Figure 3: Temperature-dependent catalytic performance.
From: Non-syngas direct steam reforming of methanol to hydrogen and carbon dioxide at low temperature
(a) A plot of catalytic performance, gas content and CO selectivity (and concentration), against reaction temperature for steam reforming of methanol by CuZnGaOx; (b) Thermodynamic calculations (reaction conditions: 0.40 g cat.+0.40 g SiC; liquid feed of CH3OH:H2O=1: 2 at 0.01 ml min−1; N2 carrier at 10 ml min−1; varying temperature).
