Sequentially prepared Mo-V-Based SCR catalyst for simultaneous Hg0 oxidation and NO reduction

Molybdenum (Mo)-vanadium (V)-based selective catalytic reduction (SCR) catalyst synthesized by the sequential impregnation of Mo and W followed by V was investigated for simultaneous elemental mercury (Hg-0) oxidation and nitrogen oxide (NO) reduction in an existing SCR unit with respect to different TiO2 phases, calcination temperatures, flue gas constituents, gas velocities, and reaction temperatures. Anatase phase TiO2 and the calcination temperatures of 400 and 500 degrees C resulted in similar to 69% Hg-0 oxidation at 10 ppmv HCl and 350 degrees C. The high calcination temperature of 700 degrees C resulted in TiO2 phase transformation from anatase to rutile and agglomeration. The modified SCR catalyst prepared with the impregnation sequence of Mo and W followed by V using anatase TiO2 and calcination temperature 500 degrees C showed similar to 99% Hg-0 oxidation and 87% NO reduction conversions at an NH3/NO molar ratio of 0.9 under 350 degrees C and 5,000 hr 1 space velocity in typical sub-bituminous and lignite coal simulated flue gases. The effects of these parameters and conditions were further investigated using various characterization techniques including BET, TEM, XRD, NH3 TPD and XAFS.

Automated summary

The Mo-V-based SCR catalyst showed good performance for Hg-0 oxidation and NO reduction under various conditions, with the best results observed using anatase TiO2 and a calcination temperature of 500 degrees Celsius. Various characterization techniques were used to investigate the effects of different parameters and conditions on the catalyst performance.