A catalytic Pd-Ag membrane reactor has been packed with a Co-Al(2)O(3) catalyst to perform the ethanol steam reforming reaction using a simulated bio-ethanol mixture (H(2)O/C(2)H(5)OH feed molar ratio = 18.7/1). In Part! of this work, low hydrogen recovery (<= 30%) and CO-free hydrogen yield (<= 20%) were obtained. In this second study the influence of higher pressure and sweep-gas flow rate was studied in order to improve the membrane reactor performances in terms of higher ethanol conversion, CO-free hydrogen yield and hydrogen recovery. The counter-current sweep-gas flow configuration was used for studying the effect of the reaction pressure and the sweep factor on the reaction system, while the co-current flow configuration was also considered for analysing the weight hourly space velocity effect. Moreover, a comparison with a traditional reactor working at the same MR operating conditions was also realized. As best results, the membrane reactor showed 100% ethanol conversion, 95.0% CO-free hydrogen recovery and similar to 60.0% CO-free hydrogen yield, operating at 400 degrees C and 3.0 (abs) bar. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.