The representation of multispecies chemi cal transformations into models fo
r porous media flow and transport is investigated. Since the rate of transf
ormation is dependent on the actual concentrations of the reactants inside
the pore-spaces (rather than the averaged concentration that is amenable to
a porous continuum model) such models may show a lesser or greater rate of
transformation than is actually occurring, depending on the pore-scale cor
relation of the reactant concentrations. To examine this experimentally, a
bimolecular reaction (A + B --> Product) in a saturated porous media flow i
n a column was studied using a spectrophotometer. The second-order rate con
stant of the reaction was independently determined in well-mixed batch test
s. In the reactive transport experiments, the porous medium column was init
ially saturated with one reactant, the other reactant was injected at one l
ongitudinal end of the column, and the effluent concentrations were measure
d. It is documented that a reactive transport model that does not account f
or the pore-scale segregation of reactants can substantially overpredict th
e product concentration.