Abstract

The reforming of methanol is usually carried out by a catalytic process. In this study, a single-stage, non-catalytic, methanol pyrolysis and reforming, process for producing mainly hydrogen using an atmospheric-pressure microwave plasma reactor is demonstrated. When the applied power was elevated from 800 to 1400 W, the selectivity of H 2 increased from 77.5% to 85.8% at inlet molar fraction of MeOH = 3.3%. The selectivities of carbon-containing byproducts were in the order: CO > carbon black > C 2H 2 > CH 4 > CO 2 ∼ C 2H 4. In addition, a higher conversion of methanol with a higher selectivity of H 2 was achieved at a higher applied power. While a low required energy consumption of H 2 (13.2 eV/molecule-H 2) was obtained at a low applied power (800 W) and a higher inlet concentration of methanol (5.0%).

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