• Title/Summary/Keyword: Oxidation of carbon

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Kinetic Model for Oxidation of Carbon Fiber/Glass Matrix Composites

  • Park, Chan;Park, Hee-Lack
    • The Korean Journal of Ceramics
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    • v.4 no.3
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    • pp.254-259
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    • 1998
  • A kinetic model predicting the oxidation of carbon fiber reinforced glass matrix composites has been described. The weight loss of composites during oxidation implied that a gasification of carbon fiber takes place and the transport of reactants $(O_2)$ or product (CO or $CO_3$) in the glass matrix was partially the rate controlling step. The kinetic model in this study was based on the work of Sohn and Szekely which may be regarded as a generalization of numerous models in the gas-solid reaction system. A comparison of this model with experimental data is also presented.

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Structural Changes during Oxidation Process of Anisotopic Mesophase Carbon fibers(I) - TEM and XRD Study (산화반응에 의한 이방성 메조페이스 탄소섬유의 구조 변화(I) - TEM 및 XRD를 이용한 분석)

  • Roh, J.S.
    • Korean Journal of Materials Research
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    • v.13 no.12
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    • pp.825-830
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    • 2003
  • Structural changes during oxidation of anisotopic mesophase carbon fiber(AMCFs) have been observed with TEM and XRD. It was shown that the AMCFs are three dimensionally stacked structure of turbostratic layers, and are non-homogeneous structure which consist of the highly ordered areas and the random areas. The $d_{ 002}$, Lc, and La of AMCFs which were measured by XRD were 3.44, 146, and $135\AA$, respectively. It was observed that the oxidation initiated at the random areas, because the $d_{002}$ / decreased to the value of 3.41 $\AA$ during initial oxidation stage. It was also observed that the La of the oxidized AMCFs increased up to 182 $\AA$ during the whole oxidation process, and the $d_{002}$ of that increases up to 9.44 $\AA$ when the burn-off is over the degree of 20%. Therefore, it was suggested that the micro-crystalline grew up by heat treatment effects during the fibers were oxidized, In addition, it was shown that there was difference in the measured value of La by XRD and TEM, in case of 39% oxidized fibers for example, the measured La was $ 165\AA$ by XRD and in the range of 180∼220 $\AA$ by TEM.

Catalytic Oxidation Conversion Characteristics of VOCs in Supercritical Fluid Media (초임계유체 반응매개상에서 VOCs의 촉매산화 전환특성)

  • 이승범;홍인권;이재동
    • Journal of environmental and Sanitary engineering
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    • v.16 no.4
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    • pp.69-76
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    • 2001
  • The catalytic oxidation of volatile organic compounds (VOCs), which were benzene and toluene, was studied in the supercritical carbon dioxide($SC-CO_2$) media. In $SC-CO_2$ media, the deep oxidation conversion of VOCs was increased with the temperature and pressure. The deep oxidation conversion in SC -$CO_2$ media is better than that in air media at same pressure condition. This can be explained by the solubility of VOCs in $SC-CO_2$. The many intermediates produced by the partial oxidation of VOCs were detected from off-line samples. The intermediates were Identified as benzene, toluene, benzaldehyde, phenol, naphthalene, 1,1`-biphenyl, benzoic acid, 3-methylphenol, 1,1'-(1,2-ethanediyl)bis- benzene, 1,1'-(1,2-ethene- diyl)bis-benzene, anthracene, and so on. The amount of intermediates was decreased as the molar radio of oxygen to carbon dioxide was decreased. When the molar ratio of oxygen to carbon dioxide was 1 : 16, the deep conversion was kept constant. Thus, the catalytic oxidation process in $SC-CO_2$ media can be combined on-line with supercritical fluid extraction of environmental matrices and supercritical regeneration of used adsorbent. Thus, the nontoxic $SC-CO_2$ media process was suggested as the new VOCs control technology.

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Liquid Phase Oxidation of Xylenes: Effects of Water Concentration and Alkali Metals

  • Jhung, Sung-Hwa;Lee, Ki-Hwa;Park, Youn-Seok
    • Bulletin of the Korean Chemical Society
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    • v.23 no.1
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    • pp.59-64
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    • 2002
  • A facile and precise batch oxidation reaction system allows continuous monitoring of the oxidation rate and cumulated oxygen conversion of xylenes, and the side reactions to carbon monoxide and carbon dioxide may also be studied. The oxidation reaction can be analyzed precisely with the rate and amount of oxygen consumed. The reaction reveals that 4-carboxybenzaldehyde is an unstable intermediate of p-xylene oxidation as the reaction proceeds instantaneously from p-toluic acid to TPA (terephthalic acid). The alkali metals accelerate oxidation, even though they retard the reaction initially. The oxidation rate increases with decreasing water concentration. However, in the later part of reaction, the reactivity decreases a bit if the water concentration is very low. This retarding effect of water can be overcome partly by the addition of potassium. The oxidation of o-xylene, compared with the oxidation of p-xylene and m-xylene, proceeds quite fast initially, however, the oxidation rate of xylene isomers in the later stage of reaction is in the order of p-xylene > mxylene > o-xylene.

Methanol Oxidation Effect on Carbon Supported Pt Particles Studied by 13C NMR, XRD, and TEM

  • Han, Kee Sung;Han, Oc Hee
    • Bulletin of the Korean Chemical Society
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    • v.27 no.8
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    • pp.1121-1126
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    • 2006
  • Methanol oxidation effect on carbon supported Pt was investigated as a function of Pt content in a sample which is closely correlated with Pt particle sizes. After prolonged methanol oxidation the Pt particle size did not change within the experimental error ranges. The $^{13}C$ chemical shift and linewidth of CO adsorbed on Pt show non-linear behavior simply due to the Pt particle size difference. The Pt size variation difference between this work and the previous reports of the particle growths is explained by the experimental temperature difference.

Equilibrium and Dynamic Adsorption of Methylene Blue from Aqueous Solutions by Surface Modified Activated Carbons

  • Goyal, Meenakshi;Singh, Sukhmehar;Bansal, Roop C.
    • Carbon letters
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    • v.5 no.4
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    • pp.170-179
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    • 2004
  • The equilibrium and dynamic adsorption of methylene blue from aqueous solutions by activated carbons have been studied. The equilibrium studies have been carried out on two samples of activated carbon fibres and two samples of granulated activated carbons. These activated carbons have different BET surface areas and are associated with varying amounts of carbon oxygen surface groups. The amounts of these surface groups was enhanced by oxidation with $HNO_3$ and $O_2$ gas at $350^{\circ}C$ and decreased by degassing at increasing temperatures of $400^{\circ}$, $650^{\circ}$ and $950^{\circ}C$. The adsorption increases on oxidation of the carbon surface and decreases on degassing. The increase in adsorption has been attributed to the formation of acidic carbon-oxygen surface groups and the decrease in adsorption on degassing to their elimination. The dynamic adsorption studies have been carried out on the two granulated activated carbons using two 50 mm diameter glass columns at a feed concentration of 300 mg/L and at different hydraulic loading rates (HLR) and bed heights. The minimum achievable concentrations are comparatively lower while the adsorption capacities are higher for GAC-S under the same operating conditions. The adsorption capacity of a carbon increases with increase in HLR but the rate of increase decreases at higher HLR values.

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Mechanical Interfacial Properties of Anodically Oxidized Carbon Fibers-reinforced Composites (양극산화 처리된 탄소섬유 강화 복합재료의 기계적 계면물성)

  • Park, Soo-Jin;Oh, Jin-Seok;Lee, Jae-Rock
    • Proceedings of the Korean Society For Composite Materials Conference
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    • 2003.04a
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    • pp.188-191
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    • 2003
  • In this wort. the effect of anodic oxidation on surface characteristics of high strength PAN-based carbon fibers is investigated in terms of surface and mechanical interfacial properties of the composites. As a result, the acidity of carbon fiber surfaces is increased, due to the development of oxygen functional groups in the presence of anodic oxidation. Also. it is found that the critical stress intensity factor ($K_{IC}$) is improved in the oxidized fibers-reinforced composites. which can be attributed to the good wettability between fibers and epoxy resin matrix.

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Influence of Oxidation Inhibitor on Carbon-Carbon Composites : 7. Studies on Work of Adhesion and Fracture Toughness of Carbon-Carbon Composites (산화억제제를 첨가한 탄소/탄소 복합재료의 물성에 관한 연구 : 7. 탄소/탄소 복합재료외 부착력과 파괴인성)

  • 박수진;서민강;이재락
    • Polymer(Korea)
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    • v.25 no.3
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    • pp.435-440
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    • 2001
  • The objective of this study was to examine the effect of oxidation inhibitor contents on the work of adhesion, fracture toughness, and impact strength of the unidirectional carbon-carbon composites (C/C composites). The molybdenum disilicide ($MoSi_2$) used as an oxidation inhibitor was impregnated with phenolic resins to improve the anti-oxidation properties of the composites in different concentrations of 4, 12 and 20 wt%. Based on Wilhelmy equation, the work of adhesion of C/C composites was calculated by contact angle methods. Fracture toughness and impact strength were pressured by three-point bending test for the critical intensity factor ($K_IC$) and Izod test method, respectively. As a result, the composites made with $MoSi_2$ resulted in an increasing of both fracture toughness and impact strength. Especially, the composites made with 12 wt% $MoSi_2$ content showed the highest value of London dispersive component, $W_A\;^L$, in work of adhesion, resulting from improving the interfacial adhesion force among fibers, filler, and matrix in this system.

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Adsorption and Oxidation Reaction Rate of $SO_2$ in Slurries of Activated Carbon (활성탄 슬러리를 이용한 $SO_2$ 가스의 흡착 및 산화반응 속도)

  • 최용택;신창섭;이태희
    • Journal of Korean Society for Atmospheric Environment
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    • v.3 no.1
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    • pp.41-46
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    • 1987
  • Adsorption and reaction studies were made for the catalytic oxidation in aqueous slurries of activated carbon at room temperature and atmospheric pressure. In order to analyze the reaction rate, the mechanism was assumed by the steps of nonhomogeneous catalytic reaction. The experimental result show that oxidation rate was controlled by the reaction between adsorbed molecular oxygen and sulfur dioxide on the catalyst surface. Ar room temperature, the equat5ion of reaction rate was given as $ro_2 = 2.49 \times 10^{-7} P_O_2^{0.604}$.

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