Marc Gerritsma and Bart De Maerschalck
Conservation of momentum in the Stokes limit yields
∇·(pI −
τ
) = 0 in
Ω
, (121)
where p denotes the pressure field, I the unit tensor in R
d
, d = dim(
Ω
) and
τ
is the
extra-stress tensor.
The constitutive equation which relates the extra-stress tensor to the velocity field
is given by
λ
∇
τ
+
τ
= 2
µ
d , (122)
where
λ
is the relaxation time and
µ
the polymeric viscosity of the fluid,
∇
· denotes
the upper convected derivative defined as
∇
A =
∂
A
∂
t
+ (u,∇) A −L
τ
−
τ
L
T
, (123)
where (L)
i j
=
∂
u
i
/
∂
x
j
and 2d = L + L
T
. The UCM model (122) describes the fact
that the extra-stress does not instantaneously equal the rate of deformation of the
flow, but is also convected and deformed along the particle paths as expressed by
(123). When the relaxation time
λ
= 0, the stress components are no longer con-
vected along the particle paths and Newtonian Stokes flow is retrieved.
Consider the flow past a cylinder placed at the centerline of a channel of width
4R, where R denotes the radius of the cylinder. The computational domain equals
the domain used by Alves, Pinho and Oliveira, [2]. At inflow, 19R upstream of the
cylinder, a fully developed Poiseuille flow is prescribed for velocity and extra-stress
components. The downstream length is taken to be 59R. The number of spectral
elements equals K = 16 and the polynomial degree in each element has been set
to N = 16 for all variables. The topology of the grid and the Gauss-Lobatto grid
near the cylinder are shown in Fig. 27. Note the small spectral elements around
the cylinder and in the wake of the cylinder. Especially near the rear stagnation
point a very small spectral element is placed to capture the high stress-gradients. In
order to compare the results obtained with D-LSQSEM-DM the non-dimensional
drag coefficient on the cylinder is compared with results reported in [2]. The drag
coefficient is defined as
C
d
:=
1
µ
U
Z
surf. cyl
(
τ
− pI) ·n
x
dS , (124)
where n
x
is the x-component of the outward unit normal at the cylinder and U is
the bulk velocity. The influence of elasticity in the flow is denoted by the Deborah
number, De
De =
λ
U
R
. (125)
Fig. 28 graphically displays the drag coefficients as a function of De. From the
results presented above it can be concluded that D-LSQSEM-DM is capable of pro-
ducing drag coefficients in agreement with those reported in [2]. However, agree-
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