• 제목/요약/키워드: Ceramic catalysts

검색결과 101건 처리시간 0.019초

Tetra Ethyl Ortho Silicate의 수화 및 중합에 미치는 촉매의 영향 (The Effects of Catalyst on the Hydrolysis and Polymerization of TEOS)

  • 정형진;이전국
    • 한국세라믹학회지
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    • 제27권1호
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    • pp.86-90
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    • 1990
  • The shape and characteristics of polymers in hydrolzed and polymerized sol were affected by the types of catalysts. In our research, the contents of water and catalysts were constant and the types of catalyst were varied. In the case of acid catalysts, polymers in sol were linear and spinnable. The shapes of polymer were affected by the types of anions in acid catalysts. In the case of catalyst having anions, F, Cl, in the same period, the effects were similar. But in the case of base catalysts polymers were rigid rod like and not spinnable.

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Modification of Thermal Degradation of Oligo(methylsilene) Catalyzed by Group 4 and 6 Transition Metal Complexes

  • 우희권;양수연;황택성;김동표
    • Bulletin of the Korean Chemical Society
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    • 제19권12호
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    • pp.1310-1314
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    • 1998
  • The oligo(methylsilene) (1) was treated with the group 4 metallocene Cp2MCl2/Red-Al (M = Ti, Zr, Hf) combination catalysts and with the group 6 metal carbonyl M(CO)6 (M = Cr, W) catalysts, producing the modified, cross-linked polymers. The average molecular weights and percent ceramic residue yields of modified polymers increase as the catalyst goes down from Ti to Hf and similarly as the catalyst goes down from Cr to W. An interrelationship between average molecular weights and percent ceramic residue yield is found within the respective group of catalysts, but is not observed as the catalyst goes down from Ti to W. The polymers modified with the group 4 metallocene combination catalysts have higher molecular weights and similar percent ceramic residue yields as compared to the polymers modified with the group 6 metal carbonyl catalysts. The catalytic activities of group 4 metallocene combinations appear to be higher -100 ℃, but to be lower at very high temperature than those of group 6 metal carbonyls.

촉매담지 세라믹 필터를 이용한 황산화물과 질소산화물의 제거에 관한 연구 (A Study on the Removal of SOx and NOx Using Catalytic Ceramic Filters)

  • 홍민선;이동섭
    • 한국대기환경학회지
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    • 제14권5호
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    • pp.455-464
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    • 1998
  • Removal teals of Soxmox were performed using low density ceramic filters doped with various catalysts. Disc type (50 mmO.Dx10 mmt) low density ceramic filters were doped with three different catalysts such as Cu to remove SOx and NOx, and Mn and Co to remove NOx. The air permeabilities and specific surface areas were 40~50cc/min.cm2.cmH2O and 4.1~8.88 m2/g, respectively. Also, the peak pore sizes of catalyst support were 3~5nm. Tests were focused to search optimum operating temperatures for different catalysts. It was found that as the CuO content increases, SOx removal efficiency was increased. NOx removal efficiencies for Mn, Cu and Co, were 85% at 30$0^{\circ}C$, 90% at 40$0^{\circ}C$ and 90% at 45$0^{\circ}C$, respectively.

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Catalytic Effects of Barium Carbonate on the Anodic Performance of Solid Oxide Fuel Cells

  • Yoon, Sung-Eun;Ahn, Jae-Yeong;Park, Jong-Sung
    • 한국세라믹학회지
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    • 제52권5호
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    • pp.350-355
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    • 2015
  • To develop ceramic composite anodes of solid oxide fuel cells without metal catalysts, a small amount of barium carbonate was added to an $(La_{0.8}Sr_{0.2})(Cr_{0.5}Mn_{0.5})O_3(LSCM)$ - YSZ ceramic composite anode and its catalytic effects on the electrode performance were investigated. A barium precursor solution with citric acid was used to synthesize the barium carbonate during ignition, while a barium precursor solution without citric acid was used to create hydrated barium hydroxide. The addition of barium carbonate to the ceramic composite anode caused stable fuel cell performance at 1073 K; this performance was higher than that of a fuel cell with $CeO_2$ catalyst; however, the addition of hydrated barium hydroxide to the ceramic composite anode caused poor stability of the fuel cell performance.

자동차 배기가스 중의 CO 가스 제거를 위한 촉매장치의 개발에 관한 연구 (The Study on the Supported Oxide Catalysts for Reducing CO Gas in Automotive Exhaust Gas)

  • 김환
    • 한국세라믹학회지
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    • 제17권4호
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    • pp.179-187
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    • 1980
  • Perovskite-type oxide catalysts in the $\textrm{LaMnO}_3$ family were prepared by both freeze drying and precipitation technique, and their catalytic activities with respect to the oxidation of CO with $O_2$ were measured in the composite gases. Freeze drying is a new technique for the prevention of migration of the solutes during drying. Therefore, the corrugated cordierite monolith fabricated with the Ø 1mm stainless steel bar was directly impregnated with nitrate solutions containing the appropriate cations, freeze dried and calcined. Precipitation was done by using $\textrm{(NH_4)}_2\textrm{CO}_3$ but the precipitated catalysts gave lower catalytic than the freeze dried samples due to, in part, relatively high calcining temperature. In this study, freeze dried composition had high catalytic activity, and their apparent activation energy for oxidation of CO was calculated by the rate plots using the data where the percent conversion of CO was less than 20%.

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규산 나트륨으로부터 THF에 의해 추출된 규산을 이용한 Mullite 전구체 제조시 촉매에 대한 영향 (Effect of Catalysts on Preparation of Mullite Precursor Using Silicic Acid Extracted by THF from Sodium Silicate)

  • 정흥호;박은희;김도수;정호승;노재성
    • 한국세라믹학회지
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    • 제37권6호
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    • pp.517-523
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    • 2000
  • Effect of catalysts, which was catalyzed by acid(HCl and HNO3) and base(NH4OH), on characteristics of the mullite powders prepared by sol-gel methdo wa sinvestigated by XRD, TGA, SEm AND BET. As a result, weight loss as a function of catalysts was in order of HCl=32.6%>HNO3=25.44%>Non=24.0%>NH4OH=22.5%. The mullite powder dried at 100$^{\circ}C$ appeared spherical shape in acid catalyst and different shape in base catalyst, but sintering powder at 1400$^{\circ}C$ appeared very fine particle of 0.05∼0.1$\mu\textrm{m}$ regardless of catalysts. In all cae, the pore quantity, which was capable to adsoprtion, was decreased with increasing temperature. In base catalyst, no change of special surface area in mullite appeared.

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Preparation of 27Ni6Zr4O143M(M=Mg, Ca, Sr, or Ba)O/70 Zeolite Y Catalysts and Hydrogen-rich Gas Production by Ethanol Steam Reforming

  • Kim, Dongjin;Lee, Jun Su;Lee, Gayoung;Choi, Byung-Hyun;Ji, Mi-Jung;Park, Sun-Min;Kang, Misook
    • Bulletin of the Korean Chemical Society
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    • 제34권7호
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    • pp.2073-2080
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    • 2013
  • In this study the effects of adding alkaline-earth (IIA) metal oxides to NiZr-loaded Zeolite Y catalysts were investigated on hydrogen rich production by ethanol steam reforming (ESR). Four kinds of alkaline-earth metal (Mg, Ca, Sr, or Ba) oxides of 3.0% by weight were loaded between the $Ni_6Zr_4O_{14}$ main catalytic species and the microporous Zeolite Y support. The characterizations of these catalysts were examined by XRD, TEM, $H_2$-TPR, $NH_3$-TPD, and XPS. Catalytic performances during ESR were found to depend on the basicity of the added alkaline-earth metal oxides and $H_2$ production and ethanol conversion were maximized to 82% and 98% respectively in 27($Ni_6Zr_4O_{14}$)3MgO/70Zeolite Y catalyst at $600^{\circ}C$. Many carbon deposits and carbon nano fibers were seen on the surface of $30Ni_6Zr_4O_{14}$/70Zeolite Y catalyst but lesser amounts were observed on alkaline-earth metal oxide-loaded 27($Ni_6Zr_4O_{14}$)3MO/70Zeolite Y catalysts in TEM photos after ESR. This study demonstrates that hydrogen yields from ESR are closely related to the acidities of catalysts and that alkaline-earth metal oxides reduce the acidities of 27($Ni_6Zr_4O_{14}$)3MO/70Zeolite Y catalysts and promote hydrogen evolution by preventing progression to hydrocarbons.

금속을 이온교환시킨 ZSM-5 촉매 상에서 Nitric Oxide의 환원반응 (Selective Catalytic Reduction of Nitric Oxide over Metal Exchanged ZSM-5 Catalysts)

  • 안성환;김태옥;함현식
    • 한국응용과학기술학회지
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    • 제17권1호
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    • pp.1-5
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    • 2000
  • The selective catalytic reduction(SCR) of nitric oxide by ethane in the presence of oxygen was investigated on Cu-ZSM-5, Co-ZSM-5 and Ga-ZSM-5 catalysts over a range of 400, 450 and $500^{\circ}C$. The catalysts were prepared by ion-exchange method. The composition of the reactant gases were 1000 ppm of NO, 1000 ppm of $C_{2}H_{6}$ and 2.5% of $O_{2}$, and the reaction was conducted in a fixed-bed reactor at 1 atm. For the 20wt% Co-ZSM-5(50) catalyst, the NO conversion reached up to 100%, while the $C_2H_6$ conversion and the CO selectivity were about 50% and 25%, respectively, at $450^{\circ}C$. For the 20wt% Cu-ZSM-5(50) catalyst, the NO conversion and the C2H6 conversion were about 80% and 100%, respectively, but there was no CO produced. The metal ion-exchanged ZSM-5 catalysts exhibited a tendency to increase the NO conversion with the Si/Al ratio of the ZSM-5, that is, NO conversion was inversely proportional to the acidity of the catalysts. But, the effect of the acidity on NO conversion was not so large. From the XRD results of the catalysts before and after SCR reaction it was found that there was no structural change.

연탄 연소가스의 촉매제독에 관한 연구 (Catalytic Detoxication of Coal Combustion Gases)

  • 장두원;어용선;손연수
    • 대한화학회지
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    • 제29권6호
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    • pp.656-663
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    • 1985
  • 연탄 연소시 발생하는 일산화탄소의 촉매전환에 의한 제독 실험을 실시하였다. 구형 ${\gamma}-Al_2O_3$ pellets, ceramic foam, honeycomb 등 세가지 다른 형태의 지지체에 0.2%의 백금을 담지시킨 후 촉매를 연탄연소 실험에 응용한 결과 첫회 사용시에는 일산화탄소의 제거효과가 모두 우수하였으나 반복 사용할 경우 사용횟수에 따라 촉매활성 전하 현상이 뚜렷하게 나타났다. 사용한 촉매양에 비하여 ceramic foam 촉매가 제독효과 및 내구성에서 가장 우수하였다. 촉매활성저하 원인은 아연 및 황화합물에 의한 촉매독이 뚜렷하였고 소결 등에 의한 백금 활성면적의 감소현상도 동시에 나타났다.

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아크릴계 하이솔리드 도료의 Rotation Rheometer에 의한 경화거동 연구 (Curing Behavior by Rotation Rheometer of Acrylic High-Solid Coatings)

  • 양인모;정충호;김태옥;박홍수;박은경
    • 한국응용과학기술학회지
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    • 제18권1호
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    • pp.40-48
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    • 2001
  • Curing reaction was carried out with the acrylic resin (ACR) [n-butyl acrylate/atyrene/2-hydroxyethyl methacrylate/acetoacetoxyethyl methacrylate (AAEM)] synthesized before and a curing agent, hexamethoxymethylmelamine (HMMM). With rotational rheometer, the effect of catalysts on curing rate of acrylic resin/melamine was examined. Among the four catalysts used, p-toluene sulfonic acid showed the highest reactivity, and the optimum amount of catalyst was 0.5 phr. It was observed that in the ACR/HMMM curing reaction, gelation point was lowered with the increasing the amount of AAEM and HMMM in the ACR.