Kinetic Study of Zirconia-Alumina-Supported Ni-Fe Catalyst for Dry Reforming of Methane: Impact of Partial Pressure and Reaction Temperature

Figure 2

Catalytic activity in terms of (a) CH₄ consumption rate at constant CO₂ partial pressure (43.42 kPa), (b) CO₂ consumption rate at constant CO₂ partial pressure (43.42 kPa), (c) CH₄ consumption rate at constant CH₄ partial pressure (43.42 kPa), and (d) CO₂ consumption rate at constant CH₄ partial pressure (43.42 kPa).

(a)

(b)

(c)

(d)