“…In the investigation of metal-support interaction of Ni-based catalysts for TRM (reaction conditions: tubular reactor, at 800 • C, 1 bar, GHSV = 17,220 mL h − 1 g − 1 , molar ratio of CH 4 :CO 2 :H 2 O:O 2 : N 2 = 1:0.23:0.46:0.07:0.28, TOS = 10 h), Kumar et al [51,52] reported that the Ni/SBA-15 possessed excellent resistance towards carbon deposition and great confinement governing the TRM performance with time-on-stream but re-oxidation of partial metallic Ni to NiO was unavoidable, as evidenced by XRD analyses. Such observation is in accordance with the findings of Kim et al in their study of TRM over NiCe@SiO 2 catalysts [77]. The TRM reaction was carried out in a fixed bed reactor at atmospheric pressure, using 75 mg catalyst, GHSV of 60, 000 mL g − 1 h − 1 at different O/M feed molar ratios, TOS of 20 h. They assigned the deactivation of NiCe@SiO 2 to re-oxidation of the metallic Ni form deteriorating the multi-yolk-shell nanotube configuration under high feed ratio of oxidizing agents.…”