• Title/Summary/Keyword: V5.2

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$V_2O_5$가 코팅된 Li-Mn spinel의 합성과 전기화학적 특성

  • Kim, Jun-Il;Lee, Jae-Won;No, Gwang-Cheol;Park, Seon-Min;Seon, Yang-Guk
    • Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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    • 2009.11a
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    • pp.268-268
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    • 2009
  • Li-Mn spinel의 고온수영 특성을 향상을 위해 졸-겔법으로 $V_2O_5$를 Li-Mn spinel 표면에 코팅을 하였다. $V_2O_5$의 코팅양은 1, 3, 5wt%로 조절하여 코팅 양에 따른 특성변화를 조사하였다. XRD분석결과 $V_2O_5$가 코팅된 Li-Mn spinel을 $400^{\circ}C$에서 열처리시 $Mn(VO_3)_2$가 생성되는 것을 확인하였다. 충방전 테스트결과, 고온에서 $V_2O_5$를 코팅한 Li-Mn spinel이 우수한 수명을 나타냈다. 하지만 코팅량이 1wt%까지는 용량의 변화가 거의 없었고, 5wt% 코팅시 현격히 용량이 감소하였다.

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Benzyl Alcohol Oxidation over H5PMo10V2O40 Catalyst Chemically Immobilized on Sulfur-containing Mesoporous Carbon (황이 포함된 중형기공성 탄소에 화학적으로 고정화된 H5PMo10V2O40 촉매 상에서 Benzyl Alcohol 산화반응)

  • Gim, Min Yeong;Kang, Tae Hun;Choi, Jung Ho;Song, In Kyu
    • Korean Chemical Engineering Research
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    • v.54 no.3
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    • pp.419-424
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    • 2016
  • $H_5PMo_{10}V_2O_{40}$ ($PMo_{10}V_2$) catalyst chemically immobilized on sulfur-containing mesoporous carbon (S-MC) was prepared, and it was applied to the benzyl alcohol oxidation reaction. S-MC was synthesized by a templating method using SBA-15 and p-toluenesulfonic acid as a templating agent and a carbon precursor, respectively. S-MC was then modified to have a positive charge, and thus, to provide sites for the immobilization of $PMo_{10}V_2$. By taking advantage of the overall negative charge of $[PMo_{10}V_2O4_{40}]^{5-}$, $PMo_{10}V_2$ catalyst was immobilized on the S-MC support as a charge matching component. It was revealed that $PMo_{10}V_2$ species were finely and molecularly dispersed on the S-MC via chemical immobilization. In the vapor-phase oxidation of benzyl alcohol, $PMo_{10}V_2$/S-MC catalyst showed higher conversion of benzyl alcohol and higher yield for benzaldehyde and benzoic acid than unsupported $PMo_{10}V_2$ catalyst. The enhanced catalytic performance of $PMo_{10}V_2$/S-MC was due to fine dispersion of $PMo_{10}V_2$ species on the S-MC via chemical immobilization.

Selective Catalytic Oxidation of Hydrogen Sulfide Using $V_{2}O_{5}-TiO_2$ Catalyst Prepared by Nonhydrolytic Sol-Gel Method (비가수분해 솔-젤법으로 제조한 $V_{2}O_{5}-TiO_2$ 촉매를 이용한 황화수소의 선택 산화반응)

  • Kim, Sang-Yun;Cho, Dal-Rae;Park, Dae-Won
    • Clean Technology
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    • v.14 no.3
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    • pp.204-210
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    • 2008
  • A series of $V_{2}O_{5}-TiO_2$ xerogel catalysts were prepared by nonhydrolytic sol-gel method and analysed by various characterization techniques. These catalysts showed much higher surface areas and total pore volumes than conventional V$V_{2}O_{5}-TiO_2$ xerogel and impregnated $V_{2}O_{5}/TiO_2$ catalysts. It was found that the textural property of $V_{2}O_{5}-TiO_2$ material varies with the method and conditions of synthesis. Surface vanadates and $TiO_2$ anatase phase are the crucial factors to obtain high catalytic activities. The selective oxidation of hydrogen sulfide in the presence of excess water and ammonia was studied over these catalysts. Xerogel catalysts prepared by non-hydrolytic sol-gel method showed very high conversion of $H_{2}S$ without harmful emission of $SO_2$. The highest catalytic activity shown by these $V_{2}O_{5}-TiO_2$ catalysts may be due to their high surface area and good dispersion of vanadia species in the titania matrix.

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Investigation of $xV_2O_5-B_2O_3$ and $xV_2O_5-B_2O_3-yNa_3O$ Glasses by $^{11}B MAS$ NMR

  • Kim, Sun-ha;Han, Oc-Hee;Kang, Jae-Pil
    • Journal of the Korean Magnetic Resonance Society
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    • v.9 no.1
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    • pp.61-66
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    • 2005
  • $^{11}B MAS NMR$ spectra of binary glass system $xV_2O5-B_2O_3$ and ternary glass system $xV_2O5-B_2O_3-yNa_2O$ (x = $V_2O_5 mol%/$B_2O_3$ mol%, y = $Na_2O$ mol$/$B_2O_3$ mol%) were acquired. $BO_3$ units are dominant components in the spectra of $xV_2O_5-B_2O_3$glass systems while both $BO_3$ and $BO_4$ unit appear in comparable amounts in the spectra of $xV_2O_5-B_2O_3-yNa_2O$ glass systems. More $BO_3$ units were monitored for higher $V_2O_5$ contents while more $BO_4$ unit for higher $Na_2O$ contents. Quadrupole parameters such as $e^2qQ$ and $\eta$ obtained form spectral simulation indicate that $e^2qQ$ has a maximum value at x = y 1 and $\eta$ decreases and increases as x or y grows, respectively. Our results suggest that $V_2O_5$ and $Na_2O$ play opposite roles in the ternary glasses.

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V2O5 Embedded All Transparent Metal Oxide Photoelectric Device (V2O5 기반의 금속 산화물 투명 광전소자)

  • Kim, Sangyun;Choi, Yourim;Lee, Gyeong-Nam;Kim, Joondong
    • The Transactions of The Korean Institute of Electrical Engineers
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    • v.67 no.6
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    • pp.789-793
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    • 2018
  • All transparent metal oxide photoelectric device based on $V_2O_5$ was fabricated with structure of $V_2O_5/ZnO/ITO$ by magnetron sputtering system. $V_2O_5$ was deposited by reactive sputtering system with 4 inch vanadium target (purity 99.99%). In order to achieve p-n junction, p-type $V_2O_5$ was deposited onto the n-type ZnO layer. The ITO (indium tin oxide) was applied as the electron transporting layer for effective collection of the photo-induced electrons. Electrical and optical properties were analyzed. The Mott-Schottky analysis was applied to investigate the energy band diagram through the metal oxide layers. The $V_2O_5/ZnO/ITO$ photoelectric device has a rectifying ratio of 99.25 and photoresponse ratios of 1.6, 4.88 and 2.68 under different wavelength light illumination of 455 nm, 560 nm and 740 nm. Superior optical properties were realized with the high transmittance of average 70 % for visible light range. Transparent $V_2O_5$ layer absorbs the short wavelength light efficiently while passing the visible light. This research may provide a route for all-transparent photoelectric devices based on the adoption of the emerging p-type $V_2O_5$ metal oxide layer.

Activity of $V_2O_5-WO_3/TiO_2$-based SCR Catalyst for the Oxidation of Gas-phase Elemental Mercury ($V_2O_5-WO_3/TiO_2$ 계 SCR 촉매의 가스상 원소수은 산화 활성)

  • Hong, Hyun-Jo;Ham, Sung-Won
    • Clean Technology
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    • v.17 no.4
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    • pp.370-378
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    • 2011
  • Catalytic activity of $V_2O_5-WO_3/TiO_2$-based SCR catalyst was examined for the oxidation of gas-phase elemental mercury to oxidized mercury. Mercury species was not detected on the commercial SCR catalyst after the oxidation reaction of elemental mercury, regadless of the presence of HCl acting as oxidant and the reaction conditions. This suggests that elemental mercury oxidation by HCl could occur via a Eley-Rideal mechanism with gas phase or weakly-bound mercury on the surface of $V_2O_5-WO_3/TiO_2$ SCR catalyst. The activity for mercury oxidation was significantly increased with the increase of $V_2O_5$ loading, which indicates that $V_2O_5$ is the active site. However, turnover frequency for mercury oxidation was decreased with the increase of $V_2O_5$ loading, indicating the activity for mercury oxidation was strongly dependent on the surface structure of vanadia species. The activity for oxidation of elemental mercury under SCR condition was much less than that under oxidation condition at the same HCl concentration and reaction temperature.

The Studies on the Thermal Resistant Properties of $WO_3/TiO_2$ and $V_2O_5-WO_3/TiO_2$ Catalysts for NOx Reduction of Flue Gases from Industrial Boiler and on Catalyst Surface Acid Characteristics (産業用 보일러의 燃燒 排가스 中 NOx 處理를 위한 SCR 用 $WO_3/TiO_2$$V_2O_5/TiO_2$ 觸媒들의 耐熱特性과 表面 酸特性에 關한 硏究)

  • 이중범;임상윤;정석진;성준용
    • Journal of Korean Society for Atmospheric Environment
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    • v.6 no.1
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    • pp.31-42
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    • 1990
  • In order to suggest an efficient catalyst systems for NOx reduction of flue gases from industrial boilers, $TiO_2$ supported $WO_3-V_2O_5, V_2O_5$ and $WS_2$ catalysts were tested for the performances of NOx reduction at high reactin temperature range (250-500$^\circ$C) using a simulated flue gas system. It was found that while the proposed $WO_3/TiO_2$ and $WO_3-V_2O_5/TiO_2$ catalysts showed a significant high NOx reduction efficiency at about 350-400$^\circ$C, the conventional commercial catalyst of $V_2O_5/TiO_2$ showed a significant drop in NOx reduction efficiency due to the excessive $NH_3$ oxidation. From the measurement of surface acidities of those catalysts, it was found that the acidity are well correlated with the activities of NOx reduction. The reason of high activity of $WO_3$ series catalysts at high reaction temperature seems due to the low value of surface excess oxygen compared with that of $V_2O_5/TiO_2$ seems equivalent to the acid site of that catalyst.

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Load of Soil Layers Established with Perlite (펄라이트로 조성된 토양층의 하중)

  • 이성기;류남형;허근영
    • Journal of the Korean Institute of Landscape Architecture
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    • v.30 no.1
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    • pp.87-95
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    • 2002
  • This study was carried out to investigate the load of soil layers affected by soil depth in artificial soil alone or in blends with Loam with various ratio. The artificial soils were perlite large grain, perlite small grain, and perlite small grains blended with Loam (sand 46%, silt 40%, clay 14%) at a ratio of 8:2, 6:4, 5:5 (v/v). The soil layers were divided into a planting layer and a well-drained layer, then the weight of each layer in the air-dried state and in the field capacity were determined. The data were subjected to correlation analysis, regression analysis, and paired samples t-test. The summarized results are as follows; 1) In the air-dried state, the regression equations of the well-drained layer weight(kg/m2) in perlite large grain, planting layer weight in perlite small grain, planting layer weight in perlite small grain biended with loam(8:2, v/v), perlite small grain blended with loam(6:4, v/v), and perlite small grain blended with loam(5:5, v/v) were; 1.65824*X+0.026, 1.52292*X-0.052, 3.21468*X+0.515, 6.17549*X+ 0.083, and 6.02100*X + 33.133, respectively, where X is soil depth measured in Centimeters. 2) In the field capacity, the regression equations of the well-drained layer weight(kg/m2) in perlite large grain, planting layer weight in perlite small grain, planting layer weight in perlite small grain blended with loam(8:2, v/v), perlite small grain blended with loam(6:4, v/v), and perlite small grain blended with loam(5:5, v/v) were 5.055*X - 2.006, 7.073*X + 100.008, 8.092*X + 116.676, 10.766*X + 100.112, and 10.974*X + 124.423, respectively, where X is the soil depth measured in Centimeters. 3) All of the equations mentioned above were statistically reliable and therefore easily applicable in practical business affairs.

Low operating voltage and long lifetime organic light-emitting diodes with vanadium oxide $(V_2O_5)$ doped hole transport layer

  • Yun, J.Y.;Noh, S.U.;Shin, Y.C.;Baek, H.I.;Lee, C.H.
    • 한국정보디스플레이학회:학술대회논문집
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    • 2006.08a
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    • pp.1038-1041
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    • 2006
  • We report low operating voltage and long lifetime organic light-emitting diodes (OLEDs) with a vanadium oxide $(V_2O_5)-doped$ N,N'-di(1-naphthyl)- N,N'-diphenylbenzidine $({\alpha}-NPD)$ layer between indium tin oxide and ${\alpha}-NPD$. At a luminance of $1000\;cd/m^2$, $V_2O_5$ doped ${\alpha}-NPD$ device shows a operation voltage of 5.1V, while the device without $V_2O_5$ shows 5.8V. The $V_2O_5$ doped $({\alpha}-NPD)$ device also shows a longer lifetime and smaller operation voltage variation over time. It is suggested that the improved device performance can be attributed to the higher hole-injection efficiency and stability of the $V_2O_5$ doped $({\alpha}-NPD)$ layer.

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Photoelectrochemical Converision with $SrTiO_3$ Ceramic Electrodes ($SrTiO_3$ 세라믹 전극에 의한 광전기 화학변환)

  • 윤기현;김태희
    • Journal of the Korean Ceramic Society
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    • v.22 no.3
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    • pp.19-24
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    • 1985
  • The phtoelectrochemical porperties of $Nb_2O_5$, $Sb_2O_3$ and $V_2O_5$ doped and pure $SrTiO_3$ ceramic electodes were investigated. Shapes of I-V and I-λ characteristics of the pure $SrTiO_3$ ceramic electrode are similar to those of SrTiO3 single crystal electorde ; the anodic current strats at -0.9V (vs. Ag/AgCI) in 1 N-NaOH aqueous solution and the photoresponse appears at a wavelength of about 390nm and the quantum efficiency is about 3.5% at wavelength of 390nm under 0.5V vs. Ag/AgCl. Photocurrents of $Nb_2O_5$, $Sb_2O_3$ and $V_2O_5$ doped electrodes and $V_2O_5$ doped ceramic electrode appears at wavelength of 390nm and 500nm respectively.

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