• Bulletin of the Korean Chemical Society
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• 제21권12호
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• pp.1233-1238
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• 2000

$Mo/{\gamma}-Al_2O_3catalysts$ modified with Fe, Co, and Ni were prepared by impregnation method and catalytic activity for water gas shift reaction was examined. The optimum amount of Mo loaded for the reaction was 10 wt% $MoO_3$ to ${\gamma}-Al_2O_3.$ The catalytic activity of $MoO_3/{\gamma}-Al_2O_3was$ increased by modifying with Fe, Co, and Ni in the order of Co${\thickapprox}$ Ni > Fe. The optimum amounts of Co and Ni added were 3 wt% based on CoO and NiO to 10 wt% $MoO_3/{\gamma}-Al_2O_3$, restectively. The TPR (temperature-programmed reduction) analysis revealed that the addition of Co and Ni enganced the reducibility of the catalysts. The results of both catalytic activity and TPR experiments strongly suggest that the redox property of the catalyst is an important factor in water gas shift reaction on the sulfided Mo catalysts, which could be an evidence of oxy-sulfide redox mechanism.

• Bulletin of the Korean Chemical Society
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• 제28권3호
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• pp.413-416
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• 2007

The adsorption and surface reactions of NO on a VO/V(110) surface have been investigated using X-ray photoelectron spectroscopy (XPS), near-edge X-ray absorption fine structure, and temperature programmed desorption (TPD) technique. NO is molecularly adsorbed on VO/V(110) at 80 K. As the surface coverage of NO increases, the NO dimer is formed on the surface at 80 K. Both NO and (NO)2 are adsorbed on the surface with the N-O bond perpendicular to the surface. (NO)2 decomposes at ~100 K and the reaction product is desorbed as N2O. Decomposition of NO takes place when the surface temperature is higher than 273 K.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2012년도 제42회 동계 정기 학술대회 초록집
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• pp.87-88
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• 2012

Metal oxide nanostructures have been applied to various fields such as energy, catalysts and electronics. We have freely designed one and two-dimensional (1 and 2-D) metal (transition metals and lanthanides) oxide nanostructures, characterized them using various techniques including scanning electron microscopy, transmission electron microscopy, X-ray diffraction crystallography, thermogravimetric analysis, FT-IR, UV-visible-NIR absorption, Raman, photoluminescence, X-ray photoelectron spectroscopy, and temperature-programmed thermal desorption (reaction) mass spectrometry. In addition, Ag- and Au-doped metal oxides will be discussed in this talk.

• 한국자동차공학회논문집
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• 제19권3호
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• pp.52-56
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• 2011

Active regeneration in CDPF requires $O_2$ which regenerates soot at high temperature. However, small amount of NO can interrupt $O_2$ regeneration in CDPF. To verify this phenomena, soot oxidation experiments using a flow reactor with a $Pr/CeO_2$ catalyst are carried out to simulate Catalyzed Diesel Particulate Filter (CDPF) phenomena. Catalytic soot oxidation with and without small amount of NO is conducted under tight contact condition. As the heating rate rises, the temperature gap of maximum reaction rate is increased between with and without 50ppm NO. To accelerate the $NO_2$ de-coupling effect, CTO process is performed to eliminate interfacial contact for that time. As CTO process is extended, temperature which indicates peak reaction rate increases. From this result, it is found that small amount of NO can affect tight contact soot oxidation by removal of interfacial contact between soot and catalyst.

• Bulletin of the Korean Chemical Society
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• 제31권11호
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• pp.3283-3290
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• 2010

The gas-phase dehydration of glycerol to acrolein was carried out over 10 wt % HSiW catalysts supported on different supports, viz. $\gamma-Al_2O_3$, $SiO_2-Al_2O_3$, $TiO_2$, $ZrO_2$, $SiO_2$, AC, $CeO_2$ and MgO. The same reaction was also conducted over each support without HSiW for comparison. Several characterization techniques, $N_2$-physisorption, thermogravimetric analysis (TGA), differential scanning calorimetry (DSC), the temperature-programmed desorption of ammonia ($NH_3$-TPD), temperature-programmed oxidation (TPO) with mass spectroscopy and CHNS analysis were employed to characterize the catalysts. The glycerol conversion generally increased with increasing amount of acid sites. Ceria showed the highest 1-hydroxyacetone selectivity at $315^{\circ}C$ among the various metal oxides. The supported HSiW catalyst showed superior catalytic activity to that of the corresponding support. Among the supported HSiW catalysts, HSiW/$ZrO_2$ and HSiW/$SiO_2-Al_2O_3$ showed the highest acrolein selectivity. In the case of HSiW/$ZrO_2$, the initial catalytic activity was recovered after the removal of the accumulated carbon species at $550^{\circ}C$ in the presence of oxygen.

• 신재생에너지
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• 제6권4호
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• pp.30-40
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• 2010

Syngas from gasification of coal can be converted to SNG(Synthesis Natural Gas) through gas cleaning, water gas shift, $CO_2$ removal, and methanation. One of the key technologies involved in the production of SNG is the methanation process. In the methanation process, carbon oxide is converted into methane by reaction with hydrogen. Major factors of methanation are hydrogen-carbon oxide ratio, reaction temperature and space velocity. In order to understand the catalytic behavior, temperature programmed surface reaction (TPSR) experiments and reaction in a fixed bed reactor of carbon monoxide have been performed using two commercial catalyst with different Ni contents (Catalyst A, B). In case of catalyst A, CO conversion was over 99% at the temperature range of $350{\sim}420^{\circ}C$ and CO conversions and $CH_4$ selectivity were lower at the space condition over 3000 1/h. In case of catalyst B, CO conversion was 100% at the temperature over $370^{\circ}C$ and CO conversions and $CH_4$ selectivity were lower at the space condition over 4700 1/h. Also, conditions to satisfy $CH_4$ productivity over 500 ml/h.g-cat were over 2000 1/h of space velocity in case of catalyst A and over 2300 1/h of space velocity in case of catalyst B.

• 대한화학회지
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• 제23권3호
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• pp.161-164
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• 1979

$Ca^{2+},\;La^{3+},\;NH_4^+$ 등으로 양이온을 교혼하거나, 알루미늄을 추출한 합성 zeolite Y에 팔라듐을 담지시켜, 촉매산성도 및 담지된 금속의 유효표면적을, n-butane의 분해반응에서 촉매활성과 관련지어 조사하였다. 암모니아의 TPD(Temperature Programmed Desorption) 실험에 의하면 NaY < CaY < LaY 순으로 강한 산점의 양이 많아졌으며, 알루미늄 추출로 $SiO_2/Al_2O_3$의 비가 커질 수록 전체산점의 양은 감소되었으나, 강한 산점의 양은 증가되었다. CO의 화학흡착으로 측정한 담지금속의 유효표면적은 산성도가 큰 촉매에서 비교적 컸다. n-Butane의 zeolite 촉매에서의 반응은, 촉매의 산성도와 금속성분의 유효표면적에 관계되나, 전화율이 측정한 범위내에서의 유효표면적에 비례하므로 금속성분에 의한 탈수소반응이 중요한 단계로 생각된다.

• 청정기술
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• 제20권1호
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• pp.28-34
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• 2014

본 연구에서는 나노 크기의 결정 구조를 가진 타이타니아 담체를 용매열합성법(solvothermal method)을 활용하여 합성한 후 팔라듐과 구리를 담지한 촉매를 제조하였다. 제조된 촉매를 수중 질산성 질소 저감 반응에 적용한 결과, 타이타니아 담체의 결정 크기가 반응 활성에 영향을 미치는 것이 확인되었다. 결정 크기가 작은 담체를 활용한 촉매가 더 빠른 속도로 질산성 질소를 저감하였지만, 반응 중 pH가 높게 형성되어 질소 선택도가 매우 낮은 현상을 보였다. 이를 해결하기 위해 pH 완충제인 이산화탄소를 공급하여 질소 선택도를 약 60% 증가시켰다. 상기에 언급한 촉매를 대상으로 질소 흡-탈착, X-ray diffraction (XRD), $H_2$-temperature programmed reduction (TPR), X-ray photoelectron spectroscopy (XPS) 등의 다양한 특성화 분석을 수행하여 촉매의 반응활성과 물성간의 상관관계에 대해 조사하였다.

• 청정기술
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• 제2권1호
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• pp.60-68
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• 1996

고정층 반응기에서 망간광석을 이용하여 저농도의 일산화탄소 산화제어반응에 대하여 고찰하였다. 고려된 실험변수는 일산화탄소 농도 (500ppm~10000ppm), 산소 농도(500ppm~99.8%)와 촉매의 온도($50{\sim}750^{\circ}C$)이다. 또한 망간광석의 특성은 Thermogravimetric Analysis(TGA), 일산화탄소에 의한 환원, Temperature Programmed Reduction(TPR)실험을 이용하여 규명하였다. 망간광석의 일산화탄소 산화력은 순수이산화망간에 비해서 단위 면적당 높은 산화력과 $750^{\circ}C$까지 가열된 후에도 산화력이 유지될 수 있는 안정된 촉매작용을 보였다. Temperature Programmed Desorption(TPD), TPR 실험과 TG 등의 분석결과 산소의 농도가 낮거나 무산소하에서 망간광석의 격자내 산소가 쉽게 제공될 수 있음을 알 수 있었다. 일산화탄소의 농도가 500~3500ppm일 때 일산화탄소의 반응차수는 0.701이며 3500~10000ppm구간에서 일산화탄소의 농도에 무관한 0차 반응이었다.

• Korean Chemical Engineering Research
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• 제60권1호
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• pp.159-168
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• 2022

MoO₃ 비율을 10-50 중량비로 변화하여 제조한 Mo-Al 복합 산화물 상에서 소성 후 승온 질화반응을 통하여 얻은 Mo-Al 질화물 상에서 암모니아 분해반응에서의 촉매 활성을 검토하였다. 제조된 촉매의 물리·화학적 특성을 알아보기 위하여 N₂ 흡착분석, X-선 회절분석(XRD), X-선 광전자분석법(XPS), 수소 승온환원(H₂-TPR), 투과전자현미경(TEM) 분석을 수행하였다. 600 ℃에서 소성 후 Mo-Al 복합산화물은 γ-Al₂O₃와 Al₂(MoO₄)₃ 결정상을 나타냈으며 질화반응 후의 질화물은 비정형 형태를 보여주었다. 질화반응 후의 비표면적은 MoO₃의 위상전환반응에 의해 Mo 질화물 형성으로 인해 증가하였으며, Mo 질화물이 γ-Al₂O₃에 담지된 형태를 보여주었다. 암모니아 분해반응에서의 촉매 활성은 40 wt% MoO₃가 가장 좋은 활성을 보여주었고, 질화반응 시간이 증가함에 따라 활성이 증가하였으며 이에 따라 활성화에너지 감소 효과를 나타냈다.