whereumis the maximum velocity. Using the above expressions, equation
(14.63) results (in non-dimensional form) inCD| 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) isFiCD
32
kH^2 ^2 D | sint| sintCM cost. (14.65)LetAD
k2
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, thentmarccos 2 π. (14.66)
From equation (14.65)FimCD
3
2H^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 andπD^2
8A 1 D
ADH
CM
CDsinh(2kd) 2 kd
sinh^2 (kd)πD^2 a^2
4 ksinh(2kd) 2 kd
sinh^2 (kd)π^2 DumTd(2Fi/ u^2 mD^2 )
d(y/D)