A method for the assessment of the optimal operating conditions for a
mechanically stirred gas-liquid reactor is presented. The method explo
its both fluid dynamic and chemical information. First, the behavior o
f the specific stirring power as a function of the stirrer speed allow
s singling out the dispersion region, in which the most efficient gas-
liquid mass transfer is achieved. Inside this region, the analysis of
experimental data obtained when considering a chemical system reacting
at moderate Hatta numbers (i.e., Ha < about 2) allows determination o
f the rate constants and the fluid dynamic parameters (i.e., the mass
transfer coefficient in the absence of chemical reaction and the chara
cteristic diffusion time).