Conclusion
In previous parts, temperatures distributions of single U-pipe, double U-pipe and centered inlet heat exchangers have been investigated. According to the contours and figures of three BHEs, it can be seen that a coaxial borehole heat exchanger with centered inlet has more performance compared to others. Also in optimization part, considering the design parameters and their result on the Nusselt number and friction coefficient, it was observed that the Reynolds number has the most effect among the parameters. As the Reynolds number increases, in addition to increasing heat transfer, the pressure drop will also decrease. The other two parameters have roughly the same value. By increasing the diameter rate and stepping distance, the efficiency and design desirability will increase. According to these simulations two relations are presented to better understanding of parameters effect. Therefore, the paper presents best geometry for the highest heat transfer rate, and geometry with fin is also proposed to increase the heat transfer in borehole heat exchanger, which can be applied to engineering applications.