A computer model characterizing the performance of a spray tower oxyge
n absorption system was developed based on finite difference mass tran
sfer calculations. Performance was assessed in terms of oxygen utiliza
tion, transfer efficiency, and economy. Pilot scale tests verified mod
el assumptions and performance predictions. Simulation runs indicated
spray tower head and oxygen feed requirements for desired changes in d
issolved oxygen (DO) exceeded those required for packed column equipme
nt. Spray tower performance was improved by increasing hydraulic loadi
ng from 35 to 85 kg m(-2) s(-1) and by increasing tower height from 1.
25 to 2.50 m. The effluent DO concentration that minimized variable co
sts of oxygen transfer was lower in the spray tower than in the packed
tower, indicating clean water use of the spray tower will be limited
to moderate effluent DO requirement applications (DO <20 mg l(-1)). (C
) 1997 Elsevier Science B.V.