• Title/Summary/Keyword: 실리카-알루미나

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Effect of Alumina on the Ion-Exchange Capacity of Porous Glasses (다공질유리의 이온교환성에 미치는 알루미나의 영향)

  • 김병호;이덕열;김성길
    • Journal of the Korean Ceramic Society
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    • v.25 no.3
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    • pp.251-260
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    • 1988
  • Ion-exchange porous glasses were prepared by heat treatment and subsequently hydro thermalor acid leaching treatment $10Li_2O$.$(90-x)B_2O_3$.$xSiO_2$ base glasses containing various amount of $Al_2O_3$ or $MoO_3$. It was investigated how the phase separation and the cation exchange capacity(CEC) were affected by the addition of $Al_2O_3$ or $MoO_3$. The optimum condition of phase separation in these glasses was about 48$0^{\circ}C$ for 10 hrs. The degree of phase separation was rapidly suppressed by the addition of $Al_2O_3$ up to 10 mol% and thereafter suppression effect was decreased. The maximum value of CEC, about 252meq/100g, was observed with the $1OLi_2O$.$45B_2O_3$.$45SiO_2+7.5Al_2O_3$ porous glass prepared by hydrothermal treatment and its mean pore radius was about 16.3A. The addition of $MoO_3$ accelerated phase separation and leaching rate. Looking at the remakable increment of pore diameter and pore volume of these porous glasses by the addition of $MoO_3$, the effect of $MoO_3$ may be ascribed to the lowering of silica concentration in the borate phase and to the forming of water-soluble complex with silica during the leaching treatment.

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A Study on Intermediate Layer for Palladium-Based Alloy Composite Membrane Fabrication (팔라듐 합금 복합막 제조를 위한 Intermediate Layer 연구)

  • Hwang, Yong-Mook;Kim, Kwang-Je;So, Won-Wook;Moon, Sang-Jin;Lee, Kwan-Young
    • Applied Chemistry for Engineering
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    • v.17 no.5
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    • pp.458-464
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    • 2006
  • The Pd-Ni-Ag alloy composite membrane using modified porous stainless steel (PSS) as a substrate was prepared by a electroless plating technique. In this work, we have introduced the intermediate layer between Pd-based alloy and a metal substrate. As an intermediate layer, the mixtures of nickel powder and inorganic sol such as $SiO_{2}$ sol, $Al_{2}O_{3}$ sol, and $TiO_{2}$ sol were used. The intermediate layers were coated onto a PSS substrate according to various membrane preparation conditions and then $N_{2}$ fluxes through the membranes with different intermediate layers were measured. The surface morphology of the intermediate layer in the mixture of nickel powder and inorganic sol was analyzed using scanning electron microscope (SEM). Finally, the Pd-Ni-Ag alloy composite membrane using the support coated with the mixture of nickel powder and silica as an intermediate layer was fabricated and then the gas permeances for $H_{2}$ and $N_{2}$ through the Pd-based membrane were investigated. The selectivity of $H_2/N_2$ was infinite and the $H_{2}$ flux was $1.39{\times}10^{-2}mol/m^2{\cdot}s$ at the temperature of $500^{\circ}C$ and trans-membrane pressure difference of 1 bar.

A Study on Changes in High-Temperature Microstructure of Coal Ash Applied as Cement Clinker Raw Material (시멘트 클링커 원료로서 적용한 석탄재의 고온 미세구조 변화 고찰)

  • Yoo, Dong-Woo;Im, Young-Jin;Kwon, Sung-Ku;Lee, Seok-Je
    • Journal of the Korean Recycled Construction Resources Institute
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    • v.10 no.3
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    • pp.211-218
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    • 2022
  • Coal ash is being considered as a source of silica and alumina for cement clinker. The purpose of this study was to investigate the effect on cement clinker sintering by confirming the high-temperature microstructural change according to the firing temperature in the cement clinker sintering process of coal ash. In the coal ash used as a raw material for cement clinker, the shape change of the particle surface was confirmed from the sintering tem perature of 950 ℃. The shape of the coal ash disappeared from the sintering temperature higher than 1250 ℃. It was confirmed that the Al and Fe components of the coal ash were converted to the cement interstitial phase at a temperature higher than 1350 ℃. In addition, the clinker using a large amount of coal ash as a raw material showed a low content of Lime and a high content of Belite in the sintering tem perature range of 1150~1200 ℃. From this, it was confirmed that the formation of calcium silicate mineral proceeds more easily at the initial sintering temperature by the application of coal ash.

Detoxification of PCBs Containing Transformer Oil by Catalytic Hydrodechlorination in Supercritical Fluids (초임계유체 내 수첨탈염소반응에 의한 PCBs가 함유된 절연유의 무해화 연구)

  • Choi, Hye-Min;Kim, Jae-Hoon;Kim, Jae-Duck;Kang, Jeong-Won
    • Clean Technology
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    • v.15 no.1
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    • pp.9-15
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    • 2009
  • Catalytic hydrodechlorination of PCBs (polychlorinated biphenyls) included in the transformer oil was carried out to detoxify PCBs and to recycle the treated oil. Catalysts such as 0.98 wt% Pt and 0.79 wt% Pd on ${\gamma}$-alumina (${\gamma}-Al_2O_3$) support, 12.8 wt% Ni on ${\gamma}-Al_2O_3$, and 57.6 wt% Ni on silica-alumina ($SiO_2-Al_2O_3$) support were used for the catalytic hydrodechlorination. Various supercritical fluids such as carbon dioxide, propane and isobutane were used as reaction media. The effects of reaction temperature, reaction time, catalysts, and supercritical fluids on the catalytic hydrodechlorination were examined in detail. The detoxification degree increased in the order of Ni > Pd > Pt. This is possibly due to higher metal loading and larger metal size of the Ni catalyst. Below $175^{\circ}C,\;scCO_2$ was found as the most effective reaction media for the catalytic hydrodechlorination of PCBs included in the transformer oil.

Acidic Properties of ZSM-5 Zeolite Catalyst (ZSM-5 제올라이트 촉매의 산성도)

  • Byoung Joon Ahn;Joon Ryeo Park;Hakze Chon
    • Journal of the Korean Chemical Society
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    • v.33 no.2
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    • pp.177-184
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    • 1989
  • Acidic properties of ZSM-5 zeolite catalysts were investigated by temperature-programmed desorption technique and ir spectroscopy. Ammonia t.p.d. pattern of HZSM-5 showed three different states, designated as ${\alpha}$,${\beta}$ and ${\gamma}$. The amount of ${\gamma}$-state decreased with increasing $SiO_2/Al_2O_3$ ratio, and upon cation-exchanging with alkali cations. From the ir adsorption spectra of absorbed pyridine and the reaction study of toluene alkylation, the ${\gamma}$-state could be explained to be due to the strong Bronsted acid sites of H-ZSM-5. Also they showed that the interaction between alkali cation-exchanged ZSM-5 and bases, i.e. $NH_3$ and pyridine, was increasing with decreasing the size of cations.

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Dimethyl Ether Formation Using a Zeolite Catalyst Impregnated with Ceria (세리아 첨가 제오라이트 촉매를 이용한 디메틸 에테르 합성)

  • Kim, Bo-Kyung;Koh, Jae-Cheon;Kim, Beom-Sik;Han, Myung-Wan
    • Korean Chemical Engineering Research
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    • v.49 no.2
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    • pp.155-160
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    • 2011
  • Dimethyl ether draws an attention as a green fuel in recent years. In this study, we investigated dehydration of methanol to produce DME using solid-acid catalysts, a series of zeolite. We found that ceria took a role of promoting the reaction conversion as well as selectivity of DME formation as a cocatalyst to the zeolite catalyst. We varied Si/Al ratio and ceria percentage on the surface of the catalyst to get high performance catalyst. ZSM5-30 with 5 wt% ceria on the surface was found to have excellent DME selectivity and to be little influenced by water content in methanol feed. We proposed a reaction model and obtained kinetic parameters for the DME formation using the catalyst based on experimental results using a microreactor.

Comparison of Adsorption Characteristics on Zeolite 13X and Silica-aluminar (제올라이트 13X와 실리카-알루미나의 흡착특성 비교)

  • Lee, Song-Woo;Na, Young-Soo;An, Chang-Doeuk;Lee, Min-Gyu
    • Journal of Environmental Science International
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    • v.20 no.6
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    • pp.729-736
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    • 2011
  • This work is to compare the experiment results by a continuous fixed-bed adsorption of water vapor, acetone vapor, and toluene vapor on zeolite 13X (SAU) and silica-alumina (SAK). SAU and SAK have very different pore structure but similar composition as inorganic adsorbent. The relationship between the equilibrium adsorption capacity and specific pore size range were studied. Adsorption of water vapor was more suitable on SAU than SAK because SAU has relatively more developed pores around $5\;\AA$ than SAK in the pore range of $10\sim100\;\AA$. Adsorption of acetone vapor was more suitable on SAK than SAU because SAK has relatively more developed pores around $5\sim10\;\AA$ than SAK in the pore range of less than $10\;\AA$. Adsorption of toluene vapor was more suitable on SAK than SAU because SAK has relatively more developed pores in the pore range of $10\sim100\;\AA$ than SAK. Adsorption capacity of the adsorbent was closely related to the surface area generated in the specific pore size region. But it was difficult to distinguish the relationships between adsorption capacity and micro area, and the external surface area of adsorbent.

Preparation of Alumina-Silica Composite Coatings by Electrophoretic Deposition and their Electric Insulation Properties (EPD 방법을 이용한 알루미나-실리카 복합 코팅막의 제조와 전기절연 특성)

  • Ji, Hye;Kim, Doo Hwan;Park, Hee Jeong;Lim, Hyung Mi;Lee, Seung-Ho;Kim, Dae Sung;Kim, Younghee
    • Journal of the Korean Ceramic Society
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    • v.51 no.3
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    • pp.177-183
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    • 2014
  • Alumina-silica composite coating layers were prepared by electrophoretic deposition (EPD) of plate-shaped alumina particles dispersed in a sol-gel binder, which was prepared by hydrolysis and the condensation reaction of methyltrimethoxysilane in the presence of colloidal silica. The microstructure and the electrical and thermal properties of the coatings were compared according to the EPD process parameter: voltage, time and the content of the plate-shaped alumina particles. The electrical insulation property of the coatings was measured by a voltage test. The coatings were prepared by EPD of the sol-gel binder with 5-30 wt% plate alumina particles on parallel electrodes at a distance of 2 cm for 1-10 min under an applied voltage of 10-30 V. The coatings experienced increased breakdown voltage with increasing thickness. However, the higher the thickness was, the smaller the breakdown voltage strength was. A breakdown voltage as high as 4.6 kV was observed with a $400{\mu}m$ thickness, and a breakdown voltage strength as high as 27 kV/mm was achieved for the sample under a $100{\mu}m$ thickness.

Wear Characteristics of Rubber-Seal for Inflow of Dust Particles in Automobile Chassis System -PART II: The Influence of Dust Particle Inflow on Wear Characteristics of Rubber-Seal- (자동차 섀시 시스템에 유입되는 먼지입자에 의한 고무-씨일 부품의 마멸특성 -PART II: 먼지유입에 따른 고무-씨일의 마멸특성-)

  • Lee, Young-Ze;Chung, Soon-Oh;Won, Tae-Yeong;Kim, Gi-Hoon;Kim, Dae-Sung
    • Tribology and Lubricants
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    • v.25 no.4
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    • pp.261-264
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    • 2009
  • Environmental factors affect parts of the automobile. When dust particles are embedded, specially, friction and wear of the rubber-seal in automobile chassis system are increased. Increase in friction and wear leads to weakness of component and reduction of mechanical life. In this study, the wear characteristics of rubber-seal for inflow of dust particles are investigated. Silica($SiO_2$) and alumina($Al_2O_3$) particles are used as a dust particle because these particles are main elements of dust particles. The sliding wear tester are used for investigate the wear characteristics of rubber-seal. If the single dust particle($SiO_2$) is embedded in the rubber-seal component, the influence of dust particle size is more than that of inflow rate on the wear characteristics of rubber-seal. If the mixed dust particles are embedded in the rubber-seal component, the wear rate is increased as the rate of alumina that has a bigger hardness is increased. If the mixed dust particles that have different hardness are embedded in the rubber-seal component, the influence of particle size is more than that of particle hardness.

Synthesis of Pyridine and β-Picoline from Acrolein and Ammonia on Pd/SiO2-Al2O3 Catalysts (Pd/SiO2-Al2O3 촉매상에서 아크로레인과 암모니아로 부터 피리딘과 β-피콜린의 합성)

  • Chun, Sung-Woo;Choi, Jung-Kun;Oh, Seok-Youn;Na, Suk-Eun;Park, Dae-Won
    • Applied Chemistry for Engineering
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    • v.2 no.2
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    • pp.138-146
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    • 1991
  • $Pd/SiO_2-Al_2O_3$ catalysts were prepared for the synthesis of pyridine and ${\beta}$-picoline from acrolein and ammonia. The activity of these catalysts decreased considerably by the formation of deposits on catalyst surface during the reaction. TPR study showed that the deposits were formed by the condensation polymerization of acrolein and ammonia. The conversion and production rate of pyridine and ${\beta}$-picoline decreased with the partial pressure of acrolein. The amount of deposits and the regeneration temperature of spent catalysts increased with the partial pressure of acrolein but they were independent of the concentration of ammonia.

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