• Title/Summary/Keyword: 황의만

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The Kientic Study of Ozone$(O_3)$ with Sulfur Trioxide#(SO_3)$ in the Gas Phase (기체상태에서의 오존$(O_3)$과 삼산화황$(SO_3)$의 반응연구)

  • Kwon Young Sik
    • Journal of the Korean Chemical Society
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    • v.36 no.5
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    • pp.644-651
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    • 1992
  • The kinetics of the gas phase reaction of ozone(∼0.5 torr) with sulfur trioxide was investigated in the range of 6∼12 torr pressure at 69∼150${\circ}C$. The reaction rate of ozone with sulfur trioxide was faster than the reaction rate of $O_3 in the presence of CO_2 alone. No evidence for a molecular reaction of O_3 with SO_3 was found and the faster rate is probably due to impurity (HX) from the SO_3 reactant which gives rise to a chain reaction initiated by O_3 + HX → OH + O_2 + X and also SO_3 has a larger collision diameter, which may be attributed to the O3 thermal decomposition more feasibly. The proposed experimental law [-d(O_3)/dt] = k_a(SO_3)(O_3) + k_b(O_3)^{3/2} gives a rate constant ka(M-1 s-1) = (1.55 {\pm} 0.67) {\times} 105 e-{(9.27 0{\pm}0.43)kcal/RT}.$

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Effect of the Sulfur Removal in Manufacturing Pt/C Electrocatalysts on the Performance of Phosphoric Acid Fuel Cell (인산형 연료전지용 백금촉매제조에서 황의 제거에 따른 전극 성능)

  • Shim, Jae-Cheol;Lee, Kyung-Jik;Lee, Ju-Seong
    • Applied Chemistry for Engineering
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    • v.9 no.4
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    • pp.486-490
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    • 1998
  • Pt/C powder which was used as electrocatalyst in a Phosphoric Acid Fuel Cell(PAFC) was fabricated by colloid method. It was reported that the sulfur from reductant, $Na_2S_2O_4$, worked as a poison against catalyst during long term operation. To remove these sulfurs, we try to treat Pt/C powder by three different methods. First, we tried to remove the sulfur according to temperature and time in $H_2$ atmosphere. As the heat treatment temperature is raised up, the effect of the removal is increased but the electrode performance is decreased because of the growth of Pt particle size. The optimal heat treatment temperature is $400^{\circ}C$, the size of Pt particle is approximately $35{\sim}40{\AA}$ and the electrode performance is $360mA/cm^2$ at 0.7 V. At $400^{\circ}C$, even though the time of heat treatment is extended, size of Pt, amounts of remaining sulfur and electrode performance is almost constant. Secondly, when we removed in a crucible at $900^{\circ}C$ the removal of the sulfur was not better, but the size of Pt particle, approximately $80{\AA}$, was smaller than that of heat treatment in $H_2$ atmosphere at $900^{\circ}C$. Lastly we treated with solvents such as acetone, benzene, and carbon disulfide. It was observed that sulfur components were removed partly by extraction with solvents, the electrode performances were similar each other.

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Selective Oxidation of Hydrogen Sulfide Containing Ammonia and Water Using Fe2O3/SiO2 Catalyst (Fe2O3/SiO2 촉매 상에서 물과 암모니아가 함께 존재하는 황화수소의 선택적 산화 반응)

  • Kim, Moon-Il;Lee, Gu-Hwa;Chun, Sung-Woo;Park, Dae-Won
    • Korean Chemical Engineering Research
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    • v.50 no.3
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    • pp.398-402
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    • 2012
  • The catalytic performance of some metal oxides in the vapor phase selective oxidation of $H_2S$ in the stream containing ammonia and water was investigated. Among the catalysts tested $Fe_2O_3/SiO_2$ was the most promising catalyst for practical application. It showed higher than 90% $H_2S$ conversion and very small amount of $SO_2$ emission over a temperature range of $240{\sim}280^{\circ}C$. The effects of reaction temperature, $O_2/H_2S$ ratio, amount of ammonia and water vapor on the catalytic activity of $Fe_2O_3/SiO_2$ were discussed to better understand the reaction mechanism. The $H_2S$ conversion showed a maximum at $260^{\circ}C$ and it decreased with increasing temperature over $280^{\circ}C$. With an increase of $O_2/H_2S$ ratio from 0.5 to 4, the conversion was slightly increased, but the selectivity to elemental sulfur was remarkably decreased. The increase of ammonia amount favored the conversion and the selectivity to elemental sulfur with a decrease in $SO_2$ production. The presence of water vapor decreased both the activity and the selectivity to sulfur, but increased the ATS selectivity.

Leaching of Metal Sulfides and the Stability of Reaction Intermediates (황화광의 침출반응 및 중간생성물의 안정도)

  • Lee, Man Seung;Choi, Seung Hoon
    • Resources Recycling
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    • v.27 no.3
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    • pp.3-7
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    • 2018
  • Development of extractive metallurgical processes for metal sulfides has become of importance owing to the depletion of oxide ores with rich metal contents. Most of the leaching reactions of metal sulfides is electrochemical reaction and can be classified as $H_2S$, S, and ${SO_4}^{2-}$ evolution type. The acidity of leaching solution and the presence and concentration of an oxidizing agent affect the formation of reaction intermediates containing sulfur. Frost diagram of sulfuroxoanion indicates that the oxoanions with higher oxidation number are more thermodynamically stable in the presence of oxidizing agents.

A study on the dielectric dispersion of vulcanized natural rubber (가황에 의한 천연고무의 유전분산에 관한연구)

  • Lee, Joon-Ung;Kim, Hak-Ju
    • Elastomers and Composites
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    • v.18 no.2
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    • pp.51-59
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    • 1983
  • The dielectric properties of polymers are very important when investigating the molecular structure of polymers. The characteristics of the dielectric absorption in vulcanized natural rubber were studied in frequency ranging from 10[KHz] to 32[MHz] at the temperature of 25[$^{\circ}C$]. As a result of the study, it has been confirmed that natural rubber vulcanized below 4phr leads to two kinds of dielectric losses due to the interfacial polarization and the dipole polarization by sulfur, and of above 7[%] was only a loss due to the dipole polarization by sulfur. Futhermore, the dielectric loss maximum $tan{\delta}$ spectrum, removed to the low frequency in accordance with increasing sulfur, depends greatly on sulfur. The volume resistivity of $10^{7}{\sim}10^{11}[{\Omega}{\cdot}cm}]$, regardless of whether the crosslinking of rubber is weakened by sulfur, was observed.

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Removal of H2S by Selective Catalytic Oxidation II. Selective Oxidation of H2S on TiO2/SiO2 Catalysts (선택적 촉매 산화 반응에 의한 황화 수소의 제거 II. TiO2/SiO2 촉매 상에서 황화 수소의 선택적 산화 반응)

  • Chun, S.W.;Park, D.W.;Woo, H.C.;Hong, S.S.;Chung, J.S.
    • Applied Chemistry for Engineering
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    • v.7 no.4
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    • pp.645-652
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    • 1996
  • Selective catalytic oxidation of $H_2S$ to elemental sulfur using $TiO_2/SiO_2$ catalysts was investigated in this study. The reaction test with pure $TiS_2$ and $Ti(SO_4)_2$ and cyclic temperature operation revealed that $TiO_2$ had a good resistance to sulfation and sulfidation, which are known as the main cause of catalytic deactivation in sulfur recovery process. With the increase of $TiO_2$ loading amount in $TiO_2/SiO_2$ catalysts, the conversion of $H_2S$ increased and the selectivity of elemental sulfur was very slightly decreased. As the ratio of $O_2/H_2S$ increased, the selectivity to elemental sulfur was drastically decreased. In the presence of 10 vol.% water vapor to a stoichiometric mixture of $H_2S$ and $O_2$($H_2S$= 5 vol.% O=2.5 vol.% ), both activity and selectivity of 10 wt.% $TiO_2/SiO_2$ catalyst are decreased, but it still showed more than 80% of sulfur yield.

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