“…This direct conversion route involves partial oxidation at 300-500 °C under fuel-rich mixtures to minimize the extent of the more thermodynamically favourable combustion reaction which produces unwanted CO and CO 2 (Zhang et al, 2003;Navarro et al, 2006;Alvarez-Galvan et al, 2011). Several reviews which provided valuable discussions of various aspects of, and the progress already made in, the direct partial oxidation of methane to methanol and other oxygenates have been published (Foster, 1985;Gesser et al, 1985;Edwards & Foster, 1986;Pitchai & Klier, 1986;Fujimoto, 1994;Yang et al, 1997;Adebajo, 1999;Lunsford, 2000;Tabata et al, 2002;Zhang et al, 2003;Taniewski, 2004;de Vekki & Marakaev, 2009;Holmen, 2009;Alvarez-Galvan et al, 2011). The selective partial oxidation of methane has been carried out in four ways, namely high temperature non-catalytic gas-phase homogeneous oxidation, heterogeneous catalytic oxidation, low temperature homogeneous catalysis in solution and enzymatic or biological catalytic oxidation (Zhang et al, 2003;Holmen, 2009).…”