A model is developed that predicts bubble dynamics and oxygen transfer
in a Speece Cone. The model is based on differential mass balances fo
r both gas and water and requires a knowledge of cone dimensions, wate
r flow rate, depth to the cone, and initial bubble diameter produced b
y the oxygen diffuser. The model calculates the oxygen transfer, nitro
gen stripping, and gas-phase holdup within the cone. Experimental data
for a Speece Cone have not been published; however, a modified versio
n of the model is tested using data obtained from a hydrodynamically s
imilar full-lift hypolimnetic aerator with good results. This process
model, when coupled with a suitable cost model, should prove useful in
the preliminary design and economic optimization of Speece Cone oxyge
nators. (C) 1998 IAWQ. Published by Elsevier Science Ltd.