An experimental study of the catalytic hydrogenation of adiponitrile i
n a mini-plant with a continuously operated slurry draft-tube bubble c
olumn is discussed. The purpose of this work is to determine the influ
ence of operating parameters on the performance of the reactor, and to
develop a complete model to describe its behaviour. The following bas
ic information was first obtained: hydrodynamic data; a mock-up of the
same scale as the reactor is built to measure the characteristics of
the fluid flow. intrinsic kinetics data; the Langmuir-Hinshelwood mode
l is chosen, supposing surface reaction limitation and competitive ads
orption between hydrogen and nitriles. This correctly describes the ex
perimental data. From this first information, a model supposing well-m
ixed liquid phase is developed. It is not a completely predictive mode
l, since two parameters have to be estimated: the volumetric liquid-ph
ase mass transfer coefficient and the deactivation parameter. This com
plete model is available representing experimental data with good accu
racy.