The Sieder-Tate correlation for heat transfer in turbulent flow in a pipe gives \( \text{Nu} \propto \text{Re}^{0.8} \), where \( \text{Nu} \) is the Nusselt number and \( \text{Re} \) is the Reynolds number for the flow. Assuming that this relation is valid, the heat transfer coefficient varies with the pipe diameter (D) as: