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Ceramic Foam Catalyst Substrates for Diesel Oxidation Catalysts: Pollutant Conversion and Operational Issues

机译:用于柴油氧化催化剂的陶瓷泡沫催化剂底物:污染物转换和操作问题

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In the field of automotive exhaust catalysts, foam-type substrates have been proposed as alternatives to the well-established honeycomb substrates. The ceramic foams developed and manufactured in our laboratory are capable of redistributing the flow of exhaust gases, enhancing turbulence, mass transfer and species mixing, without increasing flow resistance and pressure drop to prohibitive levels. Based on the characteristics of turbulent mass and heat transfer, ceramic foam based catalysts have the potential for achieving similar pollutant conversion performances as state of art honeycomb catalysts with substantially lower precious metal requirements. In this paper we demonstrate this potential with a small Diesel powered Heavy Duty truck with a ceramic foam Diesel Oxidation Catalyst (DOC). Given the substantial differences in geometrical properties between foams and honeycombs a direct comparison with equal coating thickness, amount and precious metal amount is not feasible. We present however systematic comparisons with known precious metal amounts while pointing out important differences in the wash coating characteristics. As strongly affected, crucial operational characteristics we comment on, are the pressure drop and the homogenizing properties of the substrates on the temperature distribution. For the DOC applications we compared catalysts with an overall volume ratio of 1.4:1 (honeycomb: foam). The comparisons involved the serial production honeycomb to specifically coated foams. Here the wash coat amounts have been chosen in order to achieve almost equal layer thicknesses (wash-coat amount ratio of 6.5:1, honeycomb: foam). The entire precious metal load on the foam was approx. 2.8 times less than the corresponding one on the compared honeycomb. The conversion performances achieved with the foam catalyst were almost equal to those achieved by the honeycomb in respect to CO and THC oxidation, although honeycombs had 2.8 times more precious metals. In addition, the foams exhibited substantially better particle oxidizing behavior, as particle number measurements have shown. Nevertheless, NO oxidation light-off performance of the foams was worse. This may be attributed to different wash coat compositions, the wash coat composition of the serial production honeycomb was not fully known. The comparison of two differently coated foam DOCs have given insights in the conversion dependencies on the coating parameters and have shown further optimization directions.
机译:在汽车排气催化剂领域中,已经提出了泡沫型衬底作为良好建立的蜂窝基材的替代品。在我们的实验室中开发和制造的陶瓷泡沫能够重新分配废气流动,增强湍流,传质和物种混合,而不会增加流动阻力和压力降至过度水平。基于湍流质量和传热的特点,陶瓷泡沫基催化剂具有实现与最大贵金属要求的蜂窝状催化剂相似的污染物转化性能的可能性。在本文中,我们用陶瓷泡沫柴油氧化催化剂(DOC)用小柴油动力重型卡车展示了这种潜力。鉴于泡沫和蜂窝之间的几何特性的显着差异,与相等涂层厚度的直接比较,量和贵金属量是不可行的。然而,我们呈现出具有已知贵金属的系统性比较,同时指出洗涤涂层特性的重要差异。受到强烈影响,我们评论的至关重要的操作特征,是对温度分布的压降和均化性质。对于DOC应用,我们将催化剂与总体积比为1.4:1(蜂窝:泡沫)进行比较。比较涉及串联生产蜂窝,专门涂覆的泡沫。这里已经选择了洗涤涂层的量以实现几乎等于层厚度(洗涤涂层含量为6.5:1,蜂窝状:泡沫)。泡沫上的整个贵金属负载约为。比相实的蜂窝体上的相应少2.8倍。泡沫催化剂所达到的转化性能几乎等于蜂窝与CO和THC氧化而实现的那些,尽管蜂窝状的贵金属具有2.8倍。此外,泡沫表现出基本上更好的颗粒氧化行为,因为颗粒数测量显示。然而,没有泡沫的氧化脱离性能差。这可能归因于不同的洗涤涂层组合物,连续生产蜂窝的洗涤涂层组合物不完全已知。两个不同涂覆的泡沫文档的比较在涂层参数上给出了转换依赖性的见解,并且已经示出了进一步的优化方向。

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