A mathematical model describing the sulfidation of a single calcined l
imestone particle was developed and experimentally verified This model
, which includes no fitting parameters, assumes a calcined limestone p
article to consist of spherical grains of various sizes that react wit
h H2S according to the classic shrinking-core model. The initial size
distribution of the grains is derived from mercury porosimetry. The tr
ansport of H2S through the bidisperse limestone particle is calculated
based on the random-pore model of Wakao and Smith, which distinguishe
s macropore and micropore zones. Knudsen diffusivity inside the microp
ore zones is calculated according to the dusty-gas approach. The singl
e-particle model delivers the value of a new defined utilization facto
r, which includes effects of external mass-transfer limitation, pore-d
iffusion limitation, and grain-size distribution on particle reactivit
y. A correlation derived for a single batch of calcined limestone expl
icitly expresses this utilization factor. as a function of conversion
and relevant process parameters. This correlation can be easily incorp
orated into reactor models, as shown for an existing model describing
the capture of H2S by a fluidized bed of calcined limestone particles.