The catalytic activation of CH
4 by limited amounts of O
2 produces a mixture of synthesis gas (CO, H
2) and light hydrocarbons (C
2H
x), the relative amounts of each depending on catalyst type and process conditions. Using
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The catalytic activation of CH
4 by limited amounts of O
2 produces a mixture of synthesis gas (CO, H
2) and light hydrocarbons (C
2H
x), the relative amounts of each depending on catalyst type and process conditions. Using an elementary reaction mechanism for the oxidative coupling of methane (OCM) on a La
2O
3/CeO
2 catalyst derived from the literature, this study replaces the activating O
2 with moist H
2O
2 vapor to reduce synthesis gas production while improving C
2H
x yields and selectivities. As the H
2O
2 content of the activating oxidant rises, more of the CH
4 conversion occurs in the gas phase instead of with the catalytic surface. In a packed bed reactor (PBR), the use of H
2O
2 allows the PBR “light-off” to occur using a lower feed temperature. In exchange for a small decline in CH
4 conversion, C
2H
x selectivity increases while synthesis gas production drops. In a continuous stirred tank reactor (CSTR), H
2O
2 improves C
2H
x over synthesis gas across a wider range of feed temperatures than is possible with the PBR. This suggests the CSTR will likely reduce OCM preheating requirements.
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