用于CO低温氧化的铜基混合氧化物催化剂(CuMnCe、CuMnCo和CuCeZr)

Subhashish Dey , Devendra Mohan , Ganesh Chandra Dhal , Ram Prasad
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引用次数: 45

摘要

CuMnCe、CuMnCo和CuCeZr催化剂的混合金属氧化物中的表面富集效应对CO氧化非常有效。本工作描述了CuMnCe、CuMnCo和CuCeZr催化剂的制备以及用于获得催化剂结构和活性信息的表征技术。在催化剂中,CuMnCe和CuMnCo是通过共沉淀法制备的,另一种催化剂CuCeZr是通过反应研磨法制备的。在各种混合金属氧化物催化剂中,CuMnCe被认为是最有效的高活性催化剂。在CuMnOx催化剂中添加二氧化铈也提高了时效处理后的中孔/大孔体积和表面积,从而提高了催化剂的活性和稳定性。前体反应煅烧(RC)的一种新途径是合成高活性催化剂。XRD、SEM-EDX、XPS、BET和FTIR表征表明,新型催化剂在CO氧化中比传统催化剂(通过在停滞空气和流动空气中煅烧前体获得)具有惊人的活性,这与不寻常的形态有关。通过各种前体的RC获得的催化剂显示出对CO氧化的最高活性,其顺序为:CuMnCe>;CuCeZr>;CuMnCo和传统的煅烧路线也遵循相同的活性顺序。此外,通过各种煅烧条件获得的催化剂的活性顺序如下:RC>;流动的空气>;停滞的空气。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

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Copper based mixed oxide catalysts (CuMnCe, CuMnCo and CuCeZr) for the oxidation of CO at low temperature

The effect of surface enrichment in mixed metal oxides of CuMnCe, CuMnCo, and CuCeZr catalysts is highly effective for CO oxidation. The present work describes the preparation of CuMnCe, CuMnCo and CuCeZr catalysts and the characterization techniques applied to gain information about the catalyst structure and activity. Among the catalysts, CuMnCe and CuMnCo were prepared by the co-precipitation method and another catalyst CuCeZr was prepared by the reactive grinding method. In the variety of mixed metal oxide catalysts, CuMnCe was considered to be the most effective for high activity. The addition of ceria in CuMnOx catalyst has also improved the activity and stability due to increasing the meso/macropore volume and surface area after aging treatment. A novel route of reactive calcination (RC) of the precursor was the synthesis of highly active catalyst. The amazing activity of the novel catalysts over the conventional ones (obtained by calcination of the precursors in stagnant air and flowing air) in CO oxidation was associated with the unusual morphology as evidenced by XRD, SEM-EDX, XPS, BET and FTIR characterization. The catalysts obtained by RC of various precursors showed the highest activity for CO oxidation in the following order: CuMnCe > CuCeZr > CuMnCo and the traditional route of calcination also followed the same activity order. Further, the activity order of the catalysts obtained by various calcination conditions was as follows: RC > flowing-air > stagnant-air.

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