• Title/Summary/Keyword: Washcoating

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Catalytic combustion of $H_2$/Air mixture using Pt/$Al_2O_3$ coated nickel foam (Pt/$Al_2O_3$가 코팅된 니켈폼을 이용한 수소-공기 예혼합 기체의 촉매 연소)

  • Jin, Jung-Kun;Kwon, Se-Jin
    • 한국연소학회:학술대회논문집
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    • 2007.05a
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    • pp.37-44
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    • 2007
  • A nickel foam, one of metal foams was seleced as a catalyst support instead of conventional ceramic materials. $Al_2O_3$ was coated on the surface of nickel foam to increase the surface area. $Al_2O_3$ coating process was based on sol-gel process. SEM image was obtained and $Al_2O_3$ coverage was confirmed. Combustion experiments were carried out using SUS combustor and $H_2$/air mixture. Temperatures were measured with different equivalence ratios and $H_2$ flow rates. $H_2$ conversion rates were calculated by the analysis of product gas using gas chromatography. Catalytic combustion of $H_2$ was complete and stable with Pt/$Al_2O_3$ coated nickel foam and influences of water vapor were confirmed during the beginning of combustion.

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Fabrication and Performance Test of MEMS Catalytic Combustors Using Photosensitive Glass Wafer (감광유리를 이용한 MEMS 촉매 연소기의 제작 및 성능 평가)

  • Jin, Jung-Kun;Kwon, Se-Jin
    • Transactions of the Korean Society of Mechanical Engineers A
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    • v.33 no.3
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    • pp.237-242
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    • 2009
  • MEMS catalytic combustors were fabricated to use in micro-power sources as a heat source. The combustor was fabricated by photolithography and anisotropic wet etching of photosensitive glass wafers. Two different catalyst loading methods were used to complete the fabrication of the combustors. For thin film type, the $Al_2O_3$ was washcoated on the surface of the combustion chamber as a catalyst support, and for packed-bed type, ceramic foam was inserted after Pt was coated. The volume of the combustors was 1.8 $cm^3$ and 16W of heat was generated using the fabricated combustors with hydrogen. The energy density of combustor was about 8.9 W/$cm^3$.

Conversion and Aging Characteristics of Oxidation Catalyst for Natural Gas Vehicle with Lean-burn System (린번 천연가스자동차용 산화촉매의 정화 및 열화특성)

  • 최병철;윤성식;정종우
    • Transactions of the Korean Society of Automotive Engineers
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    • v.11 no.2
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    • pp.134-139
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    • 2003
  • This study was carried out to investigate the aging and conversion characteristics of oxidation catalysts for a natural gas vehicle with lean-bum system. The conversion of $CH_4$ was observed over the various composition ratio of PMs(Precious metals) and washcoating methods. On the fresh catalysts, Pd affected on the activity of $CH_4$ at low temperature more than other PMs in Pd-only and Rh/Pd/Pt catalysts. The activity at low temperature increased as a mount of Pd increases. On the aged catalysts, the $CH_4$ conversion efficiency of Pd-only catalyst with mono-layer washcoat decreased more than that of the other catalysts of $CH_4$ conversion. It was observed that the thermal durability of Rh/Pd/Pt catalysts with double-layer washcoat was better than the single washcoat catalyst.

Effect of Additives on Catalytic Activity in Thermal Catalytic De-NOx Process (Thermal catalytic de-NOX 공정에서 첨가제가 촉매의 활성에 미치는 영향에 관한 연구)

  • 이진구;김태원;최재순;김정호;이재수;장경욱;박해경
    • Journal of Korean Society for Atmospheric Environment
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    • v.15 no.3
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    • pp.249-255
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    • 1999
  • We sdudied effect of additives on catalytic activity in thermal catalytic de-NOx process which was composed of thermal reduction, catalytic reduction and catalytic oxidation stage. Pd-Pt/${\gamma}$-$Al_2O_3$ catalysts with the addition of transition metals(Co, Cu, Fe, Ni, W, Zn, Zr) and rare earth metals(Ce, Sr) were prepared by the conventional washcoating method. Those catalysts were characterized by CO pulse chemisorption, ICP, $N_2$ adsorption, SEM and XRD. The effect of catalyst additives on NOx removal for diesel emission was studied in thermal catalytic de-NOx process at reduction temperature(350~50$0^{\circ}C$), space velocity(5,000~20,000 $hr^{-1}$) and the engine load(0~120kW). The concentraton of CO, $CO_2$, NO and $NO_2$ in the exhaust gas increased with the engine load. On the other hand the concentration of $O_2$ decreased. The de-NOx activityof all prepared catalysts increased with respect to high CO and low $O_2$ level in the thermal reduction stage of the process. Insertion of Ce to Pt-Pd/${\gamma}$-$Al_2O_3$ catalyst showed the best activity of all the catalysts under these experimental conditions. De-NOx catalysts are effective to remove CO in addition to NOx in the catalytic reduction stage.

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De-NOx Characteristics for Cu-ZSM5/Alumina Beads Catalyst Filter in Urea-SCR System (Urea-SCR 시스템에서의 Cu-ZSM5/알루미나 비드 촉매필터의 De-NOx 특성)

  • Jang, Young-Sang;Shin, Young-Seop;Lee, Byoung-Jun;Park, Jai-Koo
    • Transactions of the Korean Society of Automotive Engineers
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    • v.16 no.5
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    • pp.60-67
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    • 2008
  • The catalytic filter of Cu-ZSM5/alumina beads was considered to reduce NOx in the urea SCR system. Catalytic support of porous alumina beads with mean pore size $130{\mu}m$ and porosity $75{\sim}83%$ were prepared using foaming and gel-casting method. The Cu-ZSM5 catalysts were coated on the supporting alumina beads using $Cu(NO_3)_2$ by ion exchange method. After a washcoating process was applied to coat 10w% Cu-ZSM5 on porous alumina bead, coating layer was estimated $20{\mu}m$ in thickness. The characterization and the feasibility as a catalytic supports were investigated. And the NOx conversion test in Cu-ZSM5/Alumina Beads filter system was conducted by using Urea as reductants under laboratory test. The NOx conversion was increased as size and porosity of beads and observed more than 95% excellent NOx conversion above $300^{\circ}C$.

Endothermic Properties of Liquid Fuel Decomposition Catalyst Using Metal Foam Support (메탈폼 지지체를 이용한 액체연료 분해반응 촉매의 흡열특성)

  • Mun, Jeongin;Kim, Nari;Jeong, Byunghun;Jung, Jihoon
    • Korean Chemical Engineering Research
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    • v.59 no.4
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    • pp.481-486
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    • 2021
  • In a hypersonic vehicle to solve the heat problem generated during flight, a cooling technology is being developed which uses the endothermic effect that appears during the decomposition reaction of the mounted fuel. In this study, the decomposition reaction of n-dodecane fuel was performed using HZSM-5 as a catalyst, and the catalyst was coated on metal foam to maximize the endothermic effect of the catalytic decomposition reaction and suppress coke formation. The reactor was a stainless steel flow reactor with a outer diameter of 1.27 cm, and the reaction temperature was 550 ℃, the reaction pressure was 4 MPa, and the flow rate was 12 ml per minute. As a result of the catalytic decomposition reaction using a catalyst coated with HZSM-5 on the metal foam, the heat sink was 2887 kJ/kg as a maximum, the gas phase conversion rate was 34%, and the amount of coke produced on the metal foam decreased by about 56% as the catalyst was coated compared to the uncoated catalyst.

A Study on the NOx Reduction According to the Space Velocity Variation and Binder Content of Metal foam SCR Catalyst for Cogeneration Power Plant Application (열병합발전소 적용을 위한 Metal foam SCR촉매의 공간속도와 바인더 함량에 따른 NOx 저감에 관한 연구)

  • Na, Woo-Jin;Park, Hea-Kyung
    • Journal of the Korean Applied Science and Technology
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    • v.36 no.1
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    • pp.153-164
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    • 2019
  • To develop a high performance SCR catalyst which has better specific surface area, lightness of weight and fast temperature response than those of existing commercial SCR catalyst, metal foam type SCR catalysts were prepared by washcoating with vanadium, tungsten and binder. The de-NOx performance test of the prepared catalysts was carried out on atmospheric micro-test unit at lab. scale according to space velocity variation and temperature change, and the characteristics of them were analyzed by Porosimeter, SEM(scanning electron microscope), EDX(energy dispersive x-ray spectrometer), ICP(inductively coupled plasma) and Stereomicroscope. The NOx reduction performance decreased as the space velocity increased and was found to be the best at 3.5 wt.% contents of the vanadium and tungsten. It was found that the larger amount of binder was added, the worse the NOx reduction performance was, which was considered to be that the number of active sites of the prepared catalyst surface was occupied by the binder. We found that the amount of binder to be added to prepare the catalyst should be properly controlled by the condition of coated catalyt surface.