The disintegration of lime mud particles during slaking and causticizing ha
s been studied. This work was focused on the influence of the type of impel
ler: a high-flow impeller a pitched-blade turbine and a Rushton turbine wer
e investigated. Tests were made in a batch reactor having a capacity of 65
kg suspension. A model describing the disintegration was developed.
The experimental study showed that, for residence times longer than 10 minu
tes, the particle size was influenced by the mechanical energy input from t
he impeller as well as its design. It was found that the bulk flow (kinetic
energy in macro-scale) has a major impact on the disintegration of the lim
e mud agglomerates. Nevertheless, it was possible to characterise this phen
omenon by introducing the average turbulence fluctuation (kinetic energy in
micro-scale). This was possible since the kinetic energy generated by the
impeller roughly can be divided in micro-scale and macro-scale kinetic ener
gy. The model developed describes the average particle size as a function o
f the energy input, the turbulence fluctuation and the initial particle siz
e. The model has two material-specific parameters which were determined by
fitting the model to the experimental data. It was found that, at constant
impeller speed and constant residence time, the influence on the particles
increased in the order: high flow impeller < pitched blade turbine < Rushto
n turbine. At constant energy input the order is reversed.