Canadian Journal of Chemical Engineering, Vol.76, No.4, 762-770, 1998
A method of evaluating limestone reactivity with SO2 under fluidized bed combustion conditions
The reactivity of limestone with sulphur dioxide has been evaluated during conditions similar to those existing in a fluidized bed combustor using a fixed-bed quartz reactor. The reactivity of up to 11 particle sizes of 2 limestones were evaluated, and an exponential decay function was found to best describe the rate behaviour versus conversion of CaO to CaSO4. The two constants in the exponential decay approximation could both be expressed as functions of particle size. Subsequently, the limestone reactivity as a function of both size and conversion could be reasonably well described by a total of 4 to 6 constants. An analytical sulphur capture model for fluidized bed boilers (FBB) that incorporates this type of reactivity function is proposed.
Keywords:HIGH-TEMPERATURE REACTION, GAS-SOLID REACTIONS, SULFUR-DIOXIDE;CALCIUM-OXIDE, ANALYTICAL MODEL, COAL COMBUSTORS, PORE MODEL;SIZE MODEL, SULFATION, BOILERS