• 한국세라믹학회지
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• 제33권9호
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• pp.1064-1072
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• 1996

The synthetic conditions and characteristics of ZSM-5 type zeolites (ZSM-5/silicalite) for the preparation of the zeolite composite membranes for gas separation were investigated. ZSM-5 zeolites could be synthesized by the hydrothermal treatment of the mixture of colloidal silica sol aluminum nitrate sodium hydroxide and TPABr at a temperature range of 150-17$0^{\circ}C$ in the autoclave. Silicalties were done from the solution of water glass water and TPABr. Their crystalline structures transformed from orthorhombic to monoclinic from and their pore structures of three-dimensional channels were opened as TPABr filling channels was burned off at the calcination temperature of 50$0^{\circ}C$. The specific surface area of the calcined zeolite was about 360 m3/g and its surface property was hydrophobic. Crystal sizes of ZSM-5 and silicalite were 0.5-1.0${\mu}{\textrm}{m}$ and 8-10${\mu}{\textrm}{m}$ respectively having no change due to the calcination. In particular the shape and the size of the ZSM-5 type zeolite were sensitively varied with silica sources and concentrations of reaction solutions/sols.

• 한국세라믹학회지
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• 제34권7호
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• pp.747-757
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• 1997

ZSM-5 zeolite composite membranes have been synthesized from a silica sol solution containing TPABr as an organic template by the dip-coating and the pressurized-coating hydrothermal treatment techniques. The CO2 separation efficiency of synthesized composite membranes was also investigated. The permeation mechanism of CO2 through ZSM-5 membranses was the surface diffusion, and that of N2, O2, and He gases was Knudsen diffusion or activated diffusion depending on the synthetic method of membranes and the measurement temperature. The CO2/N2 separation factor of the membrane prepared by the dip-coating hydrothermal treatment was 2.5 at about 12$0^{\circ}C$, while the ZSM-5 composite membrane synthesized by the pressurized-coating hydrothermal treatment technique showed the CO2/N2 separation factor of 9.0 at room temperature higher than that ever reported in the literature.

• Bulletin of the Korean Chemical Society
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• 제35권2호
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• pp.525-530
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• 2014

Titanium dioxide nanotube supported ZSM-5 zeolite composite catalyst was fabricated by decorating ZSM-5 zeolite on the hydrothermally synthesized titanium dioxide via hydrothermal process and subsequent annealing. The catalyst was characterized by X-ray powder diffraction (XRD), Transmission electron microscopy (TEM) and Nitrogen adsorption-desorption (BET). The surface acidity of the catalyst was measured by means of Fourier transform infrared (FT-IR) spectrum of pyridine adsorption. And the catalytic activity for ethanol dehydration to ethylene was evaluated in a continuous flow fixed-bed reactor. Attributed to the increase of the effective surface acid sites caused by titanium dioxide nanotube as electron acceptor, titanium dioxide nanotube supported ZSM-5 zeolite composite catalyst exhibits strongly enhanced activity for ethanol dehydration to ethylene.

• 멤브레인
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• 제16권2호
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• pp.159-166
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• 2006

휘발성 유기화합물로서 3가 염소탄화수소인 트리클로로메탄, 트리클로로에탄, 트리클로로에틸렌을 MFI 구조인 소수성 제올라이트 ZSM-5 분리막으로 투과증발을 이용하여 물과의 이성분계 혼합물로부터 선택적으로 분리하고자 하였다. 직경 9.5 mm 다공성 스테인리스 스틸 튜브의 내부 표면에 수열합성법으로 ZSM-5 제올라이트 결정을 성장시켜 박막을 만들어 분리막으로 이용하였으며, 합성된 ZSM-5 제올라이트 분리막으로 공급되는 3가 염소화합물의 농도 및 실험 온도에 따른 분리 특성을 고찰하였다. 3가 염소화합물의 수용액상 농도를 0.0001 몰분율부터 0.001 몰분율로 변화하면서, 또한 실험 온도를 25에서 $45^{\circ}C$로 바꾸면서 투과증발 실험을 수행한 결과 트리클로로메탄/물 이성분계에 대하여 약 $16{\sim}66$의 선택도를 얻었으며, 트리클로로에탄/물 이성분계에 대하여 $3.3{\sim}4.6$의 선택도와 트리클로로에틸렌/물 이성분계에 대하여 $1.4{\sim}8$의 선택도를 관찰할 수 있었다.

• 한국분말재료학회지
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• 제3권3호
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• pp.153-158
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• 1996

The exhaust gas from vehicle engines and industrial boilers contains considerable amount of harmful nitrogen monoxide(NO) which causes air pollusion and acid rain. To remove NO catalytic reduction processes using Cu ion exchanged ZSM-5 zeolite have been widely studied. In this study, an attempt was made to fabricate Cu/zeolite catalyst by using high energy ball mill. The catalytic performance of ball milled Cu/ZSM-5 zeolites is analyzed and optimum copper contents was determined. The processing variables were reaction temperature and copper contents. Complete removal of NO gas was obtained at the temperature of 553 K on 10wt.% CU/ZSM-5 mechanically alloyed composite powders. Mechanically alloyed CU/ZSM-5 catalyst showed homogeneous distribution of Cu in ZSM-5.

• 에너지공학
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• 제6권1호
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• pp.26-33
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• 1997

유기주형물질을 첨가하지 않고 순수하고 결정성이 좋은 구리이온이 교환된 Cu-ZSM5 제올라이트 촉매를 제조하여 NO 분해반응 실험에 사용하였다. 구리이온교환 정도의 증가에 따라 NO 분해 활성은 점차로 증가하였고 100% 이상으로 구리이온교환 시에도 지속적으로 증가하였다. 산소의 존재하에서 NO의 분해 활성은 $O_2$양이 증가할수록 저하되었고, NO, $O_2$TPD실험 결과 NO의 분해 활성점과 $O_2$의 흡착점은 같은 것으로 판명되었다. 또한 50$0^{\circ}C$에서 전처리 후에도 촉매 표면의 $O_2$는 완전히 탈착되지 않았으며, 50$0^{\circ}C$에서 수소 처리를 하였을 경우 반응 활성이 초기에 상당량 향상되는 현상으로 보아 촉매 표면에 흡착된 산소가 NO의 분해반응 활성을 저하시키는 요인이 된다는 것을 알 수 있었다.

• 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.

• 청정기술
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• 제19권3호
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• pp.287-294
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• 2013

구리-제올라이트 촉매와 Fe-제올라이트 촉매로 과잉산소 분위기에서 일산화질소의 암모니아 선택적 촉매환원반응을 체계적으로 조사하였다. 촉매는 디젤엔진에서의 SCR기술의 적용을 위하여 구리와 철을 $NH_4$-BEA와 $NH_4$-ZSM-5 제올라이트에 이온교환법과 함침법으로 담지시켜 제조하였다. 촉매의 특성은 BET, XRD, FE-TEM과 SEM/EDS를 사용하여 조사하였다. 고정된 반응조건에서 선택적 촉매환원반응의 활성을 조사한 결과에서 구리를 BEA 제올라이트에 이온교환시켜 제조한 촉매가 $200{\sim}250^{\circ}C$의 저온영역에서 탁월한 성능을 나타내었다. $250^{\circ}C$ 이하의 저온에서 구리-제올라이트 촉매가 Fe-제올라이트 촉매보다 높은 반응활성을 나타내었다. BEA 제올라이트에 담지된 촉매가 ZSM-5 제올라이트에 담지된 촉매보다 $250^{\circ}C$ 이하의 저온에서 우수한 반응활성을 나타내었다.

• Bulletin of the Korean Chemical Society
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• 제25권2호
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• pp.185-189
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• 2004

Methanol dehydration to dimethyl ether (DME) has been investigated over ZSM-5 zeolites and compared with that of ${\gamma}-Al_2O_3$. Although the catalytic activity was decreased with an increase in silica/alumina ratio, the DME selectivity increased. H-ZSM-5 and NaH-ZSM-5 zeolites were more active for conversion of methanol to DME than ${\gamma}-Al_2O_3$. $Na^+$ ion-exchanged H-ZSM-5 (NaH-ZSM-5) shows higher DME selectivity than H-ZSM-5 due to the selective removal of strong acid sites.

• 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.