Cu supported on SiO2 can be used to directly convert methane to methanol in a stepwise process with no intrinsic need for a zeolite support. Effects of parameters such as the O2 activation temperature, activation time, CH4 reaction temperature, CH4 partial pressure (p CH4) and Cu wt. % on methanol yield were investigated. Increasing the O2 activation temperature in the 200-800 °C range significantly improved the methanol yield and when carried out at 800 °C , a methanol yield of 11.5 µmol/gcatalyst was obtained after reaction with methane at 200 °C for the sample with 2 wt. % Cu. Yield per mole of Cu increased exponentially from 1.0 to 59.1 mmol with decreased Cu wt. % from 30 to 1, respectively. The increase in the O2 activation time also strongly