“…This is mainly because the micro-channel reactors merit a higher surface to volume ratio, which might be several orders of magnitude higher compared to the traditional steam reformer, and hence, the heat and mass transfer inside the micro-reformer can be greatly enhanced (Ehrfeld et al, 2000). To give a basic understanding for the size of the micro-channel reactors, Table 1 gives the dimensions of some existing micro-reformers (Jensen, 2001;Stefanie et al, 1999;Tanaka et al, 2004;Kawamura et al, 2006;Terazaki et al, 2005a;Holladay et al, 2004;Chen et al, 2004). In accordance with the information of this table, it is observed that the total length and the width of the micro-reformers are ranged within 10-80 mm, and its thickness is within 1-10 mm.…”