The hydrodynamic model of Young et al. (1991) for external-loop gas-li
ft reactors was modified to account for buoyancy forces in the gas pha
se. The revised model is based on macroscopic balances for the gas-liq
uid separator and external downcomer and spatially-averaged, I-D mass
and momentum balances in the riser. Using only the physical properties
of the gas and liquid phases, the reactor dimensions, and the gas sup
erficial velocity the model predicts gas holdup profiles, gas and liqu
id velocity profiles, and pressure profiles in the riser for bubbly fl
ow. Empirical correlations are used to represent frictional and drag e
ffects, but there are no adjustable parameters in the model. The syste
m of equations that must be solved to predict hydrodynamic behavior is
simpler than that of Young et al. The sensitivity of the model to cho
ice of drag coefficient correlation is analyzed The model predictions
match experimental data of previous works.