Spray nozzles are widely used to provide a uniform liquid distribution to p
acked distillation and absorption columns. A disadvantage of such distribut
ors is, however, the tendency for the atomized drops to be entrained by the
upflowing gas. In some instances it is not convenient or even possible to
remove the entrained liquid from the gas. A theoretical model has been deve
loped for estimating the total entrainment from spray nozzle distributors.
The model is based on drop size distribution and drop bouyancy relationship
s and has been confirmed by measurements in a 11.5-in. diameter spray conta
ctor, using four different solid-cone nozzles and the air-water system. The
model has also been confirmed by measurements of others using an air-paraf
finic oil system. The model takes into account orifice diameter, phase flow
rates, and phase physical properties. It predicts total entrainment and do
es not allow for partial removal of entrainment by walls, adjacent sprays,
or target devices used to collect the entrained liquid. Thus, the predictio
ns are conservative for multiple spray nozzle assemblies.