Thermal partial oxidation of hydrocarbons to hydrogen and carbon monoxide (i.e., synthesis gas) is limited for conventional scale reactors due to soot formation under higher fuel/air equivalence ratios. Recent research into micro-scale (<4 mm diameter) thermal partial oxidation reactors with a controlled temperature of 800-900 °C has shown promise for conversion to synthesis gas without soot formation. Direct integration of Solid Oxide Fuel Cells (SOFCs) with these micro-scale thermal partial oxidation reactors has been proposed for portable power generation systems. In this work, the micro-scale thermal partial oxidation of methanol/air is investigated at fuel/air equivalence ratios from 1-5 and at a temperature of 800 °C. High conversion rates to synthesis gas are measured with a gas chromatograph for equivalence ratios between 1.5 and 3, with the concentration of hydrogen exceeding 10% and approaching chemical equilibrium predictions. A micro-tubular SOFC is integrated with the micro-scale thermal partial oxidation reformer to electrochemically oxidize the synthesis gas while generating power. SOFC polarization losses are investigated at different equivalence ratios and temperatures of the reformer with results indicating the mass transport losses decrease significantly as the equivalence ratio increases. Peak power densities occur when the synthesis gas concentration is maximized. Short term testing of the SOFC is stable no carbon deposition on the Ni-YSZ anode.
Read full abstract