Different types of mixing cell models are analysed in detail. One type
is found to be second-order accurate when reactions are not considere
d but reduces to first-order accuracy when a sorption reaction is take
n into account. The second type is only first-order accurate even when
a reaction is not considered. The most commonly used mixing cell mode
l is extended to account for different surface boundary conditions, in
cluding that for a landfill. The exit conditions for a finite spatial
domain were taken into consideration by making use of boundary layer c
orrections. It is found that the results obtained using the mixing cel
l model coupled with a non-linear isotherm are very accurate when comp
ared with results obtained from a Crank-Nicolson scheme. It was observ
ed that the accuracy of the results is dependent on the spatial step s
ize. Best results are obtained when the spatial step size is close to
twice the dispersivity. Application of the mixing cell model with a bo
undary layer correction was demonstrated by comparison with experiment
al data from a laboratory Na-Ca exchange experiment in which a solutio
n containing Na was passed through a column filled with Ca-saturated l
oamy sand. The mixing cell model was also applied to breakthrough curv
es of two organic compounds (carbontetrachloride and tetrachloroethyle
ne) observed in a field experiment conducted at Borden, Ontario, Canad
a. The mixing cell model described satisfactorily the Na transport in
loamy sand and also the transport of organics in a Borden aquifer.