HYDROGENATION OF CARBON-DIOXIDE BY HYBRID CATALYSTS, DIRECT SYNTHESIS OF AROMATICS FROM CARBON-DIOXIDE AND HYDROGEN

Direct synthesis of aromatics from carbon dioxide hydrogenation was investigated in a single stage reactor using hybrid catalysts composed of iron catalysts and HZSM-5 zeolite. Carbon dioxide was first converted to CO by the reverse water gas shift reaction, followed by the hydrogenation of CO to hydrocarbons on iron catalyst, and finally the hydrocarbons were converted to aromatics in HZSM-5. Under the operating conditions of 350-degrees-C, 2100 kPa, and CO2/H-2 = 1/2, the maximum aromatic selectivity obtained was 22% with a CO2 conversion of 38% using fused iron catalyst combined with the zeolite. Together with the kinetic studies, thermodynamic analysis of the CO2 hydrogenation was also conducted. It was found that unlike Fischer Tropsch synthesis, the formation of hydrocarbons from CO2 may not be thermodynamically favored at higher temperatures.