Buoyancy induced heat transfer deterioration in concentric and eccentric annuli

Turbulent convection heat transfer of upward fluid flows in vertical annular channels with uniformly
heated inner wall and adiabatic outer wall is investigated numerically. Two concentric geometries with
outer-to-inner diameter ratios of 2.4 and 3 as well as two eccentric geometries with identical outer-toinner
diameter ratio of 2.4 and eccentricities of 0.25 and 0.5 are investigated. Heat transfer deterioration,
similar to that of a circular pipe, is observed. The range of buoyancy parameter, over which deterioration
is observed, is close to that of circular pipes. Moreover, it is observed that when the value of eccentricity
increases, the deterioration phenomenon becomes less pronounced and recovery of heat transfer
coefficient occurs earlier, i.e. at lower buoyancy parameters compared to concentric annuli.