Volatilization of selected organic compounds, with Henry's law constan
t larger than 10(-3) atm-m3/mole, from water under turbulent condition
s has been studied. Surface area:volume ratio and water-bulk turbulent
intensity were the two major parameters that varied in the experiment
s. A model based on idealized surface renewal process is proposed. Bas
ed on this model, an equation incorporating the surface area:volume ra
tio and turbulent intensity (expressed in terms of the velocity gradie
nt, G) is derived by solving appropriate mass-transfer differential eq
uations. The derived model has been calibrated and verified with the e
xperimental results. Both the theoretical model and the experimental r
esults confirm that the volatilization of high-volatility compounds fr
om water into air follows first-order kinetics with respect to the che
mical concentration in water-bulk phase. The volatilization rate const
ant is found to be proportional to the surface area:volume ratio. It i
s also observed that the turbulent intensity in the water phase is an
important parameter in controlling the volatilization of chemicals fro
m the water.