546111 Liquid-Phase Oxidation of Methane into Oxygenates with O2

Wednesday, June 5, 2019
Texas Ballroom Prefunction Area (Grand Hyatt San Antonio)
Jong Kyu Kang1 and Eun Duck Park1,2, (1)Department of Energy Systems Research, Ajou University, Suwon, Korea, Republic of (South), (2)Department of Chemical Engineering, Ajou University, Suwon, Korea, Republic of (South)

Methane has been used as a clean energy source because it emits the smallest amount of CO2 per heat produced among hydrocarbons. Recently increasing attention has been paid to its chemical conversion owing to the upsurge of shale gas production. However, due to the lack of the economic process for the utilization of methane as a chemical feedstock in a small scale, about 35% of methane is just being flared away in the United States. In the convention chemical process, methane is first converted into syngas (a mixture of CO and H2), which can be further transformed into various chemicals. Since the typical syngas process is energy-intensive, only large-scale methane-based process can be cost-effective compared with petrochemical process to produce the same chemical. To utilize the small gas well efficiently, the efficient direct methane conversion technology into liquids needs to be developed.

Since methane has a strong C-H bond, its functionalization is quite demanding under mild conditions. Therefore, strong oxidants including H2O2 have been used to oxidize methane in the liquid phase. Hutchings and his colleagues reported the direct conversion of methane into methanol and formic acid using heterogeneous catalysts such as Cu-promoted Fe/ZSM-5 in the aqueous phase. Because of the high price of H2O2, there have been many efforts to use O2 or air as an oxidant. However, high yields of methane oxygenates could not be accomplished in a single-step process. To compromise these two processes, in situ generation of H2O2 from H2 and O2 can be proposed in order to oxidize methane selectively under mild conditions.

In this work, Pd/C and ferrous ion was utilized to generate H2O2 from a mixture of H2 and O2 and to oxidize methane, respectively. The ferrous ion is essential to form two oxygen-radical species (hydroxyl and hydroperoxyl radical) from H2O2 to oxidize methane in the aqueous phase. The effect of catalyst compositions on the catalytic activity was examined systematically to find out the role of each component in this catalytic reaction. It can be concluded that methane can be oxidized into formic acid in the co-presence of H2 and O2 using the catalyst system composed of Pd/C and ferrous ion.


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