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The influences of the geometrical parameters of interrupted annular groove fin mainly including the annular groove diameter, the groove arc length, and the fin spacing, on the fin side thermal-hydraulic characteristics of a finned circular tube exchanger were numerically investigated by actualizing the custom FORTRAN programing with SIMPLE algorithm in a non-orthogonal curvilinear co-ordinate system, and the regression formulas of average Nusselt number and friction factor with flow parameters and geometrical parameters were obtained. Compared with the referential plain fin, interrupted annular groove fin could significantly improve thermal performance under the same pumping power constraint, and Nusselt number is closely germane to the secondary flow, which implies that the fin side heat transfer is depended entirely on the secondary flow strength. For Nusselt number, the annular groove diameter and the groove arc length have positive effect, while the fin pitch, the groove circumferential and radial locations have negative effect. The dominant parameters influencing on friction factor in turn are the fin pitch, the groove radial location, and the annular groove diameter. The optimal annular groove diameter is screened, and found that the optimal annular groove diameter is closely related with Reynolds number under the same pumping power constraint, while under the same mass-flow rate constraint that is scarcely related with Reynolds number.

The thermal-hydraulic characteristics of a novel fin punched with curve trapezoidal vortex generators (CTVG) are investigated numerically. The effects of multi-parameters including the geometry of CTVG, the location of CTVG, and working condition on thermal performance are considered. On one hand, CTVG can availably lessen the size of tube wake zone, decrease the mechanical energy consumption and heighten the fin heat transfer ability in this area. On the other hand, the secondary flow strength is strengthened because the longitudinal vortices generated by CTVG, which efficiently enhances the heat transfer on the fin downstream CTVG. Close relationship exists between the volume-averaged secondary flow strength and the mean Nusselt number. For studied cases, the optimal circumferential location angle of ? = 90? is found, while the optimal radial location Dg is about 1.8 times the tube outside diameter. The smaller is the height or base length of CTVG, the better the thermal performance of the enhanced fin punched with CTVG. Better thermal performance is achieved as the fin spacing is about 0.24 times the tube outside diameter.