There exists, worldwide, a strong incentive for the development of eff
icient processes that permit the recovery of Cl-2 from HCl waste bypro
ducts, to avoid the need for disposal of this toxic and corrosive mate
rial. In this paper we will describe such a process that has been deve
loped by our group and which is currently being tested at the pilot pl
ant scale. The process uses a salt mixture impregnated on a high surfa
ce area support alternately chlorinated and oxidized in two fluidized-
bed reactors in series. The process development included basic studies
of the mechanism of the HCl oxidation reaction over a broad range of
temperatures (25-400 degrees C) and pressures (10(-5) Torr, 1 atm). Th
is paper will present an overview of the results of these studies. On
the basis of these investigations, a preliminary economic evaluation w
as completed and a pilot-plant-scale unit was designed and constructed
.