Introducing roughness in tubes increases the turbulent heat-transfer c
oefficient but there is usually a much larger increase in friction fac
tor for constant geometry and flow conditions. In this study, generali
zed rib-tube correlations are used in optimizing the roughness geometr
y for two different objective functions or performance evaluation crit
eria (PEG). Considered are the maximum heat transfer for given pumping
power and surface area (R-3) and the minimum surface area for constan
t heat load and pumping power (R-5). Only tube-side flow was considere
d. The PEG, with their associated constraint equations, were evaluated
by using a simple iterative procedure over a wide range of parameters
(Re = 10,000-100,000, Pr = 0.7-35, e/d = 0.01-0.1, p/d = 0.1-1.0, and
alpha/90 = 0-1.0). The optimum rib geometry had e/d = 0.02, p/d = 0.1
, and alpha/90 = 1.0. The Reynolds and Prandtl numbers had little infl
uence on hear-transfer augmentation. The improvement in the effectiven
ess due to the ribbed tubes has been illustrated for different tube an
d flow variables to aid in the preliminary design of enhanced heat exc
hangers.