| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 238705 | Powder Technology | 2008 | 8 Pages |
Fragmentation of limestone due to thermal shock and calcination in a fluidised bed was studied through experiments and modelling. The time for heating was estimated by model calculations and the time for calcination by measurements. Fragmentation due to thermal shock was carried out by experiments in a CO2 atmosphere in order to prevent the effect of calcination. It was found to be much less than fragmentation due to calcination. Average particle sizes before and after fragmentation are presented for several types of limestone. The effects of particle size and gas composition on the primary fragmentation were studied through experiments. Increasing the fluidisation velocity increased the tendency to fragment. The evolution of the particle size distribution (PSD) of limestone particles due to thermal shock and during calcination (or simultaneous calcination and sulphation) were calculated using a population balance model. Fragmentation due to thermal shock is treated as an instantaneous process. The fragmentation frequency during calcination is presented as exponentially decaying over time. In addition to the final PSD, this model also predicts the PSD during the calcination process. The fragmentation was practically found to end after 10 min. Furthermore, a population balance method to calculate the particle size distribution and amount of limestone in fluidised beds in dynamic and steady state, when feeding history is known, is presented.
Graphical abstractFragmentation of limestone due to thermal shock and calcination in a fluidised bed was studied by experiments and population balance modelling. Fragmentation due to thermal shock was carried out with experiments in a CO2 atmosphere in order to prevent the effect of calcination. In addition to final particle size distribution (PSD), this model also predicts the evolution of the PSD during the calcination process. The use of population balance modelling for calculating PSD and volume of limestone in fluidised beds is illustrated.Figure optionsDownload full-size imageDownload as PowerPoint slide
