“…In particular, a list of these catalysts includes different metals such as platinum, silver, cobalt, palladium, and manganese, − as well as different oxides and salts. , Manganese oxides, in particular, have shown the greatest activity in promoting this reaction. − As mentioned before, the use of a heterogeneous catalyst is particularly favorable for continuous operations. Moreover, this operation could be advantageously intensified by using microreactors with a catalytic coating deposited on their walls. − The two dominant methods of embedding a heterogeneous catalyst in a microflow reactors is by coating the walls [with wash-coating being the most prominent technique, although physical vapor deposition (PVD), , chemical vapor deposition (CVD), , sol–gel processing, ,− and others are also used] and by forming small, preferably uniform, beads or grains into a tight assembly, which constitutes a mini-fixed reactor with open voids whose internal dimensions are commonly in the micrometer range and form a three-dimensional channel network. These concepts represent generically different ways to overcome heat- and mass-transfer limitations and to cope with pressure loss and residence time distributions, and the manufacture of such catalysts, on an industrial scale, is also projected to have very different costs.…”