• Bulletin of the Korean Chemical Society
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• 제31권2호
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• pp.339-343
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• 2010

A series of $Ce_1Mg_xZr_{1-x}O_2$ (CMZO) mixed metal oxide with different molar ratio were prepared by simple co-precipitation method. The prepared materials were tested for their catalytic activity performance using Knoevenagel condensation of various aromatic aldehydes with barbituric acid under solvent-free condition in microwave. The best catalytic activity was obtained with CMZO (1:0.6:0.4). The synthesized materials were characterized by using XRD, FT-IR, SEM-EDS techniques.

• 한국응용과학기술학회지
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• 제30권4호
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• pp.649-655
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• 2013

페롭스카이트 촉매와 Mo, Bi를 기본으로 하는 복합 산화물 촉매를 이용하여 천연가스의 주성분인 메탄의 부분산화를 통하여 메탄올을 직접 합성하였다. 페롭스카이트($ABO_3$) 촉매는 A 및 B site 성분을 변화시키면서 사과산법으로 제조하였으며, Mo, Bi를 기본으로 하는 3성분계 복합 산화물 촉매는 공침법으로 제조하여 반응특성을 살펴보았다. 페롭스카이트 촉매에서 A site에 알칼리 금속인 Sr을, B site에 전이금속인 Cr을 도입한 $SrCrO_3$ 촉매가 $400^{\circ}C$에서 메탄올 선택도 11%로 가장 우수한 결과를 보였다. Mo, Bi를 기본으로 하는 3성분계 복합 산화물 촉매의 경우 모든 촉매에서 메탄 전환율에는 큰 차이를 보이지 않았으며, Cr을 첨가한 Mo-Bi-Cr 복합 산화물 촉매가 $400^{\circ}C$에서 메탄올 선택도 15.3%로 가장 우수한 결과를 나타냈다. 3성분계 복합 산화물 촉매에서 촉매의 활성과 메탄올 선택도는 촉매의 표면적에 정비례하였다.

• Korean Chemical Engineering Research
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• 제57권6호
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• pp.758-762
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• 2019

이동용 고분자전해질 연료전지(PEMFC)의 수소발생용으로써 $NaBH_4$는 많은 장점을 갖고 있다. 해상용으로 PEMFC가 사용될 때 해수를 이용해 $NaBH_4$를 가수분해 하면 경제적이다. 그래서 본 연구에서는 $NaBH_4$ 가수분해 과정에 증류수대신 해수를 이용해 수소를 발생시켰다. 활성탄 담지 Co-B/C 촉매를 사용해 $NaBH_4$ 가수분해 특성에 대해 연구하였다. 해수 사용시 $NaBH_4$ 농도와 NaOH농도가 증가하면서 수소수율이 감소하였다. 높은 $NaBH_4$와 NaOH농도에서 촉매 표면에 부산물이 부착되어 증류수에 비해 수소수율이 감소했다. $NaBH_4$ 가수분해 활성화에너지는 증류수와 해수 각각 59.3, 74.4kJ/mol로 해수에서 수소발생속도를 증류수와 같이 높이려면 반응온도를 $80^{\circ}C$이상 상승시켜야 함을 보였다.

• 동력기계공학회지
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• 제12권5호
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• pp.27-33
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• 2008

Natural gas has been considered one of the most promising alternative fuels for transportation because of its abundance as well as its ability to reduce regulated pollutants. We measured emission characteristics of nanoparticles from lean burn H/D(Heavy-Duty) CNG (Compressed Natural Gas) engine equipped with oxidation catalysts. The experiments were carried out to measure the emission and engine performance according to the ESC test cycle. The CO and THC conversion efficiencies on the best catalyst in the ESC test cycle achieved about 91 % and 83 %, respectively. From the measurement by the SMPS, the number of nanoparticles emitted from H/D CNG engine is reduced by about 99 % which is more than that of 2.5 L diesel engine. The particle number concentrations of H/D CNG engine were almost nanoparticles. Nanoparticles smaller than 30 nm emitted from the H/D CNG engine and diesel engine equipped with a CDPF(Catalyzed Diesel Particulate Filter) were quite similar. However, the particles bigger than 30nm from the CNG engine were smaller than the particles from diesel engine equipped with a CDPF. The higher the CNG engine load, the lower the particle number from engine-out, but it increased slightly at full load.

• Journal of Photoscience
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• 제6권3호
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• pp.91-96
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• 1999

Zeolites and microporouos materials continue to attract attention as novel hosts for photochemical reactions. Zeolities are attractive because of their ability to selectivity exchange and incorporate species within the void spaces and interconnecting channels, providing a spatial arrangement of molecules. Our research has primarily focused on intrazeolitic electron transfer from excited Ru(bpy)32+ in supercages of zeolite Y to a series of bipyridinium ions. In the Ru(bpy)32+ viologen-zeolite Y samples, the slowing of the back electron transfer from the bipyridinium radical cation to Ru(bpy)32+ allows for charge propagation via self exchange between diquat molecules. This provides an opportunity for permanent charge separation. When the migrating charge on the diquat radical within the zeolite reaches the surface, it can be transferred to a neutral viologen (PVS) in solution, resulting in permanent charge separation. The advantage of long-lived charge separation can be exploited for useful chemistry if suitable catablysts can be assembled on the zeolities. We have studied Ru(bpy)2 as water oxdiation catalysts. We have demonstrated that synthesis of RuO2 fibers on a zeolite via thermal decomposition of Ru3(CO)12 leads to the most active water decomposition catalyst reported to date. Because of the extensive interest of photochemical water reduction to H2, much is known about catalytic systems usin gone electron catalyst, and even more importantly, that no reaction of viologen occurred with H2 over this catalyst. The present challenge is to incorporate all these elements of the system into an architecture and we are examining zeolite membranes for this purpose.

• Elastomers and Composites
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• 제51권1호
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• pp.49-55
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• 2016

Nanosized cobalt disulfide ($CoS_2$) particles were synthesized with 0.08 M cobalt chloride hexahydrate ($CoCl_2{\cdot}6H_2O$) and 0.2 M sodium thiosulfate pentahydrate ($Na_2S_2O_3{\cdot}5H_2O$) dissolved in distilled water under microwave irradiation. $[C_{60}]Fullerene-CoS_2$ nanocomposites were prepared with nanosized $CoS_2$ particles and [$C_{60}$]fullerene as heated by $700^{\circ}C$ for 2 h in an electric furnace. X-ray diffraction (XRD), scanning electron microscopy (SEM) and transmission electron microscopy (TEM) identified the heated $[C_{60}]fullerene-CoS_2$ nanocomposites. Heated $[C_{60}]fullerene-CoS_2$ nanocomposites were investigated the activity of photocatalytic degradation as a catalyst in various organic dyes like acid yellow 23, methylene blue, methyl orange, and rhodamine B with ultraviolet light at 254 nm by UV-vis spectrophotometer.

• 공업화학
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• 제9권6호
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• pp.803-810
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• 1998

능금산법으로 제조된 페롭스카이트 촉매에서 입자상물질의 연소반응에 대하여 연구하였다. 페롭스카이트 산화물의 A 및 B site에 금속이온을 치환시켜 연소반응의 활성을 증가시켰다. 또한 반응온도, 산소의 농도, 공간속도, $SO_2$ 및 물의 영향에 대하여 조사하였다. $LaCoO_3$형 촉매의 A site에 알칼리족 금속을 치환시키면 연소개시 온도가 낮아졌고, 알카리족 금속은 Cs>K>Na의 순서로 연소활성을 증가시켰다. 그러나 $La_{0.6}Cs_{0.4}CoO_3 $촉매에서 B site에 Fe나 Mn을 치환시키더라도 연소개시 온도의 변화가 거의 없었다. 산소의 농도가 증가함에 따라 연소개시 온도는 낮아졌고 이산화탄소의 생성속도는 산소분압의 영향을 별로 받지 않았다. 한편 공간속도의 증가에 따라 연소개시온도가 낮아졌고, 이산화황에 대한 촉매의 비활성화는 일어나지 않았으며, 반응물 중에 첨가된 물에 의해 연소반응이 촉진되었다.

• 한국수소및신에너지학회논문집
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• 제19권3호
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• pp.199-208
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• 2008

HI decomposition was conducted using Pt/C-based catalysts with a fixed-bed reactor in the range of 573 K to 773 K. To examine the change of the characteristic properties of the catalysts, $N_2$ adsorption analyser, a X-ray diffractometer(XRD), and a scanning electron microscopy(SEM) were used before and after the HI decomposition reaction. the effect of Pt loading on HI decomposition was investigated by $CO_2$-TPD. HI conversion of all catalysts increased as decomposition temperature increased. The XRD analysis showed that the sizes of platinum particle became larger and agglomerated into a lump during the reaction. From $CO_2$-TPD, it can be concluded that the cause for the increase in catalytic activity may be attributed to the basic sites of catalyst surface. The results of both b desorption and gasification reaction showed the restriction on the use of Pt/C-based catalyst.

• 대한기계학회논문집B
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• 제28권1호
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• pp.24-30
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• 2004

Analysis model for the two-phase catalytic reactor is presented. With the progress in development of micro thermofluidic devices, needs fur understanding of the phenomena in two phase reaction in cm scale has been arisen. To investigate thermal and reactive performance of down scaled two phase reactor simple analysis model that is a kind of lumped flow model is proposed. Analysis model presented is based on the experiment on mm scale model reactor. Target experiment is catalytic decomposition of 70wt％ hydrogen peroxide with existence of perovskite L $a_{0.8}$S $r_{0.2}$Co $O_3$ catalyst. It is composed of balance equations of mass and energy. Each phase is considered to be a species fur the simplicity. Axial diffusion and transversal distribution of properties are neglected. Two phase catalytic reaction is modeled as successive gasification of liquid lump around catalyst and reaction in gas phase. Heat transfer is modeled by model function ofNu number. Modeled Nu is expressed as Nu=N $u_{0}$ (1＋ $a_1$( $a_2$ $T^{-}$ $a_3$)exp( $a_4$ $T^{-1}$)exp( $a_{5}$ z). Transfer coefficients are determined by the comparison of experimental results. With the model, heat transfer characteristics are investigated. Also by the mass transfer coefficient, characteristics in mass transfer is investigated. With the result basic understanding on design and analysis of mm scale two-phase reactive device is obtained. Also it can be further applied to micro scale reactive device fabricated by micromachining.ing..

• 대한기계학회논문집B
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• 제36권4호
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• pp.405-412
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• 2012

MCFC 발전시스템에서 연소기는 연료극의 배가스 중에 포함된 미반응 가스를 연료로 사용하여 공기극에 $H_2O$와 $CO_2$ 농도가 높은 고온의 혼합가스를 공급하는 역할을 한다. 하지만 이러한 배가스는 가연한계 이하로 내려가게 되어 통상적인 연소방식에 의한 완전연소가 어렵기 때문에 이를 해결하기 위하여 촉매연소기를 사용한다. 완전연소 및 이에 다른 공해물질의 저감 특성에 따라 최근 촉매연소는 환경친화적인 연소방식으로 주목받고 있다. 따라서 본 연구에서는 MCFC 발전시스템의 BOP 시스템에 적용되는 촉매연소기에 대한 실험연구를 수행하였다. 본문에서는 실험장치를 설명한 후 촉매연소 시스템의 설계변수, 즉, $H_2$ 연료 첨가에 따른 연료조성, 유입가스의 온도, 과잉 공기비, 촉매의 종류, 그리고 시동 스케줄에 따른 촉매연소 특성을 고찰하였다.