COMPARISON OF CORRECTION FACTORS FOR SHELL-AND-TUBE HEAT-EXCHANGERS WITH SEGMENTAL OR HELICAL BAFFLES

Heat transfer and pressure drop correction factors based on the Bell D elaware method have been compared for an optimized segmental baffle he at exchanger and a helical baffle heat exchanger In general, the resul ts showed that properly designed helical baffles offer a significant i mprovement in heat transfer while providing a reduced exchanger pressu re drop. The enhancement in heat transfer for helical baffles was refl ected by the so-called turbulence enhancement correction factor, which accounted for the increase in heat transfer observed at a critical ba ffle inclination angle of 25-degrees. As the baffle inclination angle was increased beyond this critical angle, the turbulence enhancement f actor continued to increase and eventually produced a maximum heat tra nsfer enhancement of 1.39 times that for ideal cross-flow conditions. The reduction in pressure drop due to the helical baffles was found to vary from 0. 26 to 0. 60 depending on the helical inclination angle.