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

Figure 3

Catalytic activity in terms of (a) rate of H₂ formation at constant CO₂ partial pressure (43.42 kPa), (b) rate of CO formation at constant CO₂ partial pressure (43.42 kPa), (c) rate of H₂ formation at constant CH₄ partial pressure (43.42 kPa), (d) rate of CO formation at constant CH₄ partial pressure (43.42 kPa),(e) rate of H₂O formation at constant CO₂ partial pressure (43.42 kPa), and (f) rate of H₂O formation at constant CH₄ partial pressure (43.42 kPa).

(a)

(b)

(c)

(d)

(e)

(f)