In this study, a reversed trapezoidal profile fins attachment to the tube bank heat exchanger was proposed to enhance the heat transfer performance. A validated computational fluid dynamics (CFD) model was used to investigate the flow behaviour and thermal performance of the staggered tube bank heat exchanger with reversed trapezoidal profile fins. The simulation employed the RNG k-ε model with enhanced wall treatment. The effects of fins’ angle (2°≤αtf ≤ 10°), length (0.5D ≤ Ltf ≤ 2D) and thickness (1 mm ≤ Htf ≤ 5 mm) within a range of Reynolds number (5500 ≤ Re ≤ 14500) were discussed. Nusselt number (Nu), pressure drop (ΔP) and performance evaluation criterion (PEC) were used to evaluate the heat exchanger’s performance. The results showed that both Nu and ΔP followed an increasing trend as αtf increased, which indicates a heat transfer enhancement and a larger airflow resistance. As Ltf increased from 0.5D to 2D, Nu showed a continuous increase with the maximum value obtained at Ltf = 2D. However, ΔP showed a tendency to increase and then decrease as Ltf increased, with the maximum value observed at Ltf = 1.25D. A larger thickness resulted in a higher airflow resistance penalty compared to the improvement in Nu. The thickness was recommended to be as small as possible, provided that the manufacturing process and mechanical strength requirements were met. If the adverse effect of pressure drop was not of concern, the optimal thermal–hydraulic performance (PEC) could be obtained at a larger angle, length and smaller thickness.
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