• 한국재료학회지
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• 제9권2호
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• pp.117-123
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• 1999

삼차원적 골격구조를 가지며 세공의 크기와 산성도가 유사한 SAPO-44, SAPO-34(CHA type), SAPO-17(ERI type), 그리고 1차원적 고격구조를 가진 ZSM-23(MTT type) 촉매재료를 합성하고, 메탄올 전환방응에 있어서의 촉매적 성능을 비교 검토하였다. 이들의 산성도 세기는 SAPO-44>SAPO-34>SAPO-17>ZSM-23 순으로 나타났다. 메탄올 전환반응을 비교한 결과, 삼차원적 골격구조를 가지고 있는 SAPO-34와 SAPO-44에서 높은 에티렌 선택성이 얻어졌으며, 특히 Ni을 골격내에 도입시켰을 때 그 선택율은 더욱 증가하였다. 반면에 1차원적 골격구조를 가지고 있는 ZSM-23에서는 입체적 형상선택성의 감소로 올레핀보다는 파라핀의 선택율이 우세하였다.

• 한국대기환경학회지
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• 제9권2호
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• pp.140-146
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• 1993

CoMo, NiMo/ZSM-5 catalysts were prepared at Si/Al ratios of 100, 200 and characterized by TGA, XRD and SEM. Simultaneous hydrocracking of n-heptane and hydrodesulfurization of DBT were studied over these catalysts at the ranges of temparatures between 400$^\circ$C and 500$^\circ$C, pressure of 30 $\times 10^5$ Pa and contact time of 0.02g cat. hr/ml feed in a fixed bed flow reactor. It was shown that the hydrocracking activity of n-heptane increased in the order of NM 100, CM 100, NM 200 and CM 200 catalysts. It was also shown that the Hydrodesulfurization activity of DBT increased in the order of CM 200, NM 200, CM 100 and NM 100 catalysts and these results were thought to be that the increase of acidity of catalysts might increase hydrocracking activity of these catalysts but deactive those simultaneously. In this study it was shown that CM 100 and NM 200 were active catalysts in simultaneous hydrodesulfurization of DBT and hydrocracking of n-heptane reactions.

• 자원리싸이클링
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• 제15권5호
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• pp.17-25
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• 2006

본 연구는 Al-MCM-48을 이용하여 HDPE를 촉매 분해하는 것으로, Al-MCM-48의 촉매 활성을 Al-MCM-41, Beta, ZSM-5와 비교하였다. Al-MCM-48를 사용한 열분해 활성은 무촉매 열분해의 활성보다 매우 높았다. 다른 촉매와 비교했을 때 Al-MCM-48의 활성화 에너지는 거의 차이가 없었다. 촉매의 점진적인 비활성화 경향도 조사하였다. ZSM-5와 Al-MCM-48은 Al-MCM-41과 Beta보다 비활성화 경향이 낮았다. Py-GC/FID(pyrolyzer)를 이용하여 열분해 생성물의 특성에 대하여 분석하였다. 그 결과 ZSM-5 촉매를 사용한 경우에는 $C_1-C_4$ 범위의 기상 생성물이 많이 생성되었다. Al-MCM-41과 Beta를 사용한 경우에는 주로 $C_5-C_{12}$ 범위의 화합물이 생성되었다. Al-MCM-48은 다른 촉매들에 비해 $C_5-C_{22}$ 범위의 오일 생성물에 대해서 높은 선택도를 나타내었다.

• Bulletin of the Korean Chemical Society
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• 제19권12호
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• pp.1342-1346
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• 1998

The dehydrogenation of ethylbenzene with carbon dioxide has been carried out over ZSM-5 zeolite-supported iron oxide catalyst as well as commercial catalyst (K-Fe2O3) and unsupported iron oxide (Fe3O4) for comparison. In the dehydrogenation over the ZSM-5 zeolite-supported iron oxide catalyst, ethylbenzene is predominantly converted to styrene by an oxidative pathway in the presence of excess carbon dioxide. Carbon dioxide in this reaction is found to play a role as an oxidant for promoting catalytic activity as well as coke resistance of catalyst. On the other hand, both of commercial catalyst and unsupported Fe2O4 exhibit considerable decrease in catalytic activity under the same condition. It is suggested that an active phase for the dehydrogenation with carbon dioxide over ZSM-5 zeolite-supported iron oxide catalyst would be rather a reduced and isolated magnetite (Fe3O4)-like phase having oxygen deficiency in the zeolite matrix.

• Bulletin of the Korean Chemical Society
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• 제19권5호
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• pp.530-533
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• 1998

Chemical vapor deposition of $TiCl_4$ followed by the hydrolysis thereof at elevated temperatures was employed for the formation of $TiO_2$ clusters inside ZSM-5 matrix. BET and XRD revealed that the zeolite structure remains intact. XPS, Raman, FTIR, and UV-VIS reflectance spectroscopy indicated that $TiO_2$ particles thus formed are extremely small and localized inside the zeolite matrix.

• 공업화학
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• 제8권3호
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• pp.543-549
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• 1997

니켈(Ni)이 담지된 촉매상에서 이산화탄소와 부탄의 직접반응에 의한 합성가스와 탄화수소화합물의 생성을 검토하였다. $CO_2$와 $C_4H_{10}$의 반응에서 니켈 담지촉매는 백금 담지촉매와 유사한 활성을 나타내었으며, 부탄의 탈수소에 따큰 코크의 누적이 현저하게 나타났다. 담체로 알루미나나 Y형 제올라이트를 사용하면 일산화탄소와 수소가 주생성물이었다. 반면에 니켈을 ZSM-5형 제올라이트에 담지한 경우에는 생성물 중에 다량의 방향족화합물이 얻어졌다. Ni/ZSM-5, Ni/NaY 및 Ni/알루미나 촉매상에서 반응물 중의 이산화탄소/부탄 몰비의 증가와 함께이산화탄소의 전환율도 증가하다가 2이상에서 다시 감소하였다. 담체로 ZSM-5를 사용하고 이에 담지되는 니켈의 양을 다르게 하였을 때, 반응물의 전환율은 니켈금속의 담지량이 5wt% 부근에서 가장 높았다. 코크가 누적된 촉매상에 $CO_2$ 가스나 수증기를 흘리면 코크의 양은 감소하였다. 촉매상에 누적된 코크는 활성이 높은 상태로 결합되어 있으며, 표면의 활성탄소는 반응의 중요한 중간체로 작용하는 것으로 해석된다.

• Bulletin of the Korean Chemical Society
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• 제24권1호
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• pp.106-108
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• 2003

• Bulletin of the Korean Chemical Society
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• 제22권3호
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• pp.263-266
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• 2001

Isopropylation of phenol with 2-propanol has been carried out over Na-exchanged ZSM-5 zeolites to determine the effect of catalyst acidity on phenol conversion and product selectivity. The acid type and strength of the catalyst such as Lewis, weak and strong Bronsted acid sites are measured by pyridine adsorbed XPS and the catalytic properties are interpreted in terms of the acid properties. The active site and mechanism for the reaction are suggested based on evidence of study from the reactant adsorbed FT-IR.

• 한국수소및신에너지학회논문집
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• 제23권3호
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• pp.199-206
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• 2012

HC-SCR was conducted over Co-Pt/ZSM5 catalyst coated over 200 cpsi cordierite in the condition of atomspheric pressure and $200^{\circ}C-500^{\circ}C$. Weight ratio of Co/Pt determined from EDX analysis was 8/2, which was almost equal to the weight ratio at preparation step. XPS showed that nitrates within cobalt precursor and chlorine withn Pt precursor were removed. TEM result demonstrated that crystallite size of cobalt and Pt was under 5nm. Among these tested hydrocarbon reductants, isobutane ($i-C_4H_{10}$) showed the highest de-$NO_x$ yield of 80% under the condition of the mole ratio of reductant/NOx=1.0 at $180^{\circ}C$. De-$NO_x$ yield from HC-SCR was increased as the carbon number of hydrocarbon reductant was increased. The decrease of bonding energy between C and H of HC reductant played a role to increase of de-$NO_x$ yield, which indicated that the dissociation step of C-H bond of hydrocarbon molecule might be the rate determining step of HC-SCR. The increase of oxygen concentration in the feed resulted in the decrease of de-$NO_x$ yield but the increase of CO and $N_2O$ yield.

• 한국수소및신에너지학회논문집
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• 제22권2호
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• pp.265-273
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• 2011

HC-SCR was conducted using Fe/ZSM5 catalyst coated over 200 cpi cordierite in the conditions of atomspheric pressure and $200^{\circ}C-500^{\circ}C$. Among the tested hydrocarbon reductants, isobutane (i-$C_4H_{10}$) showed the highest de-$NO_x$ yield of 69% at $320^{\circ}C$ with the mole ratio of reductant/$NO_x$ =1.0. De-$NO_x$ yield resulted by the change of alkane reductant was increased as the carbon number of alkane reductant was increased. The order of increase of de-$NO_x$ yield was proportional to the order of decrease of bonding energy between C and H of reductant, where the H abstraction step from alkane molecule could be the rate controlling step of HC-SCR.