“…(3) intensification of process owing to the integration of different steps in a small-scale device; (4) enhancement of surface area to volume ratio owing to extremely high intensification; (5) high reactant conversion or low reaction temperature owing to thermodynamic equilibrium shifting resulting from the removal of specified products from reacted mixture; and (6) high selectivity of the achieved product owing to optimized reactant distribution resulting from the addition of specified reactants in a controllable way (Alfadhel & Kothare, 2005;Gallucci, Fernandez, Corengia, & Van Sint Annaland, 2013;Jensen, 1999;Kim, Kellogg, Livaich, & Wilhite, 2009;Kolb, 2013;Kothare, 2006;Tan & Li, 2013). Among versatile MMRs, those with a hydrogen separation function are being investigated and have found a number of applications such as hydrogen production from WGS, hydrogen production from methanol steam reforming (MeOHSR), onboard fuel processing for portable PEMFCs, production of moisture-free formaldehyde by the dehydrogenation of methanol, and dehydrogenation of cyclohexane to benzene (Alfadhel & Kothare, 2005;Allen, Irving, & Thomson, 2000;Franz, Schmidt, & Jensen, 1999;Karnik, Hatalis, & Kothare, 2003;Mauer, Claivaz, Fichtner, Schubet, & Renken, 2000;Zheng, Jones, Fang, & Cui, 2000).…”