Hydrogen-rich gas production from tar model compound disintegrates over low-temperature plasma in dielectric barrier discharge reactor.

Hydrogen-rich gas production from reforming of naphthalene as a typical tar model compound was investigated under catalytic, plasma and plasma-catalytic systems. The effect of Gd promoter and solvent on naphthalene decomposition and gaseous products within the reforming reaction was studied. The catalysts were prepared by the thermal fusion method and characterized by XRD, XPS, SEM, BET, TEM, TG and H 2 -TPR. Compared to catalytic systems and plasma systems, the plasma-catalytic system shows the highest naphthalene conversion, as well as highest yield of hydrogen-rich gas on account of the synergetic effect of plasma and catalyst. Ni–Gd/SiO 2 @Al 2 O 3 catalyst exhibits superior catalytic activity than that on Ni/SiO 2 @Al 2 O 3 , due to higher dispersity of nickel species and reducibility of catalysts, as well as more Ni0 species and more surface oxygen species. No sintering and no coke formed on the fusion used catalyst owing to low content and high dispersion of nickel species. Maximum both naphthalene conversion and H 2 yield were observed on Ni-10Gd catalyst, about 89 % and 0.17 mol/mol-naphthalene, respectively. Furthermore, the presence of OH· radicals originating from methanol and the subsequent methanol reforming reaction play a pivotal role in augmenting naphthalene conversion and facilitating the formation of H 2 , CO, and CH 4. [Display omitted] • Ni-10Gd catalyst showed the highest conversion in plasma reforming of naphthalene owing to synergetic effect. • Gd enhances the dispersity and reducibility of catalyst, Ni0 species and surface oxygen species, as well as the naphthalene disintegrates. • Fusion catalysts exhibited high resistance to carbon deposition and sintering. • More OH· radicals in methanol contribute to the activity in plasma-catalytic system. [ABSTRACT FROM AUTHOR]