Capture of [formula omitted] by limestone under calcination conditions in a high-pressure fluidized-bed reactor

Abstract

The experiments on the sulfidation of CaO were carried out in a high-pressure and -temperature fluidized-bed reactor. The rate of CaO sulfidation decreased with the increase in total pressure under constant H 2 S partial pressure. H 2 O introduced in inlet gas and produced during reaction promoted the sintering of CaS or CaO, resulting in the decrease in both the rate of CaO sulfidation and final conversion. When the calcination of CaCO 3 and the sulfidation of CaO took place simultaneously, however, there was little influence of H 2 O on the reaction. Both the calcination of CaCO 3 and sulfidation of CaO slowed down with increasing CO 2 partial pressure. The sulfidation of CaO was always slower than CaCO 3 calcination in the range of the experimental conditions. A shrinking unreacted-core model with variable effective diffusivity predicted well the sulfidation process accompanied by the calcination.