
7.12 Notes and References 451
Taylor Dispersion Taylor dispersion is named after its investigation by Taylor
(1953), who carried out experiments on the dispersal of solute in flow down a tube.
The dispersion is enabled by the combination of differential axial advection by the
down tube velocity, typically a Poiseuille flow, and the rapid cross stream diffusion
which renders the cross-sectional concentration profile radially uniform. The theory
of Taylor is somewhat heuristic; it was later elaborated by Aris (1956). For a formal
derivation using asymptotic methods, see Fowler (1997, p. 222, Exercise 2).
Its application to porous media stems from the conceptual idea that the pore space
consists of a network of narrow tubules connected at pore junctions. If the tubes are
of radius a and length d
p
, the latter corresponding to grain size, then the Darcy
flux |u|∼πφU, while the pore radius a ∼ d
p
√
φ. This would suggest a Taylor
dispersion coefficient of
D
T
≈
a
2
U
2
48D
∼
d
2
p
|u|
2
48π
2
Dφ
, (7.280)
as opposed to the measured values which more nearly have D
T
∼|u|. Taylor dis-
persion in porous media has been studied by Saffman (1959), Brenner (1980) and
Rubinstein and Mauri (1986), the latter using the method of homogenisation.
Biofilm Growth Monod kinetics was described by Monod (1949), by way of
analogy with enzyme kinetics, where one considers the uptake of nutrients as oc-
curring through a series of fast intermediary reactions; when two nutrients control
growth, as in respiration, it is usual to take the growth rate as proportional to the
product of two Monod factors (Bader 1978). A variety of enhancements to this
simple model have also been proposed to account for nutrient consumption due to
maintenance, inactivation of cells in adverse conditions, and other observed effects
(Beeftink et al. 1990; Wanner et al. 2006).
Bacteria in soils commonly grow as attached biofilms on soil grains, with a thick-
ness of the order of 100 µ. A variety of models to describe biofilm growth have been
presented, with an ultimate view of being able to parameterise the uptake rate of
contaminant species in soils and other environments (Rittmann and McCarty 1980;
Picioreanu et al. 1998;Eberletal.2001; Dockery and Klapper 2001; Cogan and
Keener 2004).
Remediation Sites The three sites described in Sect. 7.8 are under study by the
Groundwater Restoration and Protection Group at the University of Sheffield, led by
Professor David Lerner. The site at Four Ashes is described by Mayer et al. (2001),
that at Rexco by Hüttmann et al. (2003), and that at St. Alban’s by Wealthall et al.
(2001).
The description of the two species reaction front given by (7.192) is similar to
that for a diffusion flame (Buckmaster and Ludford 1982) in combustion, and also
corrosion in alloys (Hagan et al. 1986). It is not conceptually difficult to extend
this approach to an arbitrary number of reactions, although it may become awkward
when multiple reaction fronts are present (see, for example, Dewynne et al. 1993).