this study were o-cresol novolac epoxy resin and phenol novolac hardener, with organically modified layered silicates. Various kinetic parameters, including the reaction order, activation energy, and kinetic rate constants, were investigated, and the storage stability of the epoxy-layered silicate nanocomposites was measured. To synthesize the epoxy-layered silicate nanocomposites, the phenolic hardener underwent pre-intercalation by layered silicate. From the cure kinetics analyses, the organically modified layered silicate decreased the activation energy during cure reaction in the epoxy/phenolic hardener system. In addition, the storage stability of the nanocomposite with the pre-intercalated phenolic hardener was significantly increased compared to that of the nanocomposite with direct mixing of epoxy, phenolic hardener, and layered silicate. This was due to the protective effect of the reaction between onium ions and epoxide groups.

작은 반응 매질에서 일어나는 촉매 반응 속도에 관한 연구 (Kinetics of Catalytic Reactions Occurring in a Small Reaction Volume)

  • 김중한;성재영
    • 대한화학회지
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    • 제52권3호
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    • pp.217-222
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    • 2008
  • 본 논문에서는 반응 매질의 부피가 촉매 반응 속도에 미치는 영향을 조사하였다. 단순하지만 정확한 모델에 대한 연구로부터 촉매 반응의 반응 속도 계수는 매질의 부피가 줄어들 수록 증가함을 알게 되었다. 평균 반응속도 상수(average reaction rate constant)는 Collins-Kimball 속도 상수의 일반화 된 형태로 얻어졌는데, 속도 상수는 부피의 효과를 보정해주는 인자를 포함하고 있다. 조사한 모델의 반응물 농도는 전통적 화학 반응론에서 예측되는 지수함수적 감소와는 상당한 차이를 보이는데 이는 기존 화학 반응속도론에서는 무시되는 반응분자 공간 분포의 비평형 확산운동(non-equilibrium diffusive dynamics)의 효과 때문이다. 반응 매질의 부피 가 유한한 점을 고려하면, 반응 시간이 충분히 오래 지났을 때, 기존의 확산지배 반응에서는 예측 되는 않는 지수 함수적 농도 감소가 얻어지는데, 그 속도 상수 역시 반응매질 크기에 의존한다.

Phase Distribution and Interface Chemistry by Solid State SiC/Ni Reaction

  • Lim, Chang-Sung;Shim, Kwang-Bo;Shin, Dong-Woo;Auh, Keun-Ho
    • The Korean Journal of Ceramics
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    • 제2권1호
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    • pp.19-24
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    • 1996
  • The phase distribution and interface chemistry by the solid-state reaction between SiC and nickel were studied at temperatures between $550 \;and\; 1250^{\circ}C$ for 0.5-100 h. The reaction with the formation of silicides and carbon was first observed above $650^{\circ}C$. At $750^{\circ}C$, as the reaction proceeded, the initially, formed $Ni_3Si_2$ layer was converted to $Ni_2$Si. The thin nickel film reacted completely with SiC after annealing at $950^{\circ}C$ for 2 h. The thermodynamically stable $Ni_2$Si is the only obsrved silicide in the reaction zone up to $1050^{\circ}C$. The formation of $Ni_2$Si layers with carbon precipitates alternated periodically with the carbon free layers. At temperatures between $950^{\circ}C$ and $1050^{\circ}C$, the typical layer sequences in the reaction zone is determined by quantitative microanalysis to be $SiC/Ni_2$$Si+C/Ni_2$$Si/Ni_2$$Si+C/…Ni_2$Si/Ni(Si)/Ni. The mechanism of the periodic band structure formation with the carbon precipitation behaviour was discussed in terms of reaction kinetics and thermodynamic considerations. The reaction kinetics is proposed to estimate the effective reaction constant from the parabolic growth of the reaction zone.

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Kinetics and Optimization of Dimethyl Carbonate Synthesis by Transesterification using Design of Experiment

  • Lee, Kilwoo;Yoo, Kye Sang
    • Korean Chemical Engineering Research
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    • 제56권3호
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    • pp.416-420
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    • 2018
  • A comprehensive kinetic study has been conducted on dimethyl carbonate synthesis by transesterification reaction of ethylene carbonate with methanol. An alkali base metal (KOH) was used as catalyst in the synthesis of DMC, and its catalytic ability was investigated in terms of kinetics. The experiment was performed in a batch reactor at atmospheric pressure. The reaction orders, the activation energy and the rate constants were determined for both forward and backward reactions. The reaction order for forward and backward reactions was 0.87 and 2.15, and the activation energy was 12.73 and 29.28 kJ/mol, respectively. Using the general factor analysis in the design of experiments, we analyzed the main effects and interactions according to the MeOH/EC, reaction temperature and KOH concentration. DMC yield with various reaction conditions was presented for all ranges using surface and contour plot. Furthermore, the optimal conditions for DMC yield were determined using response surface method.

디메틸에테르의 직접반응 속도론 (Kinetics on Direct Synthesis Dimethyl Ether)

  • 조원일;최창우;백영순;노경호
    • 한국가스학회:학술대회논문집
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    • 한국가스학회 2005년도 추계학술발표회 논문집
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    • pp.83-87
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    • 2005
  • The kinetics of the direct synthesis of DME was studied under different conditions over a temperature range of $220\~280^{\circ}C$, syngas ratio $1.2\~ 3.0$ All experiment were carried out over hybrid catalyst, composed to a methanol synthesis catalyst (Cu/ZnO/$Al_2O_3$) and a dehydration Catalyst ($\gamma$-Al_2O_3$) The observed reaction rate qualitatively follows a Langmiur-Hinshellwood type of reaction mechanism. Such a mechanism is considered with three reaction, methanol synthesis, methanol dehydration and water gas shift reaction. From a surface reaction with dissociative adsorption of hydrogen, methanol and water, individual reaction rate was determined

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디메틸테레프탈레이트와 1,4-부탄디올의 에스테르교환 반응 특성 (Transesterification Kinetics of Dimethyl Terephthalate with 1,4-Butanediol)

  • 조임표;이진홍;조상환;조민정;한명완;강경석
    • Korean Chemical Engineering Research
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    • 제51권1호
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    • pp.58-67
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    • 2013
  • PBT (polybutylene terephthalate)는 저흡수율, 치수 안정성, 내마모성 등 기계적 특성이 우수하며, 전기전자 부품, 자동차 부품, 각종 정밀 부품에 사용된다. DMT (dimethyl terephthalate)와 BD (1,4-butandiol)를 사용하여 PBT의 원료단량체인 BHBT (bis-hydroxybutyle terephthalate)를 생산하는 에스테르 교환 반응 반응에 대해 연구 하였다. 촉매로는 zinc acetate가 사용되었다. 기존의 연구에서는 반응 중 생성 메탄올이 제거되는 반회분식 반응기를 통한 kinetics 연구가 이루어져 역반응이 고려되지 않음에 따른 모델의 부정확함이 있었다. 본 연구에서는 회분식 반응기를 사용하고 반응 중 DMT와 메탄올 양을 정량하여 생성되는 MHBT (methyl hydroxylbutylene terephthalate)와 BHBT를 추정할 수 있도록 하고, 이 반응들에서 역반응들을 고려할 수 있도록 하여 보다 정확한 모델을 제안하였다. 다양한 반응속도 모델을 제시하였고, 이 모델들이 예측한 값들이 실험 데이터와 잘 일치함을 보였다.

Curing Kinetics of the No-Flow Underfill Encapsulant

  • Jung, Hye-Wook;Han, Sang-Gyun;Kim, Min-Young;Kim, Won-Ho
    • 한국마이크로전자및패키징학회:학술대회논문집
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    • 한국마이크로전자및패키징학회 2001년도 추계 기술심포지움
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    • pp.134-137
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    • 2001
  • The cure kinetics of a cycloalipatic epoxy / anhydride / Co(II) system for a no-flow underfill encapsulant, has been studied by using a differential scanning calorimetry(DSC) under isothermal and dynamic conditions over the temperature range of $160^{\circ}C ~220^{\circ}C$. The kinetic analysis was carried out by fitting dynamic/isothermal heating experimental data to the kinetic expressions to determine the reaction parameters, such as order of reaction and reaction constants. Diffusion-controlled reaction has been observed as the cure conversion increases and successfully analyzed by incorporating the diffusion control term into the rate equation. The prediction of reaction rates by the model equation corresponded well to experimental data at all temperature.

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