• Title/Summary/Keyword: $Ce-ZrO_2$

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Syngas and Hydrogen Production under concentrated solar radiation : Redox system of $ZrO_2$ nano-structure (고온 태양열을 이용한 합성가스 및 수소 생산 : $ZrO_2$ 나노 구조화에 따른 산화/환원 특성)

  • Jang, Jong-Tak;Lee, Jong-Min;Cho, Eun-Su;Yang, Seung-Chan;Yoon, Ki-June;Han, Gui-Young
    • 한국태양에너지학회:학술대회논문집
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    • 2012.03a
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    • pp.463-469
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    • 2012
  • Solar thermochemical syngas and hydrogen production process bv redox system of metal oxide was performed under direct irradiation of the metal oxide on the SiC ceramic foam device using solar simulator. $CeO_2/ZrO_2$ nanotube has been synthesized by anodic oxidation method. Syngas and hydrogen production process is one of the promising chemical pathway for storage and transportation of solar heat by converting solar energy to chemical energy. The produced syngas had the $H_2/CO$ ratio of 2, which was suitable for methanol synthesis or Fischer-Tropsch synthesis process. After ten cycles of redox reaction, $CeO_2$ was analyzed using XRD pattern and SEM image in order to characterize the physical and chemical change of metal oxide at the high temperature.

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Effects of Gallia Additions on Sintering Behavior of 상용분말로 제조된 $Ce_{0.8}Gd_{0.2}O_{2-\delta}$ Ceramics Prepared by Commercial Powders (상용분말로 제조된 $Ce_{0.8}Gd_{0.2}O_{2-\delta}$ 세라믹스의 소결성에 미치는 $Ga_2O_3$의 첨가효과)

  • 최광훈;박혜영;이주신;류봉기
    • Proceedings of the Materials Research Society of Korea Conference
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    • 2003.11a
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    • pp.113-113
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    • 2003
  • 고체전해질체로 사용되는 산소이온전도체로는 $Y_2$O$_3$ 안정화 ZrO$_2$가 널리 연구되어 왔고, 실질적으로 많이 사용되고 있다. 그러나 특히 대전력을 얻고자 하는 고체전해질 연료전지 분야에 있어서는 다른 재료를 찾고자 하는 많은 노력이 이루어지고 있다. 이에 CeO$_2$계 세라믹스는 ZrO$_2$계보다 낮은 온도에서 더 높은 이온전도도를 가지고 있어 많은 주목을 받고 있다. 그러나 이 CeO$_2$계를 소결시키는 데는 1$600^{\circ}C$이상의 고온을 필요로 한다. 이 런 고온의 소결온도를 낮추기 위한 방안으로는 균일하고 미세한 출발원료를 사용하거나 소결조제를 첨가하는 것 등이 있다. 균일하고 미세한 출발원료를 제조하는 연구는 국내외에서 많이 이루어지고 있으나 소결조제 첨가에 대한 연구는 별로 이루어진게 없다. 다만 국외에서 Co$_3$O$_4$, Fe$_2$O$_3$, CoO 첨가에 의한 연구가 최근에 이루어지고 있으며, 본 연구실을 중심으로 Ga$_2$O$_3$, $Al_2$O$_3$ 첨가에 대한 연구가 이루어지고 있다. 본 연구실에서는 그간 공침법으로 제조되는 소결조제 첨가 Gd$_2$O$_3$-doped CeO$_2$ 분말을 사용하여 소결조제 첨가효과를 살펴보았다.

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Synthesis of Garnet in the Ca-Ce-Gd-Zr-Fe-O System (Ca-Gd-Ce-Zr-Fe-O계에서의 석류석 합성 연구)

  • Chae Soo-Chun;Jang Young-Nam;Bae In-Kook;Yudintsev S.V.
    • Economic and Environmental Geology
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    • v.38 no.2 s.171
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    • pp.187-196
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    • 2005
  • Structural sites which cations can occupy in garnet structure are centers of the tetrahedron, octahedron, and distorted cube sharing edges with the tetrahedron and octahedron. Among them, the size of cation occuping at tetrahedral site (the center of tetrahedron) is closely related with the size of a unit cell of garnet. Accordingly, garnet containing iron with relative large ionic radii in tetrahedral site can be considered as a promising matrix for the immobilization of the elements with large ionic radii, such as actinides in radioactive wastes. We synthesized several garnets with the batch composition of $Ca_{1.5}GdCe_{0.5}ZrFeFe_3O_{12}$, and studied their properties and phase relations under various conditions. Mixed samples were fabricated in a pellet form under a pressure of $200{\~}400{\cal}kg/{\cal}cm^2$ and were sintered in the temperature range of $1100\~1400^{\circ}C$ in air and under oxygen atmospheres. Phase identification and chemical analysis of synthesized samples were conducted by XRD and SEM/EDS. In results, garnet was obtained as the main phase at $1300^{\circ}C$, an optimum condition in this system, even though some minor phases like perovskite and unknown phase were included. The compositions of garnet and perovskite synthesized from the batch composition of $Ca_{1.5}GdCe_{0.5}ZrFeFe_3O_{12}$ were ranged $[Ca_{l.2-1.8}Gd_{0.9-1.4}Ce_{0.3-0.5}]^{VIII}[Zr_{0.8-1.3}Fe_{0.7-1.2}]^{VI}[Fe_{2.9-3.1}]^{IV}O_{12}$ and $Ca_{0.1-0.5}Gd_{0.0-0.8}Ce_{0.1-0.5}\;Zr_{0.0-0.2}Fe_{0.9-1.1}O_3$, respectively. Ca content was exceeded and Ce content was depleted in the 8-coordinated site, comparing to the initial batch composition. This phenomena was closely related to the content of Zr and Fe in the 6-coordinated site.

Hot Corrosion of NiCrAlY/(ZrO2-CeO2-Y2O3) Composite Coatings in Molten Salt (내열복합코팅 NiCrAlY/(ZrO2-CeO2-Y2O3)의 용융염 부식)

  • Lee, Jae-Ho;Lee, Dong-Bok
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2013.05a
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    • pp.116-116
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    • 2013
  • (Ni-22Cr-10Al-1Y)와 ($ZrO_2-25CeO_2-2.5Y_2O_3$)로 구성되는 금속/세라믹 복합코팅을 대기용사(ASP; air plasma spay)으로 철 기판위에 1:3, 2:2, 3:1의 무게비로 혼합하여 제조하였다. 용사된 코팅은 금속이영지역과 세라믹잉여지역으로 구별되고, 용사중에 NiCrAlY중의 Al이 선택적으로 산화되어 Al2O3가 계면에 존재하였다. 복합코팅은 $NaCl-Na_2SO_4$ 용융염에서 $800{\sim}900^{\circ}C$, 50시간 동안 부식실험을 실시하였다. 부식생성물은 NiO, $Cr_2O_3$, ${\alpha}-Al_2O_3$가 생성되는데, 부식이 진행되면서 용해되었다. 용융염 부식이 진행되는 동안에 Cr, Al이 외방확산하였고, Na, Cl, S는 내부로 확산되었다. 시간 및 온도뿐만 아니라 금속의 양이 증가할수록 코팅의 내식성은 저하되었다.

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Two-step thermochemical cycles for hydrogen production using NiFe2O4/m-ZrO2 and CeO2 devices (NiFe2O4/m-ZrO2와 CeO2를 이용한 고온 태양열 열화학 싸이클의 수소 생산)

  • Kim, Chul-Sook;Cho, Ji-Hyun;Kim, Dong-Yeon;Seo, Tae-Beom
    • Journal of the Korean Solar Energy Society
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    • v.33 no.2
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    • pp.93-100
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    • 2013
  • Two-step thermochemical cycle using ferrite-oxide($Fe_2O_4$) device was investigated. The $H_2O$(g) was converted into $H_2$ in the first experiment which was performed using a dish type solar thermal system. However the experiment was lasted only for 2 cycles because the metal oxide device was sintered and broken down. Another problem was that the reaction was taken place mainly on a side of the metal oxide device. The m-$ZrO_2$, which was widely known as a material preventing sintering, was applied on the metal oxide device. The ferrite loading rate and the thickness of the metal oxide device were increased from 10.67wt% to 20wt% and from 10mm to 15mm, respectively. The chemical reactor having two inlets was designed in order to supply the reactants uniformly to the metal oxide device. The second-experiment was lasted for 5 cycles, which was for 6 hours. The total amount of the $H_2$ production was 861.30ml. And cerium oxide($CeO_2$) device was used for increasing $H_2$ production rate. $CeO_2$ device had low thermal resistance, however, more $H_2$ production rate than $Fe_2O_4$ device.

Pt/$Ce_{(1-x)}Zr_{(x)}O_2$ catalyst optimization for water gas shift reaction (WGS 반응용 Pt/$Ce_{(1-x)}Zr_{(x)}O_2$ 촉매 최적화)

  • Jeong, Dae-Woon;Kim, Ki-Sun;Eum, Ic-Hwan;Lee, Sung-Hun;Koo, Kee-Young;Yoon, Wang-Lai;Roh, Hyun-Seog
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.11a
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    • pp.213-216
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    • 2009
  • WGS(Water Gas Shift)반응은 일산화탄소(CO)를 이산화탄소($CO_2$)로 전환하는 반응으로 일체형 수소생산시스템의 실현을 위한 고순도 수소생산에 있어서 중요한 단계이다. WGS 반응은 열역학적 평형을 고려하여 고온전이반응(HTS: High Temperature Shift)과 저온전이반응(LTS: Low Temperature Shift) 두 단계 반응으로 진행된다. 두 단계 공정의 통합을 위해 낮은 온도에서 높은 활성을 갖는 WGS 반응용 촉매 개발이 필요하다. 최근 낮은 온도에서 높은 활성을 갖는 귀금속 촉매에 다양한 담체를 적용시킨 연구가 활발히 진행되고 있다. 선행 연구 결과, Ce-$ZrO_2$ 구조는 Ce/Zr 비에 따라 다양한 특성 변화를 관찰하였다. 따라서 낮은 온도에서 높은 활성을 갖는 WGS 반응용 촉매 제조를 위해 환원성 담체인 $CeZrO_2$에 Pt 을 담지시켜 성능을 평가하였다. 제조된 모든 담체는 공침법(Co-precipitation)으로 제조 하였으며 $500^{\circ}C$에서 6시간 소성하였다. 제조된 담체에 백금(Pt)을 함침법(Incipient Wetness Impregnate)으로 담지시켰다. 특성분석은 BET를 이용하여 표면적을 측정하였다. 촉매 반응 실험조건은 $200^{\circ}C{\sim}400^{\circ}C$ 온도범위에서 기체공간속도(GHSV: Gas Hourly Space Velocity) 45,000 ml/$h{\cdot}g-cat$ 으로 혼합가스($H_2$:60%, $N_2$:20%,$CH_4$:1%,CO:9%,$CO_2$:10%)를 흘려 반응 후 배출되는 가스를 Micro-Gas Chromatography 를 이용하여 측정하였다.

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A Study on the Ceria Stabilized Tetragonal Zirconia Polycrystals(Ce-TZP)(I) : Effect of CeO2 Content on the Mechanical Properties and Fracture Behavior of Ce-TZP (CeO2 안정화 정방정 Zirconia 다결정체(Ce-TZP)에 관한 연구(I) : CeO2 함량에 따른 Ce-TZP의 기계적 성질과 파괴거동의 변화)

  • 김문일;박정현;강대석;문성환
    • Journal of the Korean Ceramic Society
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    • v.26 no.5
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    • pp.719-727
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    • 1989
  • By using commercial zirconia powder CeO2-ZrO2 ceramics containing 8~16mol% CeO2 was made by heat treatment at 1350~155$0^{\circ}C$ for 1~10hr. The minimum amount of CeO2 for obtaining complete tetragonal phase was 12mol%, and in the tetragonal phase region fracture toughness of Ce-TZP was decreased with increasing CeO2 content and the maximum value was obtained when 12mol% CeO2 was added. The bending strength goes through maximum at 14mol% CeO2. Fracture mode of Ce-TZP transformed from intergranular to transgranular fracture with increasing CeO2 content, so the morphology of fracture surface of 16mol% Ce-TZP was wholly transgranular and this tendency was independent on grain size. The crystal structure of the 12mol% Ce-TZP was monoclinic with fringes along the grain boundaries which are lying in the particular plane from the TEM observation. The chemical composition of the sintered body was homogeneous as a whole and some amorphism or air pocket was observed at the triple junction.

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Steam Reforming of Hydrothermal Liquefaction Liquid from Macro Algae over Ni-K2TixOy Catalysts (Ni-K2TixOy 촉매를 이용한 해조류 유래 수열 액화 원료의 수증기 개질 반응 연구)

  • Park, Yong Beom;Lim, Hankwon;Woo, Hee-Chul
    • Clean Technology
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    • v.23 no.1
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    • pp.104-112
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    • 2017
  • Hydrogen production via steam reforming of liquefaction liquid from marine algae over hydrothermal liquefaction was carried out at 873 ~ 1073 K with a commercial catalyst and Ni based $K_2Ti_xO_y$ added catalysts. Liquefaction liquid obtained by hydrothermal liquefaction (503 K, 2 h) was used as a reactant and comparison studies for catalytic activity over different catalysts (FCR-4-02, $Ni/K_2Ti_xO_y-Al_2O_3$, $Ni/K_2Ti_xO_y-SiO_2$, $Ni/K_2Ti_xO_y-ZrO_2/CeO_2$ and Ni/$K_2Ti_xO_y$-MgO), reaction temperature were performed. Experimental results showed Ni/$K_2Ti_xO_y$ based catalysts ($Ni/K_2Ti_xO_y-Al_2O_3$, $Ni/K_2Ti_xO_y-SiO_2$, Ni/$K_2Ti_xO_y-ZrO_2$/ $CeO_2$ and Ni/$K_2Ti_xO_y$-MgO) have a higher activity than commercial catalyst (FCR-4-02) and In particular, a product composition was different depending on support materials. An acidic support ($Al_2O_3$) and a basic support (MgO) led to a higher selectivity for CO while a neutral support ($SiO_2$) and a reducing support ($ZrO_2/CeO_2$) resulted in a higher $CO_2$ selectivity due to water gas shift reaction.

The optical and structural properties by ZrO2 and Y2O3 compositional ratio of Co- and Ce-doped cubic zirconia (YSZ) single crystals (ZrO2와 Y2O3 조성비에 따른 Co와 Ce 첨가 큐빅지르코니아(YSZ) 단결정의 광학적 및 구조적 특성)

  • Moon, So-I.;Park, Hee-Yul;Seok, Jeong-Won
    • Journal of the Korean Crystal Growth and Crystal Technology
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    • v.22 no.2
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    • pp.73-77
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    • 2012
  • Co-(0.8 wt%) and Ce-(0.4 wt%) doped cubic zirconia ($ZrO_2$ : $Y_2O_3$ = 80 : 20, 70 : 30, 60 : 40, 50 : 50 wt%) single crystals grown by a skull melting method were heat-treated in $N_2$ at $1000^{\circ}C$ for 5 hrs. The orange, yellowish brown and brown colored as-grown single crystals were changed into either brownish red, yellow and green color after the heat treatment. Before and after the heat treatment, the YSZ (yttria-stabilized zirconia) single crystals were cut for wafer form (${\phi}6.5mm{\times}t2mm$). The optical and structural properties were examined by UV-VIS spectrophotometer and X-ray diffraction. Absorption by $Ce^{3+}(^2F_{5/2,7/2}(4f){\rightarrow}^2T_g(5d^1))$, $Co^{2+}(^4A_2(^4F){\rightarrow}^4T_1(^4F)$ or $^4T_1(^4P))$ and $Co^{3+}$, change of ionization energy and lattice parameter were confirmed.

Two-Step Thermochemical Cycle with Supported $NiFe_2O_4$ for Hydrogen Production (지지체의 변화에 따른 Ni-페라이트의 2단계 열화학 사이클 반응 특성에 관한 연구)

  • Kim, Woo-Jin;Kang, Kyoung-Soo;Kim, Chang-Hee;Choi, Won-Chul;Kang, Yong;Park, Chu-Sik
    • Transactions of the Korean hydrogen and new energy society
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    • v.19 no.6
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    • pp.505-513
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    • 2008
  • The two-step thermochemical cycle was examined on the $CeO_2$, YSZ, and $ZrO_2$-supported $NiFe_2O_4$ to investigate the effects of support material addition. The supported $NiFe_2O_4$ was prepared by the aerial oxidation method. Thermal reduction was conducted at 1573K and 1523K while water-splitting was carried out at 1073K. Supporting $NiFe_2O_4$ on $CeO_2$, YSZ and $ZrO_2$ alleviated the high-temperature sintering of iron-oxide. As a result, the supported $NiFe_2O_4$ exhibited greater reactivity and repeatability in the water-splitting cycle as compared to the unsupported $NiFe_2O_4$. Especially, $ZrO_2$-supported $NiFe_2O_4$ showed better sintering inhibition effect than other supporting materials, but hydrogen production amount was decreased as cycle repeated. In case of $CeO_2$-supported $NiFe_2O_4$, improvement of hydrogen production was found when the thermal reduction was conducted at 1573K. It was deduced that redox reaction of $CeO_2$ activated above 1573K.