Plasma-Catalytic CO2 Hydrogenation at Low Temperatures PROJECT TITLE :Plasma-Catalytic CO2 Hydrogenation at Low TemperaturesABSTRACT:A coaxial packed-bed dielectric barrier discharge (DBD) reactor has been developed for plasma-catalytic CO2 hydrogenation at low temperatures and atmospheric pressure. Reverse water-gas shift reaction and carbon dioxide methanation are found dominant within the plasma CO2 hydrogenation method. The results show that the H2/CO2 molar ratio considerably affects the CO2 conversion and therefore the yield of CO and CH4. The result of various γ-Al2O3 supported metal catalysts (Cu/γ-Al2O3, Mn/γ-Al2O3, and Cu-Mn/γ-Al2O3) on the performance of the CO2 hydrogenation has been investigated. Compared with the plasma CO2 hydrogenation while not a catalyst, the mixture of plasma with these catalysts enhances the conversion of CO2 by 6.sevenp.c-36%. The Mn/γ-Al2O3 catalyst shows the best catalytic activity for CO production, followed by the Cu-Mn/γ-Al2O3 and Cu/γ-Al2O3 catalysts. The presence of the Mn/γ-Al2O3 catalyst within the plasma process significantly will increase the yield of CO by 114%, compared with the plasma reaction within the absence of a catalyst. Additionally, we tend to realize that combining plasma with the Mn/γ-Al2O3 catalyst significantly enhances the energy potency of CO production by 116%, whereas packing the Cu/γ-Al2O3 catalyst into the DBD reactor only increases the energy potency of CO production by fifty twopercent. Did you like this research project? To get this research project Guidelines, Training and Code... Click Here facebook twitter google+ linkedin stumble pinterest Underwater Electrical Explosion of Wires and Wire Arrays and Generation of Converging Shock Waves Reliability Equivalence and Sensitivity Analysis to UHVDC Systems Based on the Matrix Description of the F D Method
