Tuesday, November 17, 2020
Catalysis and Reaction Engineering Division (20) (PreRecorded+)
In this study, molybdenum (Mo)-modified vanadium (V)-based selective catalytic reduction (SCR) catalysts were investigated for the simultaneous removal of elemental mercury (Hg(0)) and nitrogen oxide (NO) in terms of different metal loadings, impregnation sequences, TiO2 phases, calcination temperatures, flue gas constituents, gas velocities, and reaction temperatures. Different impregnation sequences could lead to different Hg(0) oxidation performances. The modified SCR catalyst prepared using the impregnation sequence of Mo+W followed by V exhibited the highest Hg(0) oxidation performance. Meanwhile, the NO reduction performance was quite constant with respect to different impregnation sequences. Anatase phase TiO2 and the calcination temperatures of 400 and 500 °C resulted in the best performance. The high calcination temperature of 700 °C resulted in TiO2 phase transformation and agglomeration. The modified SCR catalyst prepared with optimal formulations showed ~99% Hg(0) oxidation and 87% NO reduction efficiencies at a molar ratio of NH3 to NO of 0.9 under 350 °C and 5,000 hr-1 space velocity in typical sub-bituminous and lignite coal simulated flue gases. Different characterization techniques including BET, TEM, XRD, XPS, and XAFS were employed to explore the mechanisms responsible for the performance differences. The detailed experimental and characterization results will be presented.
See more of this Session: Combustion Kinetics and Emissions
See more of this Group/Topical: Catalysis and Reaction Engineering Division
See more of this Group/Topical: Catalysis and Reaction Engineering Division