• 공업화학
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• 제9권1호
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• pp.101-106
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• 1998

제올라이트를 담체로 사용하여 활성금속으로 코발트와 몰리브덴을 담지시킨 촉매와 상용공정에 사용되는 $NiMo/{\gamma}-Al_2O_3$촉매를 제조하여, 저온에서의 DBT 탈황활성과 선택성에 대하여 비교하였다. 고정층 고압 연속흐름반응기에서 수행된 탈황반응에서, 저온 영역인 $200^{\circ}C$와 $225^{\circ}C$에서는 제조된 $NiMo/{\gamma}-Al_2O_3$촉매보다 CoMo/zeolite 촉매에서 탈황활성이 더 높았으며, $275^{\circ}C$ 이상의 고온 영역에서는 $NiMo/{\gamma}-Al_2O_3$촉매의 탈황활성이 더 높게 나타났다. $NiMo/{\gamma}-Al_2O_3$촉매에서는 biphenyl과 cyclohexylbenzene이 주생성물인데 비하여 zeolite를 담체로 사용한 촉매의 경우 알킬화반응이 일어나 생성물 분포가 매우 다름을 보여주고 있으며, 알킬화반응과 수소첨가반응의 두 가지 경로를 통해서 최종 생성물질인 alkylcyclohexane을 생성하는 것으로 추정된다. 제올라이트 담체상에서 molybdenum은 flesh 촉매에서 $MoO_3$형태로 존재하고 있으며, aged 촉매상에서는 $MoO_3$와 $MoS_2$형태로 황화되어 있음을 알 수 있었다.

• Korean Chemical Engineering Research
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• 제49권2호
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• pp.168-174
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• 2011

La을 기반으로 하는 다양한 페롭스카이트 촉매를 페치니(Pechini)법에 따라 제조하고, 이 촉매를 음식물 처리 과정에서 발생하는 악취 성분의 저온 산화 반응에 적용하여 효과적인 탈취가 이루어지도록 하였다. 배출 가스의 정량 및 정성 분석을 통하여 음식물 처리 시간에 따른 주요 악취 성분의 양을 조사하였다. 그리고 주요 악취 성분들로 구성된 표준 악취 시료는 산화 반응기의 반응물로 도입하였다. 먼저, 다양한 전이 금속 M이 치환된 La 기반 페롭스카이트 촉매($LaMO_{3}$: M=Cr, Mn, Fe, Co 및 Ni)를 제조하고 전이 금속 M의 영향을 알아보기 위해 악취 성분의 산화 반응에 적용한 결과, 테스트한 촉매 중에서 $LaNiO_3$ 촉매가 가장 우수한 촉매 활성을 보였다. 또한 촉매 활성을 증진시키기 위하여 Pt가 치환된 페롭스카이트 촉매($LaNi_{1-x}Pt_{x}O_{3}$: x=0, 0.03, 0.1 및 0.3)를 제조하였고, 이로부터 $LaNi_{0.9}Pt_{0.1}O_{3}$ 촉매가 가장 효율적인 촉매인 것을 알 수 있었다. 끝으로 저온 산화 반응에서의 페롭스카이트 촉매의 활성을 극대화하기 위하여 담지된 페롭스카이트 촉매($XLaNi_{0.9}Pt_{0.1}O_{3}/Al_{2}O_{3}$: X=페롭스카이트 함량(wt%), 0, 10, 20, 30, 40, 50 및 100)를 적용하였다. $XLaNi_{0.9}Pt_{0.1}O_{3}/Al_{2}O_{3}$ 촉매의 활성은 페롭스카이트 함량에 따라 화산형(Volcano-shaped) 곡선을 나타내었으며, 이 때 $20LaNi_{0.9}Pt_{0.1}O_{3}/Al_{2}O_{3}$ 촉매가 $180^{\circ}C$의 반응 온도에서 88.7%의 가장 높은 전환율을 보였다.

• 청정기술
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• 제18권1호
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• pp.95-101
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• 2012

수소생산을 위한 메탄의 부분산화용 촉매로 알루미나에 담지된 코발트와 니켈 촉매를 함침법으로 제조하였다. 이들 코발트와 니켈 촉매에 조촉매 성분 Mg, Ce, La와 Sr을 첨가하여 초촉매 효과를 조사하였다. 메탄의 부분산화반응을 위한 촉매의 활성은 상압, $CH_4/O_2$ = 2.0에서 450~$650^{\circ}C$의 온도영역으로 조사하였다. 촉매의 특성은 BET, XRD와 SEM/EDX를 이용하여 조사하였다. 0.2 wt%의 조촉매 성분의 첨가로 촉매성능의 상승효과를 얻을 수 있었다. $500^{\circ}C$ 이상의 온도에서는 $Co/Al_2O_3$에 Mg을 첨가한 촉매가 가장 우수한 메탄 전환율과 수소 선택성을 나타내었다. 낮은 온도 영역에서는 $Ni/Al_2O_3$에 Ce와 Sr을 첨가한 촉매가 Co계 촉매보다 우수한 반응특성을 나타내었다. $Co/Al_2O_3$와 $Ni/Al_2O_3$에 조촉매를 첨가한 경우 촉매의 표면적이 증가하는 것으로 나타났다.

• 한국수소및신에너지학회논문집
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• 제25권6호
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• pp.570-576
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• 2014

LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas ratio on the amount of LFG components over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Results were obtained through the activity reaction experiments at the temperature of $900^{\circ}C$ and GHSV of 4,000. The results were as following; it has generally shown that methane conversion rate increased with the increase of oxygen and carbon dioxide amounts. Highly methane conversion of 92~93% and syngas ratio of approximately 1.0 were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 360ml/min of water, respectively, under reactor pressure of 15 bar for 50 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.

• 한국수소및신에너지학회논문집
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• 제26권5호
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• pp.477-483
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• 2015

LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas yield on the amount of LFG components over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Results were obtained through the methan reforming experiments at the temperature of $900^{\circ}C$ and GHSV of 8,800. The results were as following; it has generally shown that syngas yield increase with the increase of oxygen and steam amounts and then decrease. Highly methane conversion of above 98% and syngas yield of approximately 60% were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 450ml/min of steam, respectively, under reactor pressure of 1 bar for 200 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.

• 공업화학
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• 제19권5호
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• pp.466-470
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• 2008

본 연구에서는 가연성 폐기물에서 발생되는 합성가스 내 $CH_4$를 나노기공성 촉매를 사용하여 $H_2$로 전환하고자 하였다. 이때 사용된 나노기공성 촉매는 $Ni/Al_2O_3$ 촉매를 one-pot 방법으로 제조하여 사용하였다. 촉매의 분석 결과, 삼차원으로 연결된 스폰지 모양을 갖는 입자가 형성되었으며, 구형의 상용 촉매보다 넓은 표면적과 작은 입자크기, 균일한 기공 크기의 특성을 지닌 나노기공성 촉매가 제조된 것을 확인할 수 있었다. $CH_4$ 개질반응에 사용된 $Ni/Al_2O_3$ 촉매의 Ni 최적 담지량은 16 wt%였으며 $750^{\circ}C$에서 $CH_4$ 전환율 91%, $CO_2$ 전환율 92%로 가장 높은 전환율을 나타냈다. 또한, 상용 알루미나를 사용하여 제조한 촉매와의 성능 비교 결과 자체 제조한 촉매가 약 20% 향상된 전환율을 나타냈다.

• 한국재료학회지
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• 제25권8호
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• pp.391-397
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• 2015

NiO catalysts/$Al_2O_3$/FeCrAl alloy foam for hydrogen production was prepared using atomic layer deposition (ALD) and subsequent dip-coating methods. FeCrAl alloy foam and $Al_2O_3$ inter-layer were used as catalyst supports. To improve the dispersion and stability of NiO catalysts, an $Al_2O_3$ inter-layer was introduced and their thickness was systematically controlled to 0, 20, 50 and 80 nm using an ALD technique. The structural, chemical bonding and morphological properties (including dispersion) of the NiO catalysts/$Al_2O_3$/FeCrAl alloy foam were characterized by X-ray diffraction, X-ray photoelectron spectroscopy, field-emission scanning electron microscopy and scanning electron microscopy-energy dispersive spectroscopy. In particular, to evaluate the stability of the NiO catalysts grown on $Al_2O_3$/FeCrAl alloy foam, chronoamperometry tests were performed and then the ingredient amounts of electrolytes were analyzed via inductively coupled plasma spectrometer. We found that the introduction of $Al_2O_3$ inter-layer improved the dispersion and stability of the NiO catalysts on the supports. Thus, when an $Al_2O_3$ inter-layer with a 80 nm thickness was grown between the FeCrAl alloy foam and the NiO catalysts, it indicated improved dispersion and stability of the NiO catalysts compared to the other samples. The performance improvement can be explained by optimum thickness of $Al_2O_3$ inter-layer resulting from the role of a passivation layer.

• 한국표면공학회:학술대회논문집
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• 한국표면공학회 2012년도 춘계학술발표회 논문집
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• pp.218-219
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• 2012

Carbon coils could be synthesized using $C_2H_2/H_2$ as source gases and $SF_6$ as an incorporated additive gas under thermal chemical vapor deposition system. Prior to the carbon coils deposition reaction, two kinds of samples having different combination of Ni catalyst and substrate were employed, namely a commercially-made $Al_2O_3$ ceramic boat with Ni powders and a commercially-made $Al_2O_3$ substrate with Ni layer. By using a commercially-made $Al_2O_3$ ceramic boat, the production yield of carbon coils could be enhanced as much as 10 times higher than that of $Al_2O_3$ substrate. Furthermore, the dominant formation of the microsized carbon coils could be obtained by using $Al_2O_3$ ceramic boat.

• 한국대기환경학회지
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• 제2권2호
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• pp.51-59
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• 1986

Hydrodesulfurization of dibenzothiophene (DBT) dissolved in n-heptane was studied over sulfided $Ni - W/\gamma - Al_2O_3$ catalyst at temperature ranges from 513 to 573 K and at pressure ranges from 20 to 60 x $10^5$ Pa. Hydrogenation of biphenyl (BP) and cyclohexylbenzene (CHB) observed in products were also run. The products were almost biphenyl and cyclohyxylbenzene, and the conversion of DBT was very sensitive to temperature. Concerning the products distribution while the formation of biphenyl decreased, the formation of cyclohexylbenzene increased in the range of high pressure. The reaction network was found to be sequential reaction which formed cyclohexybenzent through the intermediate of biphenyl. The disappearances of DBT and biphenyl were the first order with respect to DBT and biphenyl and their activation energys were 24.3 and 13.6 Kcal/mol, respectively.

• 한국응용과학기술학회지
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• 제28권3호
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• pp.321-328
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• 2011

The autothermal reforming reaction of methane was investigated to produce hyd rogen with Ni/$CeO_2-ZrO_2$, Ni/$Al_2O_3$-MgO and Ni-Ru/$Al_2O_3$-MgO catalysts. Honeycomb metalli c monolith was applied in order to obtain high catalytic activity and stability in autothermal r eforming. The catalysts were characterized by XRD, BET and SEM. The influence of various catalysts on hydrogen production was studied for the feed ratio($O_2/CH_4$, $H_2O/CH_4$). The $O_2/CH_4$ and $H_2O/CH_4$ ratio governed the methane conversion and temperature profile of reactor. Th e reactor temperature increased as the reaction shifted from endothermic to exothermic reactio n with increasing $O_2/CH_4$ ratio. Among the catalysts used in the experiment, the Ni-Ru/$Al_2O_3$-MgO catalyst showed the highest activity. The 60% of $CH_4$ conversion was obtained, and th e reactor temperature was maintained $600^{\circ}C$ at the condition of GHSV=$10000h^{-1}$ and feed ratio S/C/O=0.5/1/0.5.