Kinetics of the thermal dehydration of sodium carbonate decahydrate to mono
hydrate is investigated at temperatures between 15 and 30 degreesC in a bat
ch, fluidized-bed, 140-mm-ID reactor. Effects of particle size, mass of bed
, and gas velocity on the dehydration rate are also explored. A simple corr
elation based on the collected experimental data is developed. The proposed
rate law formula makes it possible to estimate the dehydration rate that w
ould be needed to design the performance of a fluidized-bed drying unit. Th
e produced monohydrate is subjected to textural analysis, and pore volume a
nd surface-area data are presented.