Abstract. Mass transfer from entrapped nonaqueous phase liquids (NAPLs) at subsurface locations of environmental contamination •'pically takes place in threedimensional groundwater flow fields. Yet most laboratory studies of NAPLs dissolution have been one-dimensional, eliminating more realistic conditions such as the heterogeneous distribution of entrapped NAPL ganglia and the potential for flow bypassing due to reduced water permeability in contaminated zones. In this study, experiments in two-dimensional flow fields were used to evaluate the effects of flow dimensionality on NAPL dissolution. Modifications of the transport code MT3D provided the capability to simulate NAPL dissolution. Regression analysis, matching experimental observations to simulated predictions, provided parameter values for a proposed phenomenological model of dissolution in two-dimensional flow fields. The proposed model predicted lower NAPL dissolution rates relative to models developed on the basis of published one-dimensional experimental measurements. The results indicate potential for significant errors using the one-dimensionally based models for NAPL dissolution in field applications. Recently, researchers have avoided the need to quantify entrapped NAPL geometry by using a lumped mass transfer coefficient K, defined as the product of the interfacial area between the NAPL and groundwater phases (ana), and an average mass transfer coefficient for the NAPL-water surface (kla) [Miller et al., 1990;Powers et al., 1992 Powers et al., , 1994. With the derivation of (1) the value of K, incorporating the unspecified specific surface area between phases, is determined from laboratory measurements. Methods to determine values of K are based on correlations containing a modified Sherwood number (Sh = K dp 2 D•I), where Sh is the Sherwood number, dp (L) Table i provides a review of some of the dimensionless correlations used to describe interphase mass transfer. 971