• 제목/요약/키워드: Monolith catalyst

검색결과 57건 처리시간 0.022초

NI/$MgAl_2O_4$코팅된 금속 모노리스 촉매의 수소 생산을 위한 천연가스 수증기 개질 반응특성에 관한 연구 (The Performance of NI/$MgAl_2O_4$ Coated Metal Monolith in Natural Gas Steam Reforming for Hydrogen Production)

  • 최은정;구기영;정운호;이영우;윤왕래
    • 한국수소및신에너지학회논문집
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    • 제21권6호
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    • pp.500-506
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    • 2010
  • The metal monolith catalyst coated with 15wt% Ni/$MgAl_2O_4$ is applied to the natural gas steam reforming for hydrogen production. To address the improvement of adherence between metal monolith and catalyst coating layer, the pre-calcination temperature as well as the coating conditions of $Al_2O_3$ sol are optimized. When the Fe-Cr alloy monolith is pre-calcined at $900^{\circ}C$ for 6 h, $Al_2O_3$ layer was formed uniformly on the entire surface of the metal substrate. It is seen that the formation of $Al_2O_3$ layer on the monolith surface is essential for the uniform coating of $Al_2O_3$ sol onto the monolith substrate. The monolith catalyst coated with 10wt% $Al_2O_3$ sol shows high $CH_4$ conversion and good thermal stability as compared with the monolith catalyst without $Al_2O_3$ sol coating under severe reaction conditions with high GHSV of 30,000 $h^{-1}$ at $700^{\circ}C$. In addition, the metal monolith catalyst shows higher catalytic activity and better thermal conductivity than 15wt% Ni/$MgAl_2O_4$ pellet catalyst.

제철소 적용을 위한 저온형 금속지지체 탈질 코팅촉매 최적화 연구 (An Optimization Study on a Low-temperature De-NOx Catalyst Coated on Metallic Monolith for Steel Plant Applications)

  • 이철호;최재형;김명수;서병한;강철희;임동하
    • 청정기술
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    • 제27권4호
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    • pp.332-340
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    • 2021
  • 최근 사업장 질소산화물(NOx) 배출허용기준 강화(2019년 1월 적용)에 따라 다량 배출사업장에서 배출되는 질소산화물을 배출허용기준 이하로 만족하기 위한 노력이 필요하다. 대표적인 질소산화물 저감 방법으로 선택적 촉매 환원법(selective catalytic reduction, SCR)을 주로 사용하고 있으며, 일반적으로 세라믹 허니컴(ceramic honeycomb) 촉매를 사용하고 있다. 본 연구에서는 높은 열적 안정성과 기계적 강도를 가지는 금속지지체 탈질 코팅촉매를 적용하여 제철소에서 배출되는 질소산화물를 저감하기 위한 연구를 수행하였다. 금속지지체 코팅촉매는 최적화된 촉매슬러리(catalyst slurry) 코팅방법을 통해 제조하였고, 내마모 시험과 굽힙 시험을 통해 코팅된 촉매가 균일하고 강건하게 부착되어 있음을 확인하였다. 금속지지체가 가지는 우수한 열전도 특성으로 인해 저온영역(200 ~ 250 ℃)에서 세라믹 허니컴 촉매보다도 우수한 탈질효율을 보였다. 또한 경제적인 촉매 설계를 위해 금속지지체 표면 상에 코팅되는 촉매의 최적 코팅량을 확인하였다. 이러한 연구결과를 바탕으로 제철소 배기가스 모사환경에서 상용급 금속지지체 코팅촉매에 대한 준파일럿 탈질 성능평가를 수행하였고, 저온영역(220 ℃)에서도 배출허용기준치(60 ppm 이하)을 만족하는 우수한 성능을 나타내었다. 따라서 물리화학적 특성이 우수한 금속지지체 코팅촉매가 최소량의 촉매 사용으로도 우수한 탈질 성능을 나타내었으며, 넓은 비표면적을 가지는 고밀도 금속지지체 적용을 통해 배연 탈질 촉매 반응기의 콤팩트화 및 소형화가 가능하였다. 이러한 결과를 바탕으로, 본 연구에서 사용된 금속지지체 코팅촉매는 제철소뿐만 아니라 화력발전, 소각장, 선박, 건설기계 등 다양한 산업 분야에 적용할 수 있는 새로운 형태의 촉매가 될 것이다.

냉간시동시 자동차용 저온활성촉매의 성능 향상을 위한 수치적 설계 (Numerical Design of Light-off Auto-Catalyst for Reducing Cold-Start Emissions)

  • 정수진;김우승
    • 대한기계학회논문집B
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    • 제24권9호
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    • pp.1264-1276
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    • 2000
  • Light-off catalyst has been used for minimization of cold-start emissions. Improved cold-start performance of light-off catalyst needs the optimal design in terms of flow distribution, geometric surface area, precious metal loading, cell density and space velocity. In this study, these influential factors are numerically investigated using integrated numerical technique by considering not only 3-D fluid flow but also heat and mass transfer with chemical reactions. The present results indicate that uneven catalyst loading of depositing high active catalyst at upstream of monolith is beneficial during warm-up period but its effect is severely deteriorated when the space velocity is above 100,000 $hr^{-1}$ To maximize light-off performance, this study suggests that 1) a light-off catalyst be designed double substrate type; 2) the substrate with high GSA and high PM loading at face be placed at the front monolith; and 3) the cell density of the rear monolith be lower to reduce the pressure drop.

10mm 스케일 촉매 연소기에서의 수소-공기 예혼합 가스의 연소 현상 관찰 (Investigation on Catalytic Combustion of Hydrogen-Air Premixed Gas in 10mm Scale Catalytic Combustor)

  • 최원영;권세진
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2004년도 제29회 KOSCI SYMPOSIUM 논문집
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    • pp.181-186
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    • 2004
  • Catalytic combustion is one of the suitable methods which is applicable to micro heat source due to high energy density and no flame quenching. And hydrogen can be oxidized at room temperature with platinum catalyst. So hydrogen-fueled micro catalytic combustor with platinum catalyst can be good and easy-handling heat source for another micro devices. In this work we focused on general catalytic combustion characteristics of hydrogen-air premixed gas in 10mm scale catalytic combustor for the further application to micro scale. Platinum was coated on dense ceramic monolith which can be installed in simple-structured catalytic combustor. We investigated the effect of flow rate, heat loss and platinum percentage in catalyst-coated monolith on catalytic combustion performance by temperature distribution in the combustor. By those results we confirmed catalytic reactivity and estimated reaction area. And we simulated micro scale catalytic reaction by sliced monolith. The results of this work will be important design factors for micro scale catalytic combustor.

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밀리미터 스케일 촉매 연소기에서의 수소-공기 예혼합 가스의 촉매 연소 특성 (Catalytic Combustion Characteristics of Hydrogen-Air Premixture in a Millimeter Scale Monolith Coated with Platinum)

  • 최원영;권세진
    • 한국연소학회지
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    • 제10권1호
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    • pp.20-26
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    • 2005
  • In the present study, catalytic combustion of hydrogen-air premixture in a millimeter scale monolith coated with Pt catalyst was investigated. As the combustor size decreases, the heat loss increases in proportion with the inverse of the scale of combustion chamber and combustion efficiency decreases in a conventional type of combustor. Combustion reaction assisted by catalyst can reduce the heat loss by decreasing the reaction temperature at which catalytic conversion takes place. Another advantage of catalytic combustion is that ignition is not required. Platinum was coated by incipient wetness method on a millimeter scale monolith with cell size of $1{\times}1mm$. Using this monolith as the core of the reaction chamber, temperatures were recorded at various locations along the flow direction. Burnt gas was passed to a gas chromatography system to measure the hydrogen content after the reaction. The measurements were made at various volume flow rate of the fuel-air premixture. The gas chromatography results showed the reaction was complete at all the test conditions and the reacting species penetrated the laminar boundary layer at the honeycomb and made contact with the catalyst coated surface. At all the measuring locations, the record showed monotonous increase of temperature during the measurement duration. And the temperature profile showed that the peak temperature is reached at the point nearest to the gas inlet and decreasing temperature along the flow direction.

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광촉매 반응치 설계를 위한 기초 연구 (A Fundamental Study for a Photocatalytic Reactor Design)

  • 손건석;윤승원;고성혁;김대중;송재원;이귀영
    • 한국자동차공학회논문집
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    • 제10권2호
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    • pp.40-47
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    • 2002
  • Because UV wavelength lights can activate photocatalysts, plasma is used as a light source of a photocatalytic reactor. Even though plasma has good intensity for photo reaction, substrate of catalyst coating was limited by the geometry of plasma generator. Usually bead type substrate was used for a pack bed type reactor. Honeycomb monolith type substrate was used with UV lamps instead plasma, due to the light penetration the honeycomb monolith length was too short to show good activity In this study a photocatalytic reactor, which is using a honeycomb monolith substrate, was investigated with plasma as an activation light source. As a parametric study the effects of 1311owing factors on plasma generation and power consumption are examined; supply voltage, substrate length, environment condition, catalyst loading and ratio. Using the test results, the practicability test was done with simulated synthetic gases representing bad smells and automotive exhaust gases.

Development of Monolithic Catalyst System with Co-Ru-Zr for CO2 (dry) Reforming of Methane : Enhanced Coke Tolerance

  • Kim, Hyojin;You, Young-Woo;Heo, Iljeong;Chang, Tae-Sun;Hong, Ji Sook;Lee, Ki Bong;Suh, Jeong Kwon
    • 청정기술
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    • 제23권3호
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    • pp.314-324
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    • 2017
  • To verify the viability of Co, Ru and Zr-based catalyst for $CO_2$ (dry) reforming reaction, catalysts were fabricated using cordierite, silicon carbide and rota monolithic substrates, and they were compared with the conventional $Co-Ru-Zr/SiO_2$ catalyst in terms of performance and durability. Cordierite monolith was showed high activity with the least amount of active component. In addition, when Cordierite monolith was coated with Co-Ru-Zr in various ways, most excellent performance was showed at a precursor solution coating method. In particular, when 0.9 wt% Co-Ru-Zr/Cordierite was used for reaction, it was observed that 95% $CO_2$ conversion was maintained for 300 h at $900^{\circ}C$.

CHANGE OF CATALYST TEMPERATURE WITH UEGI TECHNOLOGY DURING COLD START

  • CHO Y.-S.;KIM D.-S.
    • International Journal of Automotive Technology
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    • 제6권5호
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    • pp.445-451
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    • 2005
  • Most of the pollutants from passenger cars are emitted during the cold-transient phase of the FTP-75 test. In order to reduce the exhaust emissions during the cold-transient period, it is essential to warm up the catalyst as fast as possible after the engine starts, and the Unburned Exhaust Gas Ignition (UEGI) technology was developed through our previous studies to help close-coupled catalytic converters (CCC) reach the light-off temperature within a few seconds after cold-start. The UEGI system operates by igniting the unburned exhaust mixture by glow plugs installed upstream of the catalyst. The flame generates a high amount of heat, and if the heat is concentrated on a specific area of monolith surface, then thermal crack or failure of the monolith could occur. Therefore, it is very important to monitor the temperature distribution in the CCC during the UEGI operation, so the local temperatures in the monolith were measured using thermocouples. Experimental results showed that the temperature of CCC rises faster with the UEGI technology, and the CCC reaches the light-off temperature earlier than the baseline case. Under the conditions tested, the light-off time of the baseline case was 62 seconds, compared with 33 seconds for the UEGI case. The peak temperature is well under the thermal melting condition, and temperature distribution is not so severe as to consider thermal stress. It is noted that the UEGI technology is an effective method to warm up the catalyst with a small amount of thermal stress during the cold start period.

세라믹 벌집형 담체를 사용한 광촉매 반응기의 플라즈마 생성에 관한 연구 (A Study of Non-thermal Plasma Generation on a Photocatalytic Reactor Using a Ceramic Honeycomb Monolith Substrate)

  • 손건석;윤승원;고성혁;김대중;송재원;이귀영
    • 한국자동차공학회논문집
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    • 제10권2호
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    • pp.48-54
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    • 2002
  • Since photocatalysts are activated by lights of UV wavelengths, plasma is alternatively used as a light source for a photocatalytic reactor. Light intensity generated by plasma is proportional to the surface area of catalytic material, and this, in many practical applications, is prescribed by the geometry of a plasma generator. Thus, it is crucial to increase the surface area far sufficient light intensity for photocatalytic reaction. For example, in a pack-bed type reactor, multitudes of beads are used as a substrate in order to increase the surface area. Honeycomb monolith type substrate, which has very good surface area to volume ratio, has been difficult to apply plasma as a light source due to the fact that light penetration depth through the honeycomb monolith was too short to cover sufficient area, thus resulting in poor intensity for photocatalytic reaction. In this study, nonthermal plasma generation through a photocatalytic reactor of honeycomb monolith substrate is investigated to lengthen this short penetration depth. The ceramic honeycomb monolith substrate used in this study has the same length as a three way catalyst used fur automotive applications, and it is shown that sufficient light intensity for photocatalytic reaction can also be obtained with honeycomb monolith type reactor.

OPTIMUM DESIGN OF AN AUTOMOTIVE CATALYTIC CONVERTER FOR MINIMIZATION OF COLD-START EMISSIONS USING A MICRO GENETIC ALGORITHM

  • Kim, Y.D.;Kim, W.S.
    • International Journal of Automotive Technology
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    • 제8권5호
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    • pp.563-573
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    • 2007
  • Optimal design of an automotive catalytic converter for minimization of cold-start emissions is numerically performed using a micro genetic algorithm for two optimization problems: optimal geometry design of the monolith for various operating conditions and optimal axial catalyst distribution. The optimal design process considered in this study consists of three modules: analysis, optimization, and control. The analysis module is used to evaluate the objective functions with a one-dimensional single channel model and the Romberg integration method. It obtains new design variables from the control module, produces the CO cumulative emissions and the integral value of a catalyst distribution function over the monolith volume, and provides objective function values to the control module. The optimal design variables for minimizing the objective functions are determined by the optimization module using a micro genetic algorithm. The control module manages the optimal design process that mainly takes place in both the analysis and optimization modules.