Hold-up is an important design parameter for pipelines transporting solid l
iquid mixture as it correctly determines the bl situ volume fraction of dif
ferent phases. Extensive experiments have been reported to establish the ef
fect of solid concentration, flow velocity and particle size on hold-up. Ba
sed on the data base, a simple correlation has been proposed for determinat
ion of hold-up for multi-sized solid-liquid flow through pipes. The propose
d correlation [HR = 1+ 0.64(W-0/ U*)(1.50)] incorporates the effect of all
the factors affecting hold-up such as solid concentration, flow velocity, p
article size, pipe diameter, etc. The predictions based on the proposed cor
relation match reasonably well with the experimental data.