• Journal of Mechanical Science and Technology
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• 제14권6호
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• pp.699-703
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• 2000

Experiments were carried out to investigate the characteristics of the hydrocarbon (HC) emissions and to reduce cold start hydrocarbons in gasoline engines. An HC adsorber was, used and it coated was by Pd/Rh catalyst with zeolite on a honeycomb monolith. The HCs were efficiently trapped at temperatures below $100^{\circ}C by physical adsorption. After adsorption, they were reduced gradually by the catalytic oxidation of Pd/Rh catalysts as the adsorber temperature increased above $100^{\circ}C. Increasing amounts of methane, ethylene and n-butane were emitted as the fuel-air mixture became richer and the engine speed decreased. As the temperature of adsorber increased, high-number carbons into low-number carbons. Thus, the C4 concentration decreased significantly during the first 30 seconds, and the C2 concentration increased continuously.

• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2006년도 전기학술대회논문집
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• pp.23-24
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• 2006

The International Maritime Organization announced that the regulation of nitrogen oxide put into force for vessels constructed after 2000 from May, 2005 as agenda is satisfied on May, 2004. A honeycomb-typed Pillared Inter-Layered Clay(PILC) catalyst was developed for do-NOx SCR system in 2004. This catalyst has been applied to 9H25/33 engine that is one of the main diesel engines in Engine Machinery Division of the Hyundai Heavy Industries CO., LTD. In addition, we have tried to develop better catalysts in the aspects of easy synthetic method and performance.

• 한국전기화학회:학술대회논문집
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• 한국전기화학회 2003년도 연료전지심포지움 2003논문집
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• pp.89-95
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• 2003

Fuel processing is an enabling technology for faster commercialization under lack of hydrogen infrastructures. It has been reported that the development of novel catalysts that are active and selective for hydrocarbon reforming reactions. It has been realized, however, that with pellet or conventional honeycomb catalysts, the reforming process is mass transport limited. This paper reports the development of catalyst structures with microchannels that are able to reduce the diffusion resistance and thereby achieve the same production rate within a smaller reactor bed. These microchannel reforming catalysts were prepared and tested with natural gas and gasoline-type fuels in a microreactor (1-cm dia.) at space velocities of up to 250,000 per hour. These catalysts have also been used in engineering-scale reactors (10 kWe, 7-cm dia.) with similar product qualities. Compared to pellet catalysts. the microchannel catalysts enable a nearly 5-fold reduction in catalyst weight and volume.

• 공업화학
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• 제19권3호
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• pp.259-263
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• 2008

소각로에서 발생한 다이옥신 및 질소산화물 제거용 폐탈질 촉매($V_2O_5/TiO_2$)의 비활성화 원인을 규명하고자 반응 활성 실험 및 물리 화학적 특성 분석을 수행하였으며, 다양한 재생방법을 통한 폐탈질 촉매의 재생효율을 연구하였다. 고정층 실험 결과 $260^{\circ}C$를 기준으로 약 60% 정도 질소산화물 제거 활성 차이를 보였으며, 허니컴 실험의 경우 1, 2-Dichlorobenzen (1, 2-DCB) 분해효율이 $200^{\circ}C$에서 약 14% 정도 차이가 나타났다. 또한 촉매의 비활성화 원인을 연구하기 위해서 신촉매와 폐촉매에 대하여 XRD, TGA, 그리고 ICP의 특성 분석을 실시한 결과 황산 암모늄염, 중금속(Pb, As 등), 전이금속(Fe 등), 알칼리 금속(Ca), 그리고 상전이가 촉매의 비활성화 원인으로 조사되었다. 또한, 폐촉매의 재생을 위해 다양한 방법으로 처리한 결과 수세과정을 배제한 공기분위기에서 열처리한 경우 우수한 재생효과를 나타내었다.

• 한국대기환경학회지
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• 제12권2호
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• pp.121-130
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• 1996

The catalysts composed of Pt, Pd and W as active-components, $Al_{2}O_{3}$ and $SiO_{2}$ as supports, were perpared on the honeycomb type substrate and characterized by BET, SEM, TGA, FT-IR and XRD for diesel emission control. CO, $C_{3}H_{6}$, and $SO_{2}$ oxidation was carried out over these catalysts in a fixed bed continuous flow reactor at the temperatures between 100-500.deg.C and reactant gas was composed of 10 vol.% $O_{2}$, 1 vol.% CO, 0.8 vol.% $C_{3}H_{6}$ and 88.2 vol.% $N_{2}$. It was found that under these experimental conditions, the CO, $C_{3}H_{6}$ oxidation activity of Pt-W catalyst was higher than that of any other prepared catalyst, and this catalyst had also a good inhibition effect on $SO_{2}$ oxidation. Also it was show that the influence of $SO_{2}$ on $Al_{2}O_{3}$ was more sever than that of $SO_{2}$ on $SiO_{2}$.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.2221-2226
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• 2008

The objective of this paper is to describe the experimental and numerical investigation of the analysis of the heat transfer in a solar chemical reactor. These are compared about methane steam reforming process in the solar chemical reactor which was a volumetric absorber consisting of honeycomb and a multilayered catalyst supports. With this high operating temperature, convective heat loss, thermal fracture are important features for designing SCR. In order to estimate the system performance and to design the actual solar reactor with various conditions, CFD analysis was used in this study. The nickel oxide porous metal is inserted inside the solar chemical reactor to increase the conversion rate of the reforming reaction. Simulation has been carried out based on the experimental data. According to the simulation results, the optimum methane-steam mole ratio and thickness and numbers of catalyst supports were obtained.

• 한국가시화정보학회지
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• 제10권2호
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• pp.20-24
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• 2012

Increasing the active catalyst surface area is important in improving a converter's efficiency. In addition, uniform flow is advantageous in that it produces more efficient catalytic conversion. This results in the ability to use a smaller catalytic converter with uniform flow as opposed to a larger converter requirement for non-uniform flow. Therefore, it is important to characterize the internal flow of the catalytic converter. To characterize the system's flow patterns, velocity measurements were taken at the mid and exit planes of a ceramic honeycomb catalytic converter at flow rates of 37.8 l/s and 94.4 l/s. Measurements were conducted using LDV. The profiles were measured along both the major and minor axis of the planes. Primary flow direction velocities measured along the minor axis, at both flow rates, varied greatly at the mid plane and somewhat at the exit plane. The areas of greatest air flow were seen near the edges of the walls and on the side of the converter opposite the flow's entrance region. It also appears that the high velocities opposite the intake are due to the design of the entrance region. The entrance region is possibly too small to properly redirect the vertically entering fluid into an evenly distributed flow in the primary flow direction.

• 한국전산구조공학회논문집
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• 제24권4호
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• pp.413-419
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• 2011

나노 크기의 허니콤 구조물은 거시적 크기의 허니콤 구조물에 비해 보다 높은 부피 대비 표면적 비율을 구현하여 전기적, 화학적인 촉매로써 기능성을 극대화할 수 있다. 나노 크기의 구조물은 거시적 크기의 구조물과 다른 기계적 거동양상을 보이며 이는 표면효과에 기인한다. 이러한 표면효과는 원자 수준 전산모사(atomistic simulation)를 통해 규명할 수 있으나 나노 허니콤 구조물의 거동을 예측하는 것은 현실적으로 과도한 전산자원 및 계산시간으로 인해 불가능한 실정이다. 본 연구에서는 표면응력 탄성모델을 적용한 브리징방법을 균질화기법과 연계하여 나노 크기의 허니콤 구조물의 기계적 거동을 효율적으로 예측하였다.

• 공업화학
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• 제32권5호
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• pp.497-503
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• 2021

본 연구에서는 악취가스 및 휘발성 유기 화합물을 산화 제거하기 위한 백금/티타니아를 허니컴 및 메탈폼 담체에 코팅하는 방법을 확인하였다. 다양한 방법 중 파우더 코팅과 나노 코팅에 대한 비교를 수행하였다. SEM/EDX (Scanning Electron Microscopy/Energy Dispersive X-ray spectroscopy) 분석은 허니컴 및 메탈폼의 표면 상태 및 노출된 백금 성분비를 조사하는데 사용되었다. 또한, 촉매 코팅 방법에 따른 톨루엔, 트리메틸아민, 아이소프로필 알코올의 제거 성능을 비교하였다.

• Korean Chemical Engineering Research
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• 제45권6호
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• pp.663-668
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• 2007

$Ni/CeO_2-ZrO_2$ 촉매를 이용하여 수소 제조를 위한 메탄의 자열개질반응 특성을 조사하였다. 메탄의 자열개질반응에서 촉매의 활성과 안정성을 향상시키기 위해 알루미나가 코팅된 금속 모노리스를 사용하였으며, 금속모노리스 촉매체는 높은 반응온도에서 분말형태의 촉매에 비해 높은 메탄 전환율을 나타내었다. 자열개질반응에 있어서 $H_2O/CH_4/O_2$의 비는 전환율에 영향을 미치는 중요한 변수임을 알 수 있었다. $H_2O/CH_4$ 비가 증가함에 따라 수소 수율은 증가되고, 또한 $O_2/CH_4$ 비가 증가함에 따라 메탄 전환율은 증가하지만 수소 수율은 감소하였다. $Ni/CeO_2-ZrO_2$ 촉매에 0.5 wt%의 귀금속 촉매인 Ru 첨가로 인해 낮은 반응온도에서 촉매 활성이 향상되었다.