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Impact of Zeolite Beta on Hydrocarbon Trapping and Light-Off Behavior on Pt/Pd/BEA/Al_2O_3 Monolith Catalysts

机译:β沸石对Pt / Pd / BEA / Al_2O_3整体催化剂上碳氢化合物截留和起燃行为的影响

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The impact of large-pore zeolite beta (BEA) on the performance of model monolithic Pt/Pd/Al_2O_3 diesel oxida-tion catalyst is investigated in terms of hydrocarbon (HC) storage capacity, light-off, and oxidation. Dodecane (C12) is employed as the model HC to elucidate BEA loading impact on catalyst performance during temperature-programmed ox-idation of CO and C12 and mixtures in the absence of feed water. A C12 pre-storage experiment protocol quantifies stor-age at room temperature, the effect of C12 storage on light-off temperature, and the extent of release and conversion of C12. The temperature ramp experiments indicate a negligible im-pact of the zeolite on the individual reactant (CO and C12) light-offs. Co-feed experiments (HC + CO simultaneous feed) reveal light-off inhibition by CO and C12 in addition to that by pre-stored C12. This trend is consistent for all zeolite load-ing levels. During both co-feed and C12 pre-storage experi-ments, an intermediate zeolite loading results in a decreased CO light-off temperature when compared to the zeolite-free catalyst. This beneficial effect is attributed to the zeolite pro-viding alternative storage sites for the HC, thereby mitigating the inhibition on the CO light-off by freeing up precious metal sites for CO oxidation. However, the highest zeolite loading catalyst has an increased CO light-off temperature in C12 pre-storage experiments compared to the catalyst with intermedi-ate loading. This trend reversal is attributed to the kinetic and/ or transport inhibitory effect of stored C12 which overcomes the enhancement at lower loadings. The data indicate that the highest zeolite loading yields the highest percentage of stored C12 converted to CO_2, a finding relevant for HC trap catalyst design. The study findings suggest a need to optimize the zeolite loading for the desired operating conditions to achieve desired light-off and HC trapping and conversion. The impact of feed water will be investigated in future work to evaluate the generality of these findings.
机译:从碳氢化合物(HC)的储存容量,起燃和氧化方面研究了大孔沸石β(BEA)对模型整体Pt / Pd / Al_2O_3柴油氧化催化剂性能的影响。十二烷(C12)被用作HC模型,以阐明在没有给水的情况下,在CO和C12以及混合物的温度程序化氧化过程中,BEA负载量对催化剂性能的影响。 C12预存储实验协议可量化室温下的存储时间,C12存储对起燃温度的影响以及C12释放和转化的程度。温度上升实验表明,沸石对单个反应物(CO和C12)起燃的影响可忽略不计。共同进料实验(HC + CO同时进料)显示,除了预先存储的C12之外,CO和C12还具有起燃抑制作用。对于所有沸石加载水平,这种趋势都是一致的。与不含沸石的催化剂相比,在共进料和C12的预贮藏试验中,中等的沸石负载量会降低CO起燃温度。这种有益的作用归因于沸石为HC提供了替代的储存位点,从而通过释放了贵金属位点用于CO氧化,从而减轻了对CO起燃的抑制作用。但是,与具有中等负载量的催化剂相比,在C12预存储实验中,最高沸石负载量的催化剂的CO起燃温度更高。这种趋势的逆转归因于储存的C12的动力学和/或运输抑制作用,该作用克服了较低负荷下的增强作用。数据表明,最高的沸石负载量可将转化为CO_2的最高储存C12百分比转化为碳,这与HC捕集阱催化剂设计有关。研究发现表明需要针对所需的操作条件优化沸石负载量,以实现所需的起燃以及HC捕集和转化。在以后的工作中将对给水的影响进行研究,以评估这些发现的普遍性。

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