
224 4 River Flow
discharge is Q (m
3
s
−1
), and the wetted perimeter length of the cross section is l
(m), then an appropriate Reynolds number for the flow is
Re =
Q
νl
, (4.1)
where ν =μ/ρ is the kinematic viscosity (and μ is the dynamic viscosity). If l =
20 m, ν =10
−6
m
2
s
−1
, Q =10 m
3
s
−1
, then Re ∼0.5 ×10
6
. Inevitably, river flow
is turbulent for all but the smallest rivulets. A different measure of the Reynolds
number is
Re =
uh
ν
, (4.2)
where u is mean velocity and h is mean depth. In a wide channel, we find that the
width is approximately l, so that Q ≈ ulh, and this gives the same definition as
(4.1). Thus, to model river flow, and to explain the response of river discharge to
storm conditions, as measured on flood hydrographs, for instance, one must model
a flow which is essentially turbulent, and which exists in a rough, irregular channel.
The classical way in which this is done is by applying a time average to the
Navier–Stokes equations, which leads to Reynolds’ equation, which is essentially
like the Navier–Stokes equation, but with the stress tensor being augmented by a
Reynolds stress tensor. The procedure is described in Appendix B.
For a flow u =(u,v,w) which is locally unidirectional on average, such as that
in a river, we may take the mean velocity
¯
u =( ¯u, 0, 0), and then the x component
of the momentum equation becomes
ρ
∂
∂z
(
u
w
) ≈−
∂ ¯p
∂x
+μ
∂
2
¯u
∂z
2
, (4.3)
because in a shallow flow, the other Reynolds stress terms are smaller. Integration
over the depth shows that the resistance to motion is provided by the wall stress τ ,
and this is
τ =μ
∂ ¯u
∂z
+{−ρ
u
w
}, (4.4)
evaluated at the wetted perimeter of the flow. Strictly, the Reynolds stress vanishes
at the boundary (because the fluid velocity is zero there), and the molecular stress
changes rapidly to compensate, in a very thin laminar wall layer. Normally one
evaluates (4.4) just outside this layer, close to but not at the boundary, where the
molecular stress is negligible and the Reynolds stress is parameterised in some way.
A common choice is to use a friction factor, thus
τ =fρ ¯u
2
, (4.5)
where the dimensionless number f (called the friction factor) is found to depend
rather weakly on the Reynolds number.
1
A crude but effective assumption is simply
that f is constant, with a typical value for f of 0.01.
1
More precisely, the stress should be τ = fρ|¯u|¯u, since the friction acts in the opposite direction
to the flow. For unidirectional flows, this reduces to (4.5). Later (in Sect. 4.5.3), we will have need
for this more precise formula.