NONIONIC SURFACTANT-ENHANCED SOLUBILIZATION AND RECOVERY OF ORGANIC CONTAMINANTS FROM WITHIN CATIONIC SURFACTANT-ENHANCED SORBENT ZONES .2.NUMERICAL SIMULATIONS
Js. Hayworth et Dr. Burris, NONIONIC SURFACTANT-ENHANCED SOLUBILIZATION AND RECOVERY OF ORGANIC CONTAMINANTS FROM WITHIN CATIONIC SURFACTANT-ENHANCED SORBENT ZONES .2.NUMERICAL SIMULATIONS, Environmental science & technology, 31(5), 1997, pp. 1284-1289
A mathematical model is developed to investigate the simultaneous aque
ous phase transport and partitioning behavior of a nonionic surfactant
and a representative hydrophobic organic contaminant (HOC) in flow-th
rough aquifer material-water systems. Unmodified aquifer material and
aquifer material treated with a cationic surfactant are considered. No
nionic surfactant sorption is represented using the equilibrium, nonli
near two-term Langmuir equation and the kinetic, nonlinear Langmuir eq
uation. HOC sorption and solubilization is represented by an expressio
n relating HOC partitioning between the bulk solid phase and the bulk
aqueous phase containing monomer and micellar pseudophases. The model
is implemented in a one-dimensional finite difference numerical model
that utilizes Picard iteration to accommodate nonlinearities. Column e
ffluent breakthrough data are used to evaluate the modeling approach.
Experimentally determined batch data provided most of the model input
parameters. Model simulations show good agreement with measured result
s when mass transfer limitations for the nonionic surfactant are consi
dered. The model is employed to examine the potential effects of influ
ent nonionic surfactant concentration and flushing rate on the removal
of HOCs from within a cationic surfactant-enhanced sorbent zone. The
analysis revealed that increasing nonionic surfactant influent concent
rations decreased the volume of nonionic surfactant required to recove
r an HOC pulse and that HOC removal increased with increasing nonionic
surfactant Rushing rate. It is likely, however, that a maximum flow r
ate exists above which mass transfer limitations in HOC aqueous-solid
phase partitioning will occur.