K. Tatsutani et al., UNSTEADY-FLOW AND HEAT-TRANSFER FOR CYLINDER PAIRS IN A CHANNEL, International journal of heat and mass transfer, 36(13), 1993, pp. 3311-3328
The incompressible, two-dimensional, unsteady flow past a pair of cyli
nders of square cross-section, placed in tandem normal to the flow in
a channel, has been investigated by dye visualization and direct numer
ical simulation. The objective has been to evaluate the effect of cyli
nder separation distance, lambda, on the flow behavior and heat transf
er, for cylinder diameter ratios, D/d, of 1 and 2 over a range of Reyn
olds numbers 200 less-than-or-equal-to Re less-than-or-equal-to 1600,
based on the larger (downstream) cylinder diameter. A comparison betwe
en the experimental and numerical results for cylinders of equal cross
-section dimensions shows very good agreement. The results for D/d = 1
reveal three distinct flow patterns as a function of lambda and Re wh
ich, apparently, have not been previously reported: (1) For 0.25 less-
than-or-equal-to lambda less-than-or-equal-to 4 with Re less-than-or-e
qual-to 200, the inter-cylinder flow consists of a pair of steady coun
ter-rotating eddies which do not exchange fluid with the surrounding f
low and eddy shedding is observed only for the downstream cylinder. (2
) For 0.25 less-than-or-equal-to lambda less-than-or-equal-to 1.0 with
400 less-than-or-equal-to Re less-than-or-equal-to 1600, vertical flo
w oscillations arise in the inter-cylinder space, and the periodic ing
estion of backward-jetting fluid from the top and bottom walls of the
downstream cylinder into the inter-cylinder space is observed. For fix
ed lambda the unsteadiness increases with Re but only the downstream c
ylinder sheds large eddies. (3) At a critical inter-cylinder spacing r
elated to Re according to lambda(c) is similar to Re-2/3, the shedding
of large eddies also occurs at the upstream cylinder and this results
in a highly mixed inter-cylinder flow. For a cylinder diameter ratio
of D/d = 2, with the smaller cylinder located upstream of the larger h
eated cylinder, it is shown that for Re fixed an optimal location exis
ts for the upstream cylinder such that the heat transfer from the down
stream cylinder is maximized. The optimal location corresponds to a sp
acing smaller than the critical inter-cylinder spacing.