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Direct conversion of methane to chemical feedstocks such as methanol under mild conditions is ac hallenging but ideal solution for utilization of methane.P d 1 O 4 single-sites anchored on the internal surface of micropores of am icroporous silicate exhibit high selectivity and activity in transforming CH 4 to CH 3 OH at 50-95 8 8Cinaqueous phase through partial oxidation of CH 4 with H 2 O 2 .T he selectivity for methanol production remains at 86.4 %, while the activity for methanol production at 95 8 8Ci sa bout 2.78 molecules per Pd 1 O 4 site per second when 2.0 wt %C uO is used as ac ocatalyst with the Pd 1 O 4 @ZSM-5. Thec onversion rate of CH 4 to CH 3 OH at as olid-liquid interface pioneered by Hutchings et al [4a,5] is typically higher than these at as olid-gas interface, [3a,b] though the rate is still relatively low.Although catalytic activity for direct oxidation of CH 4 to CH 3 OH on these catalysts at solid-gas and solid-liquid interfaces was reported, [1,[3][4][5][6] challenges remain before ad irect oxidation process under mild conditions could be considered as ap otential approach in the chemical industry. [1] Hydraulic fracturing supplies much of this earth-abundant source from shale,w hich make chemical and energy transformations economical.