catalysts. Experimental tests were carried out for temperatures between 400 and 550° C and
pressures between 1 and 7 bar, using methane and simulated biogas (1: 1 methane-carbon
dioxide mixture) as carbonaceous feed. The results were analyzed with a simplified reaction
rate expression. The parameters of such expression were optimized in order to provide a
tool for the design of an industrial scale reactor using the catalysts considered.