Methylene chloride (CH2Cl2) is a representative model compound commonly fou
nd in aqueous wastes, process effluents, and contaminated soils and sedimen
ts.' Oxidation in supercritical water provides a viable treatment and remed
iation pathway to convert CH2Cl2 to CO2, H2O, and HCl. However, in earlier
work, partial hydrolysis was observed at subcritical temperatures (<374 deg
rees C). This low-temperature reactivity complicates the measurement of kin
etic data. In this study, the kinetics of CH2Cl2 hydrolysis in sub- and sup
ercritical water were experimentally measured and modeled. Catalytic effect
s from a high nickel content alloy used for the reactor were studied by com
paring kinetic data obtained in quartz ampules with and without metal prese
nt. No heterogeneous catalysis effects were observed. Reaction rates from 1
00 to 500 degrees C were measured to check the reproducibility of existing
published data (up to 150 degrees C) and to extend the database for hydroly
sis to the supercritical region in order to develop a robust empirical glob
al rate expression. The data show a local maximum in the rate constant belo
w the critical point of water, consistent with a possible change in the rea
ction mechanism induced by changes in the solvent's physical properties (di
electric constant, density, etc.). Variations in the global rate constant a
gree quantitatively with predictions obtained by applying the Kirkwood mode
l, which accounts for changes in the dielectric constant and density of the
solvent.