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HYDRODESULFURIZATION OF DIBENZOTHIOPHENE OVER SUPPORTED AND UNSUPPORTED MOLYBDENUM CARBIDE CATALYSTS
Kim, Kyung Lim,Park, Hea Kyung,Kim, Du Soung 한국화학공학회 1998 Korean Journal of Chemical Engineering Vol.15 No.6
A series of γ Al₂O₃ supported molybdenum carbides [carbided Mo/γ-A1₂O₃ (MCS), Co-Mo/γ-A1₂O₃ (CMCS), and Ni-Mo/γ-A1₂O₃ (NMCS)] and unsupported molybdenum carbide (MCUS) were prepared by the temperature-programmed carburization of their corresponding molybdenum nitrides with 20 % CN₄/H₂. XRD and SEM studies show that unsupported molybdenum carbide catalyst possesses a typical crystalline Mo₂C (FCC structure), while supported molybdenum carbide catalysts possess highly dispersed surface molybdenum carbide species on an alumina oxide support. The results of dibenzothiophene (DBT) hydrodesulfurization over molybdenum carbide catalysts show that the reactivity is strongly dependent on the type of catalyst. Supported molybdenum carbide catalysts possess a higher reactivity than the unsupported molybdenum carbide catalyst. In addition, Co or Ni promoted, supported molybdenum carbide catalyst possesses a higher reactivity than the unpromoted, supported molybdenum carbide catalyst. The reactivity, which is also dependent on the reaction conditions, increases with increasing reaction temperature and pressure and contact time. The CO uptakes of the molybdenum carbide catalysts correlate well with overall activity (total rate) for DBT hydrudesulfurization. The major reaction product is biphenyl, with cyclohexylbenzene next in abundance regardless of the type of catalysts and reaction conditions. It was also found that the molybdenum carbide catalysts exhibit stable initial reactivity due to the stable and weak acidic characteristics of these catalysts.
Ho-Ik Du,Soung-Ouk Heo,Tae-Min Kim,Byoung-Sung Han,Ji-Hoon Lee,Sung-Chae Yang IEEE 2014 IEEE transactions on applied superconductivity Vol.24 No.3
<P>This study examined the effects of the turn ratio and direction of two serially connected coils on the current-limiting performance of YBCO thin-film wires with different stabilization layers. Three YBCO thin-film wires with different stabilization layers were used to manufacture current-limiting elements, and their current-limiting performance was evaluated. The test equipment that consisted of two serially connected coils was connected to the current-limiting superconducting elements that were manufactured with YBCO thin-film wires. Finally, the current-limiting characteristic of each current-limiting element and its operation as a superconducting fault current limiter (SFCL) were examined after the turn ratio and direction of the two coils were varied. The current-limiting characteristic of the current-limiting element and its operation as a SFCL were verified the resistance generation tendency, current-limiting ratio, and response time as indicator.</P>
ZrO<sub>2</sub>·SO<sub>4</sub><sup>2-</sup>에 담지된 백금촉매의 저온산화반응성에 대한 연구
김기석,이태정,김병삼,김두성,Kim, Kiseok,Lee, Tae Jung,Kim, Byoung Sam,Kim, Du Soung 한국공업화학회 1998 공업화학 Vol.9 No.1
초강산 담체인 $ZrO_2$ $SO_4{^{2-}}$에 담지된 백금촉매(0.2, 0.5wt% Pt)의 저온 산화반응성을 cyclohexane의 완전산화반응에 대하여 조사 하였다. 충전층 관형반응기에서 반응물질의 전화율로 측정된 촉매활성은 촉매의 산성도와 비표면적에 비례하여 증가하였다 : $Pt/ZrO_2$ $SO_4{^{2-}}$ 촉매 제조과정에서 K(potassium)를 첨가하여 촉매의 산성도와 비표면적을 감소시켰을 때 촉매활성은 K첨가량에 비례하여 감소하였다. 또한 $Pt/ZrO_2$ $SO_4{^{2-}}$촉매는 훨씬 더 큰 비표면적을 가진 $Pt/SiO_2$, 또는 $Pt/Al_2O_3$촉매보다 뛰어난 활성을 보였다 : l5,000ppm cyclohexane농도와 $18,000hr^{-1}$공간속도를 가진 반응물질 흐름을 $250^{\circ}C$에서 0.2wt% $Pt/ZrO_2$ $SO_4{^{2-}}$촉매를 사용하여 전화시킨 결과 96%의 cyclohexane전화율을 보인 반면, 같은 반응조건 하에서 0.2wt% $Pt/SiO_2$와 0.2wt% $Pt/Al_2O_3$촉매는 각각 83%와 79%의 cyclohexane전화율을 보였다. Reactivity of Pt catalysts(0.2, 0.5 wt% Pt) supported on solid super acid, $ZrO_2$ $SO_4{^{2-}}$ for low-temperature oxidation was investigated for complete oxidation of cyclohexane. Catalytic activity measured as reactant conversion in a packed-bed tubular reactor increased in accordance with the acidity and specific surface area of the catalyst activity and specific surface area of $Pt/ZrO_2$ $SO_4{^{2-}}$ catalyst were diminished by adding potassium during catalyst preparation. the catalyst activity decreased in accordance with the amount of potassium added. In addition, $Pt/ZrO_2$ $SO_4{^{2-}}$ catalyst exhibited an activity greater than that of a $Pt/SiO_2$ or $Pt/Al_2O_3$ catalyst possessing much larger specific surface area at $250^{\circ}C$ for the reactant stream of 15.000 ppm cyclohexane concentration and $18,000hr^{-1}$ space velocity, a cyclohexane conversion as high as 96% was obtained over 0.2 wt% $Pt/ZrO_2$ $SO_4{^{2-}}$, whereas cyclohexane conversions over 0.2 wt% $Pt/SiO_2$ and 0.2 wt% $Pt/Al_2O_3$ were 83 and 79%, respectively.
사고전류 제한형 초전도케이블 제작을 위한 초전도 선재 선정에 관한 연구
허성욱,김태민,한병성,두호익,Heo, Soung-Ouk,Kim, Tae-Min,Han, Byung-Sung,Du, Ho-Ik 한국전기전자재료학회 2013 전기전자재료학회논문지 Vol.26 No.12
When an abnormal condition occurs due to a fault current at a consumer location where electricity is supplied through a high-capacity and high-$T_c$ superconducting(HTS) cable, the HTS cable would be damaged if there is no appropriate measure to protect it. Therefore, appropriate measures are needed to protect HTS cables. The fault-current-limiting HTS cable that was suggested in this study performs an ideal transport current function in normal operations and plays a role in limiting a fault current in abnormal operation (i.e., when a fault current is applied). It has a structure that facilitated its self-current-limiting ability through device change and reconfiguration in the existing HTS cable without extra switching equipment. To complete this structure, it is essential to investigate about the selection of the superconducting wire. Therefore, in this paper, HTS wire using two types of different stabilization layer is compared and examined the stability and current limiting properties under the existence of a fault current.
ZrO2 , SO42- 에 담지된 백금촉매의 저온산화반응성에 대한 연구
김기석,이태정,김병삼,김두성 ( Kiseok Kim,Tae Jung Lee,Byoung Sam Kim,Du Soung Kim ) 한국공업화학회 1998 공업화학 Vol.9 No.1
초강산 담체인 ZrO₂·SO₄^(2-)에 담지된 백금촉매(0.2, 0.5 wt% Pt)의 저온 산화반응성을 cyclohexane의 완전산화반응에 대하여 조사하였다. 충전층 관형반응기에서 반응물질의 전화율로 측정된 촉매활성은 촉매의 산성도와 비표면적에 비례하여 증가하였다: Pt/ZrO₂·SO₄^(2-) 촉매 제조과정에서 K(potassium)를 첨가하여 촉매의 산성도와 비표면적을 감소시켰을 때 촉매활성은 K첨가량에 비례하여 감소하였다. 또한 Pt/ZrO₂·SO₄^(2-) 촉매는 훨씬 더 큰 비표면적을 가진 Pt/SiO₂, 또는 Pt/Al₂O₃촉매보다 뛰어난 활성을 보였다 : 15,000ppm cyclohexane농도와 18,000hr^(-1)공간속도를 가진 반응물질 흐름을 250℃에서 0.2 wt% Pt/ZrO₂·SO₄^(2-)촉매를 사용하여 전화시킨 결과 96%의 cyclohexane전화율을 보인 반면, 같은 반응조건 하에서 0.2 wt% Pt/SiO₂와 0.2 wt% Pt/Al₂O₃촉매는 각각 83%와 79%의 cyclohexane전화율을 보였다. Reactivity of Pt catalysts(0.2, 0.5 wt% Pt) supported on solid super acid, ZrO₂·SO₄^(2-), for low-temperature oxidation was investigated for complete oxidation of cyclohexane. Catalytic activity measured as reactant conversion in a packed-bed tubular reactor increased in accordance with the acidity and specific surface area of the catalyst: as the acidity and specific surface area of Pt/ZrO₂·SO₄^(2-) catalyst were diminished by adding potassium during catalyst preparation, the catalyst activity decreased in accordance with the amount of potassium added. In addition, Pt/ZrO₂·SO₄^(2-) catalystexhibited an activity greater than that of a Pt/SiO₂ or Pt/Al₂O₃ catalyst possessing much larger specific surface area: at 250℃ for the reactant stream of 15,000ppm cyclohexane concentration and 18,000 hr^(-1) space velocity, a cyclohexane conversion as high as 96% was obtained over 0.2 wt% Pt/ZrO₂·SO₄^(2-), whereas cyclohexane conversions over 0.2 wt% Pt/SiO₂ and 0.2 wt% Pt/A1₂O₃were 83 and 79%, respectively.