The viability of a new electrolyte was demonstrated in the bench-scale
electrochemical removal of SO, from flue-gas streams at high temperat
ures. At current densities up to 20 A/m(2) approximately 99% current e
fficiency was achieved when removing 90% of inlet SOx at 480 degrees C
. As current densities increased to 100 A/m(2), current efficiencies w
ere 64% at 480 degrees C and 73% at 520 degrees C. While species prese
nt in this K2SO4/V2O5 molten salt are not well understood, a simple me
chanism was used to develop a model to describe the observed removal r
esults. This model was then used to predict preliminary economic viabi
lity of this system based on known electrochemical technology.