• 제목/요약/키워드: ${\gamma}-Al_2O_3$

검색결과 306건 처리시간 0.026초

Composition Dependence and Optical Properties of Polymethyl Methacrylate/Alumina Nanocomposite in the IR Region Determined by Kramers-Kronig Relation

  • Ghamari, Misagh;Ghasemifard, Mahdi
    • 한국세라믹학회지
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    • 제54권2호
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    • pp.102-107
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    • 2017
  • The dependence of the IR optical properties of PMMA/$Al_2O_3$ nanocomposite on the alumina content was investigated in the wavelength range of $3500-2800cm^{-1}$. The samples were prepared via emulsion polymerization technique using oleic acid as a coupling agent. Grafting density calculations were carried out by means of elemental analysis CHN to yield the best coupling agent content. FTIR analysis confirmed the existence of a chemical bond between aluminum oxide and oleic acid. The outcomes of XRD analyses showed the presence of cubic gamma aluminum oxide in the nanocomposite, in contrast to the amorphous nature of PMMA. TEM images showed the core-shell morphology of the particles other than pristine PMMA. Optical constants of the nanocomposite were calculated based on FTIR spectra and the Kramers-Kronig equations. The presence of nano alumina modified some of the optical indexes in IR region.

X-ray/gamma radiation shielding properties of Aluminium-Bariume-Zinc Oxide nanoparticles synthesized via low temperature solution combustion method

  • K.V. Sathish;K.N. Sridhar;L. Seenappa;H.C. Manjunatha;Y.S. Vidya;B. Chinnappa Reddy;S. Manjunatha;A.N. Santhosh;R. Munirathnam;Alfred Cecil Raj;P.S. Damodara Gupta;B.M. Sankarshan
    • Nuclear Engineering and Technology
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    • 제55권5호
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    • pp.1519-1526
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    • 2023
  • For the first time Aluminium-BariumeZinc oxide nanocomposite (ZABONC) was synthesized by solution combustion method where calcination was carried out at low temperatures (600℃) to study the electromagnetic (EM) (X/γ) radiation shielding properties. Further for characterization purpose standard techniques like PXRD, SEM, UV-VISIBLE, FTIR were used to find phase purity, functional groups, surface morphology, and to do structural analysis and energy band gap determination. The PXRD pattern shows (hkl) planes corresponding to spinel cubic phase of ZnAl2O4, cubic Ba(NO3)2, α and γ phase of Al2O3 which clearly confirms the formation of complex nano composite. From SEM histogram mean size of nano particles was calculated and is in the order of 17 nm. Wood and Tauc's relation direct energy band gap calculation gives energy gap of 2.9 eV. In addition, EM (X/γ) shielding properties were measured and compared with the theoretical ones using standard procedures (NaI (Tl) detector and multi channel analyzer MCA). For energy above 356 keV the measured shielding parameters agree well with the theory, while below this value slight deviation is observed, due to the influence of atomic/crystallite size of the ZABONC. Hence synthesized ZABONC can be used as a shielding material in EM (X/γ) radiation shielding.

유독성 유기용매의 촉매산화공정에서 혼합조성에 따른 간섭효과 (Inhibition Effects of Toxic Solvent Mixture in Catalytic Oxidation Process)

  • 이승범;김원일;홍인권;김형진
    • 환경위생공학
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    • 제16권3호
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    • pp.72-79
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    • 2001
  • The selective catalytic oxidation of toxic aromatic solvents (benzene, toluene, ethylbenzene, and styrene) and their mixtures were studied on a $Pt/{\;}{\gamma}-Al_2O_3$ catalyst at temperature ranging from $160~350^{\circ}C$. The deep conversion of aromatic solvents was increased as the inlet concentration was decreased and the reaction temperature was increased. The reactivity increases in order benzene > toluene > ethylbenzene > styrene. In mixture, remarkable effects on reaction rate and selectivity have been evidence ; the strongest inhibition effect is shown by styrene and increase in a reverse order with respect to that of reactivity. The inhibition effect was increased in order styrene > ethylbenzene > toluzene > benzene. This trend is due to the competition adsorption between the two or three reactants on the oxidized catalyst. Also, the deep conversion change of benzene was a small in tertiary mixtures(including of benzene and styrene) comparing with conversion characteristics of binary mixture with styrene. This result was due to small concentration of styrene. which had very strong inhibition effect.

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Modification of H-ZSM-5 and γ-Alumina with Formaldehyde and Its Application to the Synthesis of Dimethyl Ether from Syn-gas

  • Joo, Oh-Shim;Jung, Kwang-Deog;Han, Sung-Hwan
    • Bulletin of the Korean Chemical Society
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    • 제23권8호
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    • pp.1103-1105
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    • 2002
  • H-ZSM-5 and γ-alumina were treated with formaldehyde and sodium carbonate. The treatment increased the amounts of weak acid sites, removing strong acid sites. The maximum temperature of weak acid sites in their ammonia TPD spectra shifted in the direction of high temperature. The modified H-ZSM-5 and g-alumina were mixed with the methanol synthesis catalyst to perform dimethyl ether synthesis from syn-gas. The modified catalysts showed better selectivity to dimethyl ether, minimizing the reforming reaction to carbon dioxide. The maximum yield of 53.3% to dimethyl ether was achieved under the reaction conditions of 54.4 atm, 523 K, and the feed rate of 4500 Lhr-1 .gcat-1.

수첨탈황과 탈질반응에서 Thiophene과 Pyridine의 상호영향과 그 속도론적 해석 (Interactions between Hydrodesulfurization of Thiophene and Hydrodenitrogenation of Pyridine and the Kinetic Analysis)

  • 박종희;한창훈;김경림
    • 한국대기환경학회지
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    • 제4권1호
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    • pp.13-22
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    • 1988
  • Interactions between hydrodesulfurization of thiophene and hydrodenitrogenation of pyridine and the kinetic analysis were studied over $Ni-W/\gamma-Al_2O_3$ catalysts and this study was made at temperatures ranging from 473-673 K and at total pressures ranging from 10-25 $\times 10^5$ Pa. Hydrodesulfurization of thiophene was inhibited by presence of pyridine at all temperatures studied, and the rate of pyridine hydrodenitrogenation was slower than that of thiophene hydrodesulfurization in the operating conditions. Pyridine hydrodenitrogenation was also inhibited by the presence of thiophene at low temperatures but was enhanced by the thiophene at temperatures higher than 613K. Thiophene reaction rate was determined by multiple linear regression analysis using Langmuir-Hinshelwood-Hougen-Watson model and the result was given to be $r = kP_T^p_H/(1+K_Tp_T+K_Pp_P)^2$. At each temperature, reaction rate constants and absorption equilibrium equilibrium constants were determined and the activation energy was 12.98 kcal/gmol from Arrhenius plot.

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시멘트와 Fe(II)을 이용한 환원성 탈염소화반응의 유효반응성분 규명 (Identification of Active Agents for Reductive Dechlorination in Cement/Fe(II) Systems)

  • 김홍석;이유정;김하얀;황인성
    • 한국지하수토양환경학회지:지하수토양환경
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    • 제11권6호
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    • pp.35-42
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    • 2006
  • 본 연구는 시멘트/Fe(II) 시스템에서 TCE의 환원성 탈염소화에 관여하는 유효반응성분을 규명하기 위하여 수행되었다. 먼저 시멘트 자체에 존재하거나 혹은 그 수화물에 존재하는 성분을 다량 함유하고 있는 hematite(${\alpha}-Fe_2O_3$), lepidocrocite(${\gamma}$-FeOOH), akaganeite(${\beta}$-FeOOH), ettringite($Ca_6Al_2(SO_4)_3(OH)_{12}$)를 대상으로 TCE 분해실험을 수행하여 이러한 물질이 시멘트/Fe(II) 시스템에서 탈염소반응에 관여할 수 있는지 고찰한 결과, hematite가 잠재적 유효반응성분으로 선정되었다. 각 시스템의 반응속도상수를 비교해 본 결과 200 mM Fe(II)에 hematite와 CaO를 1 : 4(몰비)로 주입한 시스템($k\;=\;0.637\;day^{-1}$)이 기존의 cement와 Fe(II)을 이용한 경우($k\;=\;0.645\;day^{-1}$)와 가장 비슷한 동력학적 분해경향을 보인다는 것을 알 수 있었다. 처음에 pH 조절이 주목적으로 주입되었던 CaO 역시 분해반응에서 중요한 역할을 담당하는 것으로 나타났는데, CaO 첨가량이 증가할수록 hematite/CaO/Fe(II) 시스템의 분해능은 증가하다가 CaO 양이 일정 수준에 다다르면 증가세가 둔화되는 경향을 보여 주었다. SEM(Scanning Electron Microscopy) 분석을 통해서는 hematite/CaO/Fe(II) 시스템 내에서 분해능이 커질수록 육각형 판상의 결정이 새롭게 형성된다는 것을 확인 할 수 있었으며 이 결정은 portlandite, green rust($SO_4$), Friedel's salt 등일 가능성이 높은 것으로 판단되었다. 그리고 동일 시료의 XRD(X-Ray Diffraction) 분석을 통해서는 hematite, magnetite/maghemite, green rust($SO_4$)의 존재를 확인할 수 있었다. SEM 및 XRD 분석에서 공통적으로 나타나는 green rust($SO_4$)가 유효반응성분일 가능성이 높다고 판단되었다.

Electric Field Effect on Nanochannel Formation in Electrochemical Porous Structures of Alumina

  • Kim, Keun-Joo;Choi, Jae-Ho;Lee, Jung-Tack
    • Transactions on Electrical and Electronic Materials
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    • 제11권5호
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    • pp.230-233
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    • 2010
  • The authors investigated the anodization mechanism of aluminum in an oxalic acid solution, and the electrochemical reaction is very unique for pore formation via the dissolution process, which is very dependent on the surface geometry in nanoporous alumina templates. The cross-sectional nanochannels showed that the geometrical curvature of the initial surface can cause the branching of nanochannels to be adjusted in volume occupancy to be direct to the electric field normal to the surface. The nanoporous alumina with the crystalline $\gamma-Al_2O_3$ phase showed hexagonal ordering at a voltage of 40 V, with a nanohole distance of 102 nm from the charge density oscillation of the oxalic acid solution.

휘발성 유기화합물(VOCs)의 촉매산화 전환에서 결합구조의 영향 및 속도특성 (Influence of VOCs Structure on Catalytic Oxidation Kinetics)

  • 이승범;윤용수;홍인권;이재동
    • 환경위생공학
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    • 제15권4호
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    • pp.44-51
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    • 2000
  • The reactivity of a range of volatile organic compounds with differing functional groups observed over 0.5% $Pt/{\gamma}-Al_2O_3$ catalyst. In general, the reactivity pattern observed was alcohols > aromatics > ketones > cycloalkane > alkanes. The deep conversion was increased as reaction temperature was increased. A correlation was found between the reactivity of the individual and the strength of the weakest C-Hbond in structure. The conversion of volatile organic compounds increases in order methanol > benzene > cyclohexane > MEK > n-hexane. That is the effect of differences in total dissociation energy. An apparent zeroth-order kinetics with respect to inlet concentration have been observed. A simple multicomponent model based on two-stage redox model made reasonably good predictions of conversion over the range of parameters studied. thus, the catalytic process was suggested as the new VOCs control technology.

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방향족 유기용매의 촉매산화공정에서 이성분계 혼합물의 속도특성 예측 (Kinetics Prediction of Binary Aromatic Solvent Mixtures in Catalytic Oxidation Process)

  • 이승범;윤용수;홍인권;이재동
    • 환경위생공학
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    • 제16권1호
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    • pp.66-71
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    • 2001
  • The objective of this study was to depict the kinetic behavior of the platinum catalyst for the deep oxidation of aromatic solvents and their binary mixtures. The oxidation kinetics of aromatic solvents, which were benzene, toluene and m-xylene, was studied on a 0.5% $Pt/{\gamma}-Al_2O_3$ catalyst. Deep oxidation of binary mixtures, which were 1:1 in volume, was carried out and the inlet concentration was controlled in the range of 133 and 333ppmv. An approach based on the two-stage redox model was used to analysis the results. The deep oxidation conversion of aromatic solvents was inversely proportional to inlet concentration in plug flow reactor. This trend is due to the zeroth-order kinetics with respect to inlet concentration. The kinetic parameters of multicomponent model were independently evaluated from the single compound oxidation experiments. A simple multicomponent model based on two-stage redox rate model made reasonably good predictions of conversion over the range of parameters studied.

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Comparison of Adsorption Properties of Adsorbates on Pt(111) and Pt(111)/$\gamma-Al_2O_3$ Surface in the Ethylene Hydrogenation Reaction : MO-Theory

  • 조상준;박상문;박동호;허도성
    • Bulletin of the Korean Chemical Society
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    • 제19권7호
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    • pp.733-737
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    • 1998
  • Using an atom superposition and electron delocalization molecular orbital (ASED-MO) method, we have compared adsorption properties of adsorbates on the Pt(Ill) surface with the Pt(lll)/γ-Al203 surface in the ethylene hydrogenation reaction. In two-layer thick model systems, the calculated activation energy of the hydrogenation by the surface platinum hydride is equal to the energy by the hydride over supported platinum/γ-alumina. The transition structure on platinum is very close to the structure on the supported platinum/γ-alumina surface. Hydrogenation by the surface hydride on platinum can take place easily because the activation energy is about 0.5 eV less than hydrogenation by ethylidene. On supported platinum/,y-alumina the activation energy of the hydride mechanism is about 0.61 eV less than that of ethylidene mechanism. In one-layer thick model systems, the activation energy of hydrogenation by ethylidene is about 0.13 eV less than the activation energy of hydride reaction. The calculated activation energy by the hydride over the supported platinum y-alumina is 0. 24 eV higher than the platinum surface. We have found from this result that the catalytic properties of one-layer thick model systems have been influenced by the support but the two-layer thick model systems have not been influenced by the support.