“…For example, the conversion activity of catalyst B75 operated at 380−400 °C is in the range of 30.6−38.9 mmol (N 2 O)/g·h (GHSV = 21 200 h -1 , N 2 O = 10 mol % balanced with He), compared to that of 1.6−2.3 mmol (N 2 O)/g·h (GHSV = 30 000 h -1 , N 2 O = 0.1 mol % balanced with He) for an active Co−Mg−Al spinel catalyst (which was derived from the hydrotalcite-like compound Co−Mg−Al HTlc) operated at 350−400 °C. , It has been evidenced that decomposition of nitrous oxide on metal oxide surface involves an electron transferring from a low oxidation state metal cation to an adsorbed nitrous oxide molecule. , Related to the present catalyst system, the following mechanism can be proposed for nitrous oxide decomposition:
where Co 2+ is a divalent cobalt surface species and Co 2+ ···ON 2 represents adsorbed nitrous oxide species on an active site (eq 4). For many metal oxide catalysts, charge transfer from a low-valence metal cation to the adsorbed N 2 O is often considered as fast surface reaction, as proposed in eq 5. , Due to the site inversion in the spinel structure, as addressed in the above subsections, divalent Co 2+ and trivalent Co 3+ both exist in tetrahedral sites, in addition to the Mg 2+ . Unlike a proposed mechanism that the charge-transfer process of Co 2+ to Co 3+ causes the CoO phase to change to Co 3 O 4 , the coexistence of Co 2+ and Co 3+ in 4-fold-coordinated sites requires little geometrical change for the two types of cations in the charge-transfer process.…”