• 에너지공학
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• 제20권4호
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• pp.298-302
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• 2011

In this study, Catalytic reforming with vapor and biomass gasification was simultaneously performed in a same fixed bed reactor at $600-800^{\circ}C$. Light gases were produced from reformation of the tar (fuel gases) in biomass gasification by using limonite and dolomite, as catalysts. Hydrogen and carbon dioxide are main components in light gases. Hydrogen yields increased with temperature increasing in the range of $650-800^{\circ}C$, because the water shift reaction was promoted by catalyst. The yield of hydrogen gas was increased about 160% under catalyst with the mixture of limonite and dolomite comparing to limonite only.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2009년도 춘계학술대회 논문집
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• pp.861-862
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• 2009

Precipitated iron-based catalysts are highly promising for the Fischer-Tropsch synthesis (FTS), in particular for the low temperature FTS below $280^{\circ}C$, because of their high activity and low cost. $SiO_2$ is an essential promoter for the precipitated iron-based catalysts to improve the attrition strength and physical stability. In this study, we carried out FTS over precipitated iron-based catalysts with and without $SiO_2$ in a fixed-bed reactor. The catalysts were prepared by a conventional co-precipitation method. In case of the catalysts with $SiO_2$, we used two comparative preparation methods, i.e., incorporation of $SiO_2$ before precipitation (denoted as precipitated $SiO_2$) and after precipitation (denoted as binder $SiO_2$), respectively. The addition of $SiO_2$ crucially affects both physico-chemical properties and catalytic peformance of precipitated iron-based catalysts.

• 한국수소및신에너지학회논문집
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• 제22권4호
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• pp.415-423
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• 2011

HI decomposition step certainly demand catalytic reaction for efficient production of hydrogen in SI process. Platinum catalyst can apply to HI decomposition reaction as well as hydrogenation or dehydrogenation. Generally, noble metal is used as catalyst which is loaded form for getting high dispersion and wide active area. In this study, Pt was loaded onto zirconia, ceria, alumina, and silica by impregnation method. HI decomposition reaction was carried out under the condition of $450^{\circ}C$, 1atm, and $167.76h^{-1}$ (WHSV) in a fixed bed reactor for measuring catalytic activity. And property of a catalyst was observed by BET, TEM, XRD and chemisoption analysis. On the basis of experimental results, we discussed about conversion of HI according to physical properties of the loaded Pt catalyst onto each support.

• 한국대기환경학회지
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• 제13권4호
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• pp.319-325
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• 1997

The catalytic decomposition of CFC-113(1,1,2-trichloro-1,2,2-trifluoroethane) was studied over an activated carbon catalyst in a fixed-bed reactor at the temperature from 300 to 600$^\circ$C, the space velocity (SV) of 1800 $\sim 14400h^{-1}$ and the mole ratio(decomposition agent/CFC-113) of 0.25 $\sim$ 5. In the absence of a decomposition agent, the decomposition efficiency of CFC-113 was low but when a decomposition agent was added to the gas stream, it was dramatically increased with the increase of temperature. In particular, in the presence of n-hexane as the decomposition agent it showed a high decomposition efficiency compared with benzene at 400$^\circ$C. It was found that the decomposition activity of CFC-113 was very sensitive to reaction temperature. Thus it is expected that to raise the reaction temperature is more effective than to increase the residence time and the amount of decomposition agent. Over the activated carbon catalyst more than 99% decomposition was achieved at the reaction temperature of 600$^\circ$C, SV of 7200$h^{-1}$, the mole ration $(C_6H_{14}/CFC-113)$ of 1 in this study.

• 공업화학
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• 제27권4호
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• pp.407-414
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• 2016

고정층 반응기를 이용하여 제올라이트(HZSM-5, HBeta, HY) 상에서 국내 수종 굴참나무의 간접 촉매 열분해를 수행하였다. 고품질 바이오오일 생산 최적 조건을 도출하기 위해 시료와 촉매의 비율과 반응 온도의 영향 또한 고찰하였다. 세 종의 촉매 중에서 HZSM-5가 적절한 기공크기와 강한 산도로 인해 가장 높은 방향족 화합물 형성능을 나타내었다. HY와 HBeta 또한 촉매능을 가졌으나, 큰 기공크기로 인해 많은 양의 코크가 형성되었다. HZSM-5 상에서 참나무의 촉매 열분해를 통해 방향족 화합물의 수율을 극대화하기 위해서는 낮은 시료/촉매비와 높은 반응 온도가 요구됨을 확인하였다.

• 대한환경공학회지
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• 제22권5호
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• pp.819-825
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• 2000

본 연구는 자동차 폐촉매의 재활용 가능성을 검토하기 위하여 촉매의 물리화학적 특성 및 acetaldehyde의 연소활성에 관하여 조사하였다. 자동차 폐촉매의 물리화학적 특성을 조사하기 위하여 EA(Elemental analysis), ICP-AES (Inductively coupled plasma-atomic emission spectrophotometer), XRD(X-ray diffraction) 분석을 수행하였다. Carbon 침적량은 촉매의 전반부가 후반부보다 많았으며, 주행거리에 따라 증가하는 경향을 보였다. Pt, Pd, Rh 함유량은 제작사에 따라 구성성분의 차이를 보였다. 모델 VOC로서 acetaldehyde를 선택하였으며, 상압유통식 반응장치를 이용하여 촉매의 연소활성을 조사하였다. 자동차 폐촉매의 후반부가 전반부보다 촉매 활성이 우수하였다. 또한 주행거리의 증가에 따라 촉매활성은 감소하는 경향을 나타내며, 주행거리와 촉매활성은 매우 우수한 상관성을 보였다. 자동차 폐촉매의 acetaldehyde 연소활성은 매우 우수하였으며, 소규모의 배출원 제어에 활용 가능한 것으로 평가된다.

• 한국대기환경학회지
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• 제26권4호
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• pp.443-448
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• 2010

The objective of this study was to assess the catalytic activities of manganese oxide (MnO, $MnO_2$, $Mn_2O_3$, and $Mn_3O_4$) catalysts for odors (acetaldehyde and propionaldehyde) removal. We used a fixed bed reactor as the experimental apparatus and the catalytic performance were carried out over the temperature range of $200{\sim}470^{\circ}C$. The properties and performance of catalysts were characterized by the X-ray diffraction (XRD) and Brunauer Emmett Teller (BET). The catalytic activities of manganese oxide catalysts for acetaldehyde combustion were in the order of MnO < $MnO_2$ < $Mn_2O_3$ < $Mn_3O_4$, and it is similar to that of propionaldehyde combustion. We also confirmed that the reactions have well followed the kinetic model of Power-Rate Law and the reaction order (n) is 1 for both of the acetaldehyde and propionaldehyde combustion. In addition, the reaction activation energy of acetaldehyde and propionaldehyde combustion over $Mn_3O_4$ were found to be $72.42\;kJmol^{-1}$ for 487~503 K and $51.14\;kJmol^{-1}$ for 473~533 K, respectively.

• Korean Chemical Engineering Research
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• 제44권2호
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• pp.193-199
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• 2006

${\gamma}-Al_2O_3$에 담지한 Cu-Mn 산화물 촉매에서 톨루엔 완전산화 반응을 $160{\sim}280^{\circ}C$의 온도 범위에서 고정층 반응기로 조사하였다. BET, SEM, TPR, TPO, XPS 및 XRD를 이용하여 촉매 특성분석을 하였다. 톨루엔의 완전산화 반응은 $280^{\circ}C$ 이하에서 이루어졌으며, 적절한 Cu-Mn 담지량은 15.0 wt％Cu-10.0 wt％Mn인 것으로 나타났다. TPR/TPO 및 XPS 분석 결과, 15 Cu-10 Mn 촉매의 산화환원 봉우리가 낮은 온도로 이동하였으며 결합에너지가 높은 값으로 이동하였다. XRD 결과, 고분산된 Mn 산화물과 CuO 보다 $Cu_{1.5}Mn_{1.5}O_4$의 촉매활성 인자로서의 역할이 더욱 우수한 것으로 추측되며, 촉매의 활성은 촉매의 산화환원 능력과 촉매의 높은 산화 상태에 기인하는 것으로 사료된다.

• 청정기술
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• 제20권3호
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• pp.212-217
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• 2014

재생공정에서 황화 된 탈황흡수제의 재생을 위하여 산소는 산화제로 사용되었다. 재생공정에서 미량의 미 반응 산소는 직접 황 회수 공정으로 유입된다. 그러나, $SO_2$ 환원을 위한 반응성은 미 반응 산소의 다양한 이유에 의해서 저하된다. $SO_2$ 환원을 위한 반응성 실험을 위해 Sn-Zr계 촉매가 사용되었으며, $SO_2$와 $O_2$는 각각 5.0 vol%와 4.0 vol%로 고정하였고 $300-450^{\circ}C$와 1-20 atm에서 수행되었다. 본 연구에서는 고온건식 탈황공정의 직접 황 회수공정에 유입되는 미 반응산소에 의한 촉매반응성 저하에 미치는 영향을 조사하였다. $SO_2$ 환원으로 생성된 원소 황은 미 반응산소에 의해서 재산화되고, redox반응기구에서 Sn-Zr계 촉매의 빈 격자 산소자리가 미 반응산소에 의해서 재산화되므로 $SO_2$ 전화율은 감소되는 것으로 판단된다. 한편 환원제로써 공급된 CO는 미 반응산소에 의해서 산화되어 연소열에 의해 촉매 충전 층 온도가 상승되기도 한다. 결과적으로 충전 층의 빠른 온도상승은 활성 물질을 소결시켜 촉매의 비활성화를 초래하게 된다.

• 한국수소및신에너지학회논문집
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• 제23권4호
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• pp.346-352
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• 2012

The properties of methane oxidation were studied in this research over transition metal containing $CeO_2$ (TM/$CeO_2$, TM=Ni, Co, Cu, Fe) with TM content of 5 wt. % at atmospheric pressure. The characteristics of catalysts were investigated by various characterization techniques, including XRD, GC, SEM and EPMA analyses. The catalytic tests were carried out in a fixed Rmix ratio of 1.5 ($CH_4/O_2$) in a fixed-bed reactor operating isothermally at atmospheric pressure. Only the Ni/$CeO_2$ catalysts showed syngas production above $400^{\circ}C$ via typical partial oxidation reaction whereas other catalysts induced complete oxidation resulting in the production of $CO_2$ and $H_2O$ in whole reaction temperature range. From the quantitative analysis on carbon deposition after catalytic tests, Cu/$CeO_2$ was found to show the highest resistance on carbon deposition. Therefore Cu can be proposed as an efficient catalyst element which can be combined with a conventional Ni-based SOFC anode to enhance the carbon tolerance.