Abstract

The structural changes of Ni species in Ni/Al 2O 3, Ni/SiO 2, and Ni/TiO 2 catalysts during the repeated cycles of the methane decomposition and the subsequent gasification of deposited carbons with CO 2 have been studied. The catalytic activity for the methane decomposition depended on the size of Ni metal particles; i.e., the particle size from 60 to 100 nm was most effective. The catalytically active Ni species in Ni/SiO 2 were present as Ni metal particles with diameter from 40 to 100 nm at the first reaction cycle, but they were aggregated into ones with diameters larger than 200 nm, resulting in the deactivation of Ni/SiO 2 for methane decomposition. In contrast, catalytic activity of Ni/TiO 2 was kept high during the repeated reactions because the particle size of Ni metal was kept at the optimum size range effective for the methane decomposition. On the other hand, Ni species in a fresh Ni/Al 2O 3 were composed of highly dispersed Ni(II) species and Ni metal particles of a diameter smaller than 20 nm. During the repeated reactions, the Ni(II) species were gradually reduced, forming the fine Ni metal particles, and the fine metal particles were aggregated into ones with a larger diameter, which brought about an increase in the catalytic activity of Ni/Al 2O 3.

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