• 한국재료학회지
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• 제14권2호
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• pp.110-114
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• 2004

High velocity oxy-fuel sprayed NiCoCrAlY coatings were oxidized between 1000 and $1200^{\circ}C$ in air, and the oxide scales were examined by XRD, SEM/EDS, and EPMA. The unoxidized coatings consisted mainly of ${\gamma}$'$-Ni_3$Al, with some ${\gamma}$-Ni. The major oxide formed on the coatings was $\alpha$ $-Al_2$$O_3$. Additionally, (CoCr$_2$$O_4$, $CoAl_2$$O_4$) spinels and $Al_{5}$ $Y_3$$O_{12}$ coexisted. NiO was not found, despite of high amount of Ni in the coating. Below the oxide layer, internally formed $Al_2$$O_3$ existed.

• 공업화학
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• 제26권2호
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• pp.154-158
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• 2015

본 연구에서는 $NF_3$의 분해를 위한 ${\gamma}-Al_2O_3$의 촉매활성을 조사하였다. $NF_3$ 분해반응은 고정층 촉매반응기에서 $330{\sim}730^{\circ}C$ 범위의 반응온도와 $3,000{\sim}15,000mL/g-cat{\cdot}h$의 공간속도 조건에서 수행되었고, $NF_3$의 열분해 반응이 촉매분해반응와 비교를 위하여 함께 수행되었다. $400^{\circ}C$의 촉매분해 반응에서 $NF_3$의 전화율은 열분해 반응보다 4배 정도 높았으며, ${\gamma}-Al_2O_3$상에서 $NF_3$의 반응거동은 스팀의 존재에 따라 두 가지 반응경로를 나타내는 것으로 확인되었다. 스팀이 존재하지 않은 조건에서는 기체-고체 반응에 의해서 $NF_3$에 함유된 불소성분은 $AlF_3$로 전이되고, 스팀이 존재하는 조건에서는 가수분해에 의한 촉매적 분해반응이 일어난다. 또한 $NF_3$는 $500^{\circ}C$ 이상에서 NOx와 HF로 완전히 분해되는 것으로 FT-IR분석에서 확인되었다.

• 한국세라믹학회지
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• 제31권7호
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• pp.703-714
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• 1994

Sintering and microstructure of Ce-TZP/Al2O3 composite with $\alpha$-Al2O3 matrix containing dispersed 5~50 vol% ZrO2 were discussed. Sintered density was increased with elevating forming pressure in range of 6~300 MPa and about >99.2% of theoretical density was obtained at 1$600^{\circ}C$ for 2h in case of 300 MPa of 6~300 MPa uniaxially cold-pressed compacts containing 20 vol% ZrO2. All kinds of different batch composition exhibited nearly the same shrinkage behaviour with end-point shrinkage between 20 and 24%, and had the maximum shrinkage rate (0.41~0.54%/min) around 140$0^{\circ}C$. Grain growth was occurred faster in $\alpha$-Al2O3 than in {{{{ gamma }}-Al2O3 starting matrix during sintering at 1$600^{\circ}C$. Bimodal pore size distribution of interaglomerate pores with size of 0.03~0.2 ${\mu}{\textrm}{m}$ and of interaglomerate pores with size of around 60 ${\mu}{\textrm}{m}$ was obtained in Ce-TZP/$\alpha$-Al2O3 composite sintered at 130$0^{\circ}C$. But unimodal pore size distribution with around 0.1 ${\mu}{\textrm}{m}$ was observed in Ce-TZP/{{{{ gamma }}-Al2O3 composite sintered at the same temperature. Microcracks were occurred due to the tlongrightarrowm transformation of ZrO2 on cooling process.

• 공업화학
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• 제9권5호
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• pp.629-633
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• 1998

${\gamma}-Al_2O_3$을 불화한 촉매상에서 아세틸렌으로부터 1,1-difluoroethane을 합성하는 실험을 반응물질의 몰비와 접촉시간, 그리고 반응온도를 변화하여 실시하였다. 촉매의 불화는 무수 불화수소로 고온에서 행하였다. 제조된 시료는 XRD에 의한 결정성, 질소 흡착에 의한 세공성, 그리고 피리딘-IR과 암모니아-TPD에 의한 산 특성을 측정하였다. 촉매의 활성은 ${\gamma}-Al_2O_3$가 불화됨에 따라 향상되었고 반응온도 $200^{\circ}C$ 정도에서 원하는 생성물인 1,1-difluoroethane의 분율이 90% 이상이었다. 불화된 ${\gamma}-Al_2O_3$촉매상에서 얻은 중간생성물인 vinylfluoride에 비해 원하는 물질인 1,1-difluoroethane의 비는 불화수소/아세틸렌 몰비가 높고 접촉시간이 큰 경우에서 높았고 반응온도 $210^{\circ}C$에서 최대의 값을 얻었다.

• 한국수소및신에너지학회논문집
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• 제23권6호
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• pp.640-646
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• 2012

The effect of Ce promotion over 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts on the CO conversion and $CO_2$ selectivity was investigated in preferential CO oxidation (PrOx) to reduce the CO concentration less than 10 ppm in excess $H_2$ stream for polymer electrolyte membrane fuel cell (PEMFC). Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts were prepared by incipient wetness impregnation method and the loading amount of Pt was fixed at 1wt%. The content of Ce promoter which has excellent oxygen storage and transfer capability due to the redox property was adjusted from 0 to 1.5wt%. Ce-promoted 1wt% $Pt/{\gamma}-Al_2O_3$ catalysts exhibit high CO conversion and $CO_2$ selectivity at low temperatures below $150^{\circ}C$ due to the improvement of reducibility of surface PtOx species compared with the 1wt% $Pt/{\gamma}-Al_2O_3$ catalyst without Ce addition. When Ce content was more than 1wt%, the catalytic activity was decreased at over $160^{\circ}C$ in PrOx because of competitive $H_2$ oxidation. As a result, 0.5wt% Ce is optimal content not only to achieve high catalytic activity and good stability at low temperatures below $150^{\circ}C$ in the presence of $CO_2$ and $H_2O$ but also to minimize the $H_2$ oxidation at high temperatures.

• 공업화학
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• 제23권6호
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• pp.572-576
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• 2012

온실가스인 $CO_2$를 저감하기 위해 Pt계 촉매상 $CO_2$ methanation 반응에 관한 연구를 수행하였다. $Al_2O_3$의 전구체인 AlO(OH)를 열처리하여 지지체로 사용하였으며, 활성금속으로서 Pt를 사용하였다. XRD 분석결과, 활성금속인 Pt가 고르게 잘 분산되었음이 관찰되었으며, 지지체는 gamma phase의 $Al_2O_3$로 존재함을 확인할 수 있었다. 활성실험을 통해 $600^{\circ}C$로 열처리된 $Pt/Al_2O_3$ 촉매가 가장 우수한 전환율 및 선택도를 나타냄을 확인하였다.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 1996년도 추계학술발표회 논문집
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• pp.81-84
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• 1996

• Korean Chemical Engineering Research
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• 제45권3호
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• pp.215-218
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• 2007

본 연구의 목적은 다이옥신 분해 촉매 반응에 Pt/Al-MCM-41 메조포러스 촉매를 이용할 수 있는 가능성을 알아보고자 하는 것이다. 다이옥신 분해 반응에 대한 모델 반응으로 1,2-dichlorobenzene 분해 반응을 실시하였다. 비교 촉매로는 $Pt/{\gamma}-Al_2O_3$ 촉매를 사용하였다. Post grafting 방법으로 Al-MCM-41 촉매를 제조하여 실험한 결과, Si/Al = 15, 30인 Pt/Al-MCM-41 촉매가 $Pt/{\gamma}-Al_2O_3$ 촉매 보다 우수한 활성을 나타내었다. 이러한 반응 활성은 산점의 양과 밀접한 관계를 나타내었다. 특히 Al-MCM-41을 H-form으로 이온교환하여 반응 실험에 적용한 결과, 활성이 더욱 더 증대되었다.

• 한국재료학회지
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• 제12권2호
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• pp.153-159
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• 2002

The co-deposited behavior was investigated under varied bath compositions and current densities from Watt Ni plating bath containing Al and A1$_2$O$_3$powders. For single-particle bath, Al and A1$_2$O$_3$particles were agglomerated. The area percentage of A1$_2$O$_3$on plating surface decreased with increasing the current density, while that of Al on plating surface increased. On the other hand, in case of double-particle bath with 1.25g/$\ell$ of Al and 5.0g/$\ell$ of A1$_2$O$_3$5g, the area percentage of Ni-Al-A1$_2$O$_3$increased with increasing current density and the surface morphology was fine without agglomeration. Intermetallic compounds such as $\gamma$'and $\gamma$+$\gamma$' phases appeared when the co-deposited film was annealed.

• 청정기술
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• 제5권2호
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• pp.63-68
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• 1999

The activities of Ni(20wt%)/$La_2O_3$, Ni(20wt%)/${\gamma}-Al_2O_3$, and Ni(20wt%)/$SiO_2$ catalyst for $CO_2$ reforming of $CH_4$ were investigated in a fixed bed flow reactor under atmospheric condition. Catalyst characterization using XRD, TEM, SEM, BET analysis were also conducted. The catalytic activity of Ni(20wt%)/$La_2O_3$ catalyst has relatively superior to that of Ni(20wt%)/${\gamma}-Al_2O_3$ and Ni(20wt%)/$SiO_2$ catalyst. The good activity of Ni(20wt%)/$La_2O_3$ catalyst seems to depend on reduced $Ni^{\circ}$ phases of NiO($\rightarrow$ Ni + O), $LaNiO_3$($\rightarrow$ $Ni+La_2O_3$), Ni crystalline phases, and decoration of Ni phases by lanthanum species is also an important factor. Ni(20wt%)/${\gamma}-Al_2O_3$ and Ni(20wt%)/$SiO_2$ catalyst due to surface acidity resulted in the deposition of wisker type and encapsulate carbon on the surface of catalyst, but Ni(20wt%)/$La_2O_3$ catalyst did not show carbon on the surface of catalyst up to 8.5hr reaction.