“…As explained in [2] the flowrates of ethanol and water at the reactor entrance (F C2H5OH , F H2O ), the temperature of the entering mixture (T gas,e ), and the temperatures of the furnaces of the three reforming stages (T F,S1 , T F,S2 , T F,S3 ) have been considered as inputs. As outputs to be controlled we have considered the flowrates of H 2 and CO (F H2 and F CO ) at the output of the reformer.…”