• 제목/요약/키워드: Catalytic chemical reaction

검색결과 848건 처리시간 0.027초

열 방출률에 대한 마이크로 백금 촉매 연소기의 치수 설계 기준 (Design Criterion for the Size of Micro-scale Pt-catalytic Combustor in Respect of Heat Release Rate)

  • 이광구;스즈키 유지
    • 한국연소학회지
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    • 제19권4호
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    • pp.49-55
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    • 2014
  • Design criterion for the size of micro Pt-catalytic combustor is investigated in terms of heat release rate. One-dimensional plug flow model is applied to determine the surface reaction constants using the experimental data at stoichiometric butane-air mixture. With these reaction constants, the mass fraction of butane and heat release rate predicted by the plug flow model are in good agreement with the experimental data at the combustor exit. The relationship between the size of micro catalytic combustor and mixture flowrate is introduced in the form of product of two terms-the effect of fuel conversion efficiency, and the effect of chemical reaction rate and mass transfer rate.

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.

The Oxidation of Hydrazobenzene Catalyzed by Cobalt Complexes in Nonaqueous Solvents

  • Kim, Stephen S.B.;Hommer, Roger B.;Cannon, Roderick D.
    • Bulletin of the Korean Chemical Society
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    • 제27권2호
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    • pp.255-265
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    • 2006
  • The oxidation of hydrazobenzene by molecular oxygen in the polar solvent methanol is catalysed by a Schiff's base complex Co(3MeOsalen) which is a synthetic oxygen carrier. The products are trans-azobenzene and water. The rate of the reaction has been studied spectrophotometrically and the rate law established. A mechanism involving a ternary complex of catalyst, hydrazobenzene and molecular oxygen has been proposed. The kinetic studies show that a ternary complex $CoL{\cdot}H_2AB{\cdot}O_2$ is involved in the rate determining step. The reactions are summarised in a catalytic cycle. The kinetic data suggest that a ternary complex involving Co(3MeOsalen), triphenyl-phosphine and molecular oxygen is catalytically acive species but at higher triphenylphosphine concentrations the catalyst becomes inactive. The destruction of the catalytic activity could be due to the catalyst becoming coordinated with triphenyl phosphine at both z axis sites of the complex e.g. Co (3MeOsalen)$(PPh_3)_2$.

Hydrogen-bonded clusters in transformed Lewis acid to new Brønsted acid over WOx/SiO2 catalyst

  • Boonpai, Sirawat;Wannakao, Sippakorn;Panpranot, Joongjai;Praserthdam, Supareak;Chirawatkul, Prae;Praserthdam, Piyasan
    • Advances in nano research
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    • 제12권3호
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    • pp.291-300
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    • 2022
  • The behavior of hydrogen species on the surface of the catalyst during the Lewis acid transformation to form Brønsted acid sites over the spherical silica-supported WOx catalyst was investigated. To understand the structure-activity relationship of Lewis acid transformation and hydrogen bonding interactions, we explore the potential of using the in situ diffuse reflection infrared Fourier transform spectroscopy (DRIFTS) with adsorbed ammonia and hydrogen exposure. From the results of in situ DRIFTS measurements, Lewis acid sites on surface catalysts were transformed into new Brønsted acid sites upon hydrogen exposure. The adsorbed NH3 on Lewis acid sites migrated to Brønsted acid sites forming NH4+. The results show that the dissociated H atoms present on the catalyst surface formed new Si-OH hydroxyl species - the new Brønsted acid site. Besides, the isolated Si-O-W species is the key towards H-bond and Si-OH formation. Additionally, the H atoms adsorbed surrounding the Si-O-W species of mono-oxo O=WO4 and di-oxo (O=)2WO2 species, where the Si-O-W species are the main species presented on the Inc-SSP catalysts than that of the IWI-SSP catalysts.

아세틴 촉매상에서 글리세롤로부터 디클로로프로판올의 직접 제조 (Direct Preparation of Dichloropropanol from Glycerol over Acetin Catalyst)

  • 송선호;박동률;우성율;송원섭;권명숙;송인규
    • 청정기술
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    • 제15권1호
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    • pp.42-46
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    • 2009
  • 아세틴 촉매상에서 글리세롤(바이오디젤 제조과정의 부산물)과 염화수소 가스로부터 무용매 상태로 디클로로프로판올(DCP)을 직접 제조하는 반응을 기상-액상 회분식 반응기에서 수행하였다. 이를 위해 균일계 아세틴 촉매로 아세틴 혼합물(acetin mixture)과 트리아세틴을 사용하였다. 아세틴 촉매의 활성을 동일한 반응조건($110^{\circ}C$, 3 bar, 3시간)에서 수행된 무촉매 상태에서의 반응성과 비교하였다. 무촉매 반응에 비해 아세틴촉매를 사용한 반응에서 글리세롤의 전환율은 3%정도 증가하였으며 디클로로프로판올의 선택도는 50%가량 증가하였다. 또한 아세틴 혼합물보다는 트리아세틴의 촉매활성이 2% 정도 우수한 것으로 나타났다.

Catalytic Upgrading of Geodae-Uksae 1 over Mesoporous MCM-48 Catalysts

  • Jeon, Ki-Joon;Jin, Sung Ho;Park, Sung Hoon;Jeon, Jong-Ki;Jung, Sang-Chul;Ryu, Changkook;Park, Young-Kwon
    • Bulletin of the Korean Chemical Society
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    • 제35권7호
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    • pp.1951-1955
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    • 2014
  • Catalytic pyrolysis of Geodae-Uksae 1, a kind of miscanthus found in Korea, was carried out over mesoporous MCM-48 catalysts. For rapid product analysis and catalyst evaluation, pyrolysis-gas chromatography/mass spectrometry was used. X-ray diffraction, nitrogen sorption, pyridine adsorbed Fourier transform infrared, and NH3 temperature programmed desorption were utilized to analyze the properties of the catalysts. Compared to non-catalytic reaction, catalytic upgrading over mesoporous Al-MCM-48 catalysts produced a higher-quality bio-oil with a high stability and low oxygen content. Al-MCM-48 exhibited higher deoxygenation ability than Si-MCM-48 due to its higher acidity.

Molecular Modeling and its Experimental Verification for the Catalytic Mechanism of Candida antarctica Lipase B

  • Kwon, Cheong-Hoon;Shin, Dae-Young;Lee, Jong-Ho;Kim, Seung-Wook;Kang, Jeong-Won
    • Journal of Microbiology and Biotechnology
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    • 제17권7호
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    • pp.1098-1105
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    • 2007
  • Quantum mechanical and molecular dynamics simulation analysis has been performed on the model system for CALB (Candida antarctica lipase B) with esters to study the reaction mechanism and conformational preference of catalytic hydrolysis and the esterification reaction. Using quantum mechanical analysis, the ping-pong bi-bi mechanism was applied and energies and 3-dimensional binding configurations of the whole reaction pathways were calculated. Further molecular dynamics simulation analysis was performed on the basis of the transition state obtained from quantum mechanical study to observe the effect of structures of the substrates. Calculation results using substrates of different chain length and chiral configurations were compared for conformational preference. The calculated results showed very small influence on chain length, whereas chiral conformation showed big differences. Calculated results from molecular modeling studies have been compared qualitatively with the experimental data using racemic mixtures of (${\pm}$)-cis-4-acetamido-cyclopent-2-ene-1-ethyl acetate as substrates.

The Chemically Induced Hot Electron Flows on Metal-Semiconductor Schottky nanodiodes During Hydrogen Oxidation

  • Lee, Hyosun;Lee, Youngkeun;Lee, Changhwan;Kim, Sunmi;Park, Jeong Young
    • 한국진공학회:학술대회논문집
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    • 한국진공학회 2013년도 제45회 하계 정기학술대회 초록집
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    • pp.152-152
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    • 2013
  • Mechanism of energy conversion from chemical to electrical during exothermic catalytic reactions at the metal surfaces has been a fascinating and crucial subject in heterogeneous catalysis. A metal-semiconductor Schottky nanodiode is novel device for direct detection of chemically induced hot electrons which have sufficient energy to surmount the Schottky barrier. We measured a continuous chemicurrent during the hydrogen oxidation under of 760 Torr of O2 and 6 Torr of H2 by using Pt/Si and Pt/TiO2 nanodiodes at reaction temperatures and compared the chemicurrent with the reaction turnover rate. The thermoelectric current was measured by carrying out an experiment under O2 condition for elimination of the background current. Gas chromatograph and source meter were used for measurement of the chemical turnover rate and the chemicurrent, respectively. The correlation between the chemicurrent and the chemical turnover rate under hydrogen oxidation implies how hot electrons generated on the metal surface affect hydrogen oxidation.

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Effect of Butadiene in Catalytic Trimerization of Isobutene Using Commercial C4 Feeds

  • Yoon, Ji-Woong;Jhung, Sung-Hwa;Lee, Ji-Sun;Kim, Tae-Jin;Lee, Hee-Du;Chang, Jong-San
    • Bulletin of the Korean Chemical Society
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    • 제29권1호
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    • pp.57-60
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    • 2008
  • Catalytic oligomerization of isobutene to produce triisobutenes has been performed over a cation-exchange resin (Amberlyst-35) by using commercial C4 feeds. The catalytic activity in the oligomerization was retained without deactivation up to 90 h of reaction in a simulated reaction feed without butadiene, but its activity was significantly affected by the presence of butadiene in commercial C4 feeds. The isobutene conversion with time-on-stream was significantly decreased in the presence of butadiene, indicating the catalyst deactivation by butadiene. However, the stable activity for trimerization was accomplished when the oligomerization was carried out after eliminating butadiene by hydrogenation of the feeds. This work demonstrates that butadiene plays a role as a catalyst poison on the solid acid catalyst, so that its removal in the reactant feed is essential for practical application of trimerization.

Deep Desulfurization of Fuels by Heteropolyanion-Based Ionic Liquid

  • Li, Jinlei;Hu, Bing;Hu, Chuanqun
    • Bulletin of the Korean Chemical Society
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    • 제34권1호
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    • pp.225-230
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    • 2013
  • A new heteropolyanion-based ionic ($[Hmim]_5PMo_{10}V_2O_{40}$) was synthesized by the reaction of molybdovanadophosphoric acid ($H_5PMo_{10}O_{40}$) with N-methylimidazole. [$[Hmim]_5PMo_{10}V_2O_{40}$ showed a high catalytic activity in the oxidative desulfurization of sulfur-containing compounds in 1-methylimidazolium tetrafluoroborate ($[Hmim]BF_4$) ionic liquid using 30% aqueous $H_2O_2$ as the oxidant. The catalytic system was of high activity, simplified workup and flexible recyclability. The catalytic oxidation reactivity of sulfur-containing compounds decreased in the order dibenzothiophene (DBT) > 4,6-dimethyldibenzothiophene (4,6-DMDBT) > benzothiophene (BT). The influences of various parameters including reaction time (t) and temperature (T), catalyst dosage, and oxidant to sulfur molar ratio n(O)/n(S) on the desulfurization of model oil were investigated in details. 99.1% of DBT conversion in the model oil was achieved at atmospheric pressure under the optimal conditions: n(O)/n(S) = 4:1, $60^{\circ}C$, 100 min and molar ratio of catalyst to sulfur of 0.062. The ionic liquid can be recycled six times without significant decrease in activity.