. Degradation kinetics were best described by a reductant model that accounted for two limiting reactants, THMs and ammonia-nitrogen (NH 3 -N). A decrease in the temperature resulted in a decrease in both ammonia and THM degradation rates with ammonia rates affected to a greater extent than THM degradation rates. Similarly to the THM degradation rates, product toxicity, measured by transformation capacity (T c ), increased with increasing THM bromine substitution. Because both the rate constants and product toxicities increase with increasing THM bromine substitution, a water's THM speciation will be an important consideration for process implementation during drinking water treatment. Even though a given water sample may be kinetically favored based on THM speciation, the resulting THM product toxicity may not allow stable treatment process performance.Balancing the competing goals of disinfection and disinfection by-product (DBP) regulations is a challenge for many drinking water utilities. The proposed stage 2 disinfection and DBP regulations (15, 16) will only make this task more difficult. Although chlorine disinfection remains quite popular in the United States (6, 7), many utilities now use combinations of chlorine and chloramines to avoid excessive trihalomethane (THM) and haloacetic acid formation. A typical treatment scheme consists of an initial period of chlorination to help achieve disinfection goals followed by quenching with ammonia at some point in the treatment train to meet DBP goals through the lower DBP formation rates associated with chloramines. Nevertheless, significant formation of THMs and haloacetic acids can occur within treatment plants even during relatively short periods of chlorination (24, 28). Therefore, approaches for minimizing the formation of these DBPs or for removing the DBPs within treatment plants are potentially of much practical value.Much effort over the past two decades has gone into approaches for minimizing DBP formation through modification of disinfection practices and removal of precursor materials (23), while comparatively little effort has been expended on approaches for removing DBPs formed in treatment plants before finished water is sent into distribution systems. Very early on, both technological and philosophical problems with the removal of THMs through activated carbon adsorption and air stripping were identified (28), and approaches for removing DBPs after formation have been largely ignored since that time. Recent developments in biological treatment, however, strongly suggest that revisiting treatment processes for THM removal is worthwhile.No evidence indicates that THMs can support microbial growth. Considerable evidence is available, however, for cometabolism of chloroform, or trichloromethane (TCM), by bacteria growing on other chemicals (2, 5, 9). Of particular interest is the observation that nitrifying bacteria can cometabolize chloroform at a reasonable rate (0.03 to 0.1 liter/mg/ day). The premise of this research is that THM removal should b...