whereumis the maximum velocity. Using the above expressions, equation
(14.63) results (in non-dimensional form) in
CD| sint| sintCM cost. (14.64)
The term umT/Dis known as the Keulegan–Carpenter number, Kc. It may
be shown from equations (14.16) and (14.18) that Kc 2 πX/D. Thus Kc
specifies the relative importance of the distance of travel of the fluid parti-
cles to the diameter of the cylinder. It is clear from equation (14.64) that
for small values of Kc(in practice, less than about 1.0), inertia force domi-
nates drag force. If Kcis large, separation becomes important so the drag
outweighs the inertia force.
The in-line force per unit length, dFi/dy, given by equation (14.63) is
obtained by substituting for ufrom equation (14.16) and du/dt, the time
derivative of u.
Assuming constant values of CDandCMacross the depth, Fiafter
integration of equation (14.63) is
FiCD
32
k
H^2 ^2 D | sint| sint
CM cost. (14.65)
Let
AD
k
2
andA 1 ^2 /k. For the maximum force, Fm, on the cylinder, the time deriv-
ative of Fimust be zero, i.e. dFi/dt0. If ttm, at which Fiis equal to the
maximum value Fim, then
tmarccos 2 π. (14.66)
From equation (14.65)
FimCD
3
2
H^2 DADsin^2 (tm)CM HA 1 cos(tm). (14.67)
For an isolated cylinder in inviscid fluid, CM2.0. However, both CD
andCMare functions of the Reynolds number, the Keulegen–Carpenter
number and the surface roughness. The growth of marine plants and
πD^2
8
A 1 D
ADH
CM
CD
sinh(2kd) 2 kd
sinh^2 (kd)
πD^2 a^2
4 k
sinh(2kd) 2 kd
sinh^2 (kd)
π^2 D
umT
d(2Fi/ u^2 mD^2 )
d(y/D)