To characterize the sulfation capacity of limestone as a sorbent of SO2 in
a circulating fluidized-bed combustor (CFBC), long-term sulfation tests wer
e carried out in a thermobalance. In order to cover the range of residence
times expected in a large-scale combustor, the experiments lasted 24 h. The
residual activity of the sorbent after the first hours of reaction indicat
ed a conversion of similar to 0.1, depending on the particle's size and sul
fation conditions. The shrinking core model described well these residual a
ctivities. An effective gas-phase diffusion coefficient was derived from pl
ots of the measured conversion vs. time between 3 and 24 h. These diffusivi
ties ranged between 1.7 and 4.1 x 10(-9) m(2)/s at 850 degrees C and depend
ed only on the limestone. It is argued that this simple description could b
e incorporated into more complex sulfation models of the first few hours of
reaction and also account for the subsequent increases in conversion over
longer time scales. It is also stressed that, to predict a sorbent's perfor
mance in a boiler, characterization techniques should be expanded to experi
mental time scales similar to those expected in large-scale CFBCs.