Monomeric Cu II sites supported on alumina, prepared using surface organometallic chemistry,c onvert CH 4 to CH 3 OH selectively.T his reaction takes place by formation of CH 3 Os urface species with the concomitant reduction of two monomeric Cu II sites to Cu I ,a ccording to mass balance analysis,i nfrared, solid-state nuclear magnetic resonance,X -ray absorption, and electron paramagnetic resonance spectroscopys tudies.T his material contains as ignificant fraction of Cu active sites (22 %) and displays as electivity for CH 3 OH exceeding 83 %, based on the number of electrons involved in the transformation. These alumina-supported Cu II sites reveal that C À Hbond activation, along with the formation of CH 3 O-surface species,c an occur on pairs of proximal monomeric Cu II sites in as hort reaction time.The main constituent of natural gas,C H 4 ,i si ncreasingly produced by fracking and is widely available at extraction sites for fossil fuels.T ransport of CH 4 as liquefied natural gas is,however,expensive and energy intensive;hence,itisoften flared despite the consequent highly negative environmental impacts and loss of resource.F inding efficient routes to convert CH 4 to liquid fuels or chemicals on-site is,therefore, of significant economic and environmental importance.A s such, direct conversion of CH 4 to CH 3 OH is noteworthy since it provides al iquid that can be directly used as ac hemical feedstock, fuel, or fuel additive.H owever,t his process remains ag rand challenge because over-oxidation is favored by the higher reactivity of CH 3 OH compared to CH 4 . [1][2][3][4][5] In nature,bacterial enzymes such as methane monooxygenases, are able to oxidize CH 4 to CH 3 OH with high selectivity using O 2 as the primary oxidant. [6] These enzymes,containing Cu or Fe metal centers,have inspired the design of materials for the conversion of CH 4 to CH 3 OH under mild reaction conditions. [7] Attempts to perform this reaction catalytically with tailored materials have mostly been unsuccessful because the selectivity toward CH 3 OH is low at high CH 4 conversion. This hurdle can, in principle,b eo vercome using the concept of chemical looping,w hich entails decoupling the steps of oxidation of Cu sites and their reaction with CH 4 . [8] Thel ast step of the cycle utilizes aprotic solvent to desorb the CH 3 Ospecies that are strongly bound to the copper sites.O ft he various systems that have been investigated, Cu-exchanged zeolites have shown potential for the selective oxidation of CH 4 to CH 3 OH using molecular oxygen as an oxidant. [9][10][11][12][13] Thes tructure of the active site is highly debated, with evidence for both (m-oxo) dinuclear copper [9,14] and tris(moxo) trinuclear copper centers (Figure 1a). [15] Recent theoretical studies also suggest that monomeric Cu sites should not be excluded. [16,17] Amajor challenge in these systems is associated with the presence of as mall fraction of active sites (often below 30-60 %; note that as ystem with 90 %a ctive-site-0.47 mol CH 3 OH/mol Cu-was recently...