The replacement of lime with limestone for the neutralisation of acid
water was investigated through batch and semi-continuous studies. A fl
uidised-bed reactor with multiple stages of increasing diameters is pr
eferred for the limestone neutralisation process as it allows fluidisa
tion of the bigger particles but also prevents washout of the smaller
particles in the case where ungraded particle size limestone is used.
It was determined that the rate of neutralisation is influenced by the
particle size of limestone and the type of metal in solution. Sulphat
e is removed as gypsum to the level where the water is saturated with
calcium sulphate, while CO2 is produced as a by-product.