4.6 Article

Structure Characteristics and Removal Behavior of the Deposited Carbon on Ni-Al2O3 Catalyst for CO2 Reforming of CH4

Journal

PROCESSES
Volume 11, Issue 10, Pages -

Publisher

MDPI
DOI: 10.3390/pr11102968

Keywords

CO2 reforming of CH4; Ni-Al2O3 catalyst; carbon deposition and removal

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This study investigated the composition and structure characteristics of deposited carbon on four catalysts using various techniques. Filamentous carbon was found to be the main deposition type, which could block the catalyst pores and affect the catalytic performance. The carbon deposited on the catalyst prepared using the hydrothermal-precipitation method exhibited a high degree of graphitization, which was harmful to the catalyst stability. The decarburization temperature of the deposited carbon on the four catalysts was mainly in the range of 500-700 degrees C.
Four catalysts were prepared in our previous work using the solution combustion method, incipient-wetness impregnation method, colloid mill circulating impregnation method, and hydrothermal-precipitation method, respectively, labeled as SCM, IMP, T310, and HTP. And the performance (stability) of the four catalysts for CO2 reforming of CH4 was investigated at 800 degrees C. In this paper, the composition and structure characteristics of the deposited carbon on the above four catalysts were tested through TEM, Raman, TPH, and TG-DTG technologies. The results showed that filamentous carbon was the primary type of carbon deposition on the catalysts, and a large amount of accumulated carbon would block the catalyst pores, affecting the catalytic performance. The carbon deposited on the catalyst prepared using the hydrothermal-precipitation method calcined at 800 degrees C exhibited a high degree of graphitization, and the proportion of graphitized carbon was considerable, which is harmful to the stability of the catalyst. The decarburization temperature of the deposited carbon on the four catalysts was mainly in the range of 500-700 degrees C. Using the Coats-Redfern model, as the reaction order was set as 1, 2, 3, 4, and 5, the decarburization activation energy ranged between 50 and 80 kJ/mol.

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